Abrégé

A simple chemical treatment process for low oxygen containing HTL biocrudes has been developed. This process reduces the content of organic acids by reacting HTL biocrude with alcohols without the need for hydrotreatment catalysts or a hydrogen source, thereby increasing biocrude stability and compatibility with petroleum fuels or petroleum distillates cuts such as marine fuels or co-processing feedstocks in commercial refineries.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/04 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par extraction
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 49/00 - Traitement des huiles d'hydrocarbures, en présence d'hydrogène ou de composés donneurs d'hydrogène, non prévu dans un seul des groupes , , , ou
• C10L 1/08 - Combustibles carbonés liquides à base essentielle de mélanges d'hydrocarbures pour allumage par compression

Abrégé

2 from the product mixture in a degasser such as a flash separator, and—separating a water phase from the at least partly degassed converted feed mixture in a first separation step of the separation, and adding washing agents in the form of an acidifying agent and a diluent to the at least partly degassed and at least partly dewatched product mixture, and separating the mixture with added washing agents into an oil rich phase, a water rich phase and a solid rich phase in a second step of the separation process, and further at least partly recovering the diluent from the oil rich phase.

Classes IPC  ?

• C10G 53/04 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par plusieurs procédés de raffinage uniquement par plusieurs étapes en série comprenant au moins une étape d'extraction
• C10G 53/10 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par plusieurs procédés de raffinage uniquement par plusieurs étapes en série comprenant au moins une étape traitement acide

Abrégé

The invention relates to a low sulphur fuel blend of a first fuel blend component containing renewable hydrocarbon component(-s) and a second fuel blend component containing hydrocarbon to form at least part of a final low sulphur fuel blend having a sulphur content of less than 0.5 wt. %, where the first fuel blend component is characterised by having the characteristics (δd1, δp1, δh1)=(17-20, 6-10, 6-10); where the first fuel blend component comprises a fuel substance comprising 70% by weight of compounds having a boiling point above 220° C. and is further characterized by having the characteristics (δd, δp, δh)=(17-20, 6-15,6-12) and a linker substance comprising one or more sulphur containing solvents characterised by having the characteristics (δd3, δp3, δh3)=(17-20, 3-6, 4-6); where the fuel substance is present in the first fuel blend component in a relative amount of 90-99.5 wt. %, and the linker substance is present in the first fuel blend component in a relative amount of 0.5 to 10 wt. %; where the second fuel blend component is characterised by having the characteristics (δd2, δp2, δh2) -(17-20, 3-5, 4-7) and selected from the group of ultra low sulfur fuel oils (ULSFO) such as RMG 180, low sulphur fuel oil, marine gas oil, marine diesel oil, vacuum gas oil, and combinations thereof, where the first fuel blend component is present in the final low sulphur fuel blend in a relative amount of up to 80 wt. %.

Classes IPC  ?

• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10L 1/02 - Combustibles carbonés liquides à base essentielle de composants formés uniquement de carbone, d'hydrogène et d'oxygène
• C10L 1/14 - Composés organiques

Abrégé

h2)=(17-20, 3-5, 4-7), where the first blend component is present in the final hydrocarbon blend in a relative amount of up to 80 wt %.

Classes IPC  ?

• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10L 1/02 - Combustibles carbonés liquides à base essentielle de composants formés uniquement de carbone, d'hydrogène et d'oxygène
• C10L 10/00 - Utilisation d'additifs à des fins particulières dans les combustibles ou les feux

Abrégé

−1 and at a temperature in the range of 150° C. to 360° C., hereby providing a partially upgraded renewable crude oil, separating the partially upgraded renewable crude oil from the first reaction zone to a partially upgraded heavy renewable oil fraction, a partially upgraded light renewable oil fraction, a water stream and a process gas stream, introducing the separated and partially upgraded heavy renewable oil fraction and separated process gas to a second reaction zone comprising at least two reactors arranged in parallel and being adapted to operate in a first and a second mode of operation, the reactors comprising dual functioning heterogeneous catalyst(-s) capable of performing a catalytic steam cracking reaction in a first mode of operation or a steam reforming reaction in a second mode of operation, where the partially upgraded heavy renewable oil fraction from the first reaction zone is contacted with the dual functioning heterogeneous catalyst and steam at a pressure of 10 to 150 bar and a temperature of 350° C. to 430° C. whereby a catalytic steam cracking of the partially upgraded heavy renewable oil is performed in the reactors in the first mode of operation, hereby providing a further upgraded heavy renewable oil fraction, while separated process gas from the first and/or second reaction zone is contacted with the dual functioning catalyst and steam at a pressure of 0.1 to 10 bar and a temperature of 350 to 600° C. in the reactors in the second mode of operation and contacted with the dual functioning catalyst, thereby producing a hydrogen enriched gas, separating the further upgraded heavy renewable oil fraction from the catalytically steam cracking reactor to at least one light renewable oil fraction, a heavy renewable oil fraction, a hydrogen rich process gas and a water phase, separating hydrogen from the hydrogen enriched gas from the catalytic steam cracking zone and/or from the catalytic steam reforming and recycling it to the first reaction zone, alternating the reactors between the first mode of operation and the second mode of operation at predetermined time intervals thereby allowing for regeneration of the heterogeneous catalyst for the catalytic steam cracking in the first mode of operation while performing the steam reforming reaction of the hydrocarbons contained in the process gas in the second mode of operation;

Classes IPC  ?

• C10G 51/04 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, uniquement par plusieurs procédés de craquage uniquement par plusieurs étapes en série ne comprenant que des étapes de craquage thermique et catalytique
• C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène
• C10G 69/04 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage catalytique en l'absence d'hydrogène
• C10G 69/08 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de réformage d'essence "naphta"
• B01J 27/22 - Carbures

Abrégé

The invention relates to a process for producing an upgraded renewable oil from renewable carbonaceous material(-s) comprising providing a low sulphur oxygen containing renewable crude oil having a sulphur content of less than 0.5 wt % and an oxygen content from about 2.0 wt to about 20 wt %, pressurising the low sulphur oxygen containing renewable crude oil to an operational pressure in the range 20 to 200 bar, adding and mixing hydrogen to the pressurized low sulphur oxygen containing crude oil, heating the oil to an operational temperature in the range 180-410° C. in one or more steps, contacting said oil with at least one heterogeneous catalyst contained in a first reaction zone, contacting the effluent from said first reaction zone with at least one heterogeneous catalyst contained in a second reaction zone, where in at least one of the heterogeneous catalysts in the first reaction zone and/or the second reaction zone is on a non-sulphided form.

Classes IPC  ?

• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive

Abrégé

The invention relates to a method of heating and cooling a feed mixture in a continuous high pressure process for transforming carbonaceous materials into liquid hydrocarbon products in a high pressure processing system adapted for processing a feed mixture at a temperature of at least 340° C. and a pressure of at least 150 bar, the high pressure processing system comprising a first and a second heat exchanger having a heat transfer fluid comprising at least 90% water, preferably at least 99% water circulating in the external part of the first and the second heat exchanger, the first heat exchanger comprising a cold internal input side and a hot internal output side, the second heat exchanger comprising a hot internal input side and a cold internal output side, the system further comprising a high pressure water heater and a high pressure water cooler between the first and the second heat exchanger, where the pressurized feed mixture is heated by feeding the feed mixture to the cold internal side of the first heat exchanger, heating and pressurizing the heat transfer fluid to a pressure of at least 240 bar and a temperature of at least 400° C. at the input to the hot external side of the first heat exchanger, where the cooled heat transfer fluid from the first heat exchanger having a temperature in the range 150 to 300° C. is further cooled to a temperature of 60 to 150° C. in the high pressure water cooler prior to entering the cold external side of the second heat exchanger, where the pressurized, heated and converted feed mixture is cooled to a temperature in the range 60 to 200° C. by feeding it to the internal side of the second heat exchanger, and where the partly heated heat transfer fluid is further heated in the high pressure water heater before entering the first heat exchanger.

Classes IPC  ?

• C10G 1/08 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive avec catalyseurs mobiles
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to a method of separating and purifying products from a hydrothermal and/or solvothermal conversion process of carbonaceous material adapted to convert a feed stream comprising carbonaceous material at a pressure of at least 100 bar and a temperature of at least 300 °C, where the converted feed stream (product mixture) comprises a mixture of CO2 containing gas, an oil phase, an aqueous phase comprising water soluble organics and dissolved salts, and inorganic solid phase; where the product mixture is cooled to a temperature in the range 40 to 250 °C, and depressurized to a pressure in the range 1 to 30 bar, the method comprising - separating a gas comprising CO2 from the product mixture in a degasser such as a flash separator, and - separating a water phase from the at least partly degassed converted feed mixture in a first separation step of the separation, and adding washing agents in the form of an acidifying agent and a diluent to the at least partly degassed and at least partly dewatered product mixture, and separating the mixture with added washing agents into an oil rich phase, a water rich phase and a solid rich phase in a second step of the separation process, and further at least partly recovering the diluent from the oil rich phase.

Classes IPC  ?

• C10G 31/06 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par chauffage, refroidissement ou traitement par la pression
• C10G 31/08 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par traitement à l'eau
• C10G 53/04 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par plusieurs procédés de raffinage uniquement par plusieurs étapes en série comprenant au moins une étape d'extraction

Abrégé

2 22 from the product mixture in a degasser such as a flash separator, and - separating a water phase from the at least partly degassed converted feed mixture in a first separation step of the separation, and adding washing agents in the form of an acidifying agent and a diluent to the at least partly degassed and at least partly dewatered product mixture, and separating the mixture with added washing agents into an oil rich phase, a water rich phase and a solid rich phase in a second step of the separation process, and further at least partly recovering the diluent from the oil rich phase.

Classes IPC  ?

• C10G 31/06 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par chauffage, refroidissement ou traitement par la pression
• C10G 31/08 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par traitement à l'eau
• C10G 33/00 - Déshydratation ou désémulsification des huiles d'hydrocarbures
• C10G 53/04 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par plusieurs procédés de raffinage uniquement par plusieurs étapes en série comprenant au moins une étape d'extraction
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to producing upgraded renewable oil. Renewable crude oil is provided whose oxygen content, water content, and total acid number are within predetermined ranges. Respective fractions of the oil have boiling points below 350° C. and above 450° C. After the oil is pressurized, and hydrogen is added, the mixture is heated and contacted with a heterogeneous catalyst in a first reaction zone with weight based hourly space velocity (WHSV) of 0.1 to 1 h-1. The resultant partially hydrogenated and deoxygenated oil is further heated and contacted with a heterogeneous catalyst in a second reaction zone at WHSV of 0.1 to 1.5 h-1. Low and high boiling point liquid hydrocarbon fractions of the product of the second reaction zone are sent to third and fourth reaction zones, respectively, to be contacted with hydrogen and a heterogeneous catalyst under respective heating conditions and WHSV of 0.1 to 1 h-1.

Classes IPC  ?

• C10G 65/04 - Traitement des huiles d'hydrocarbures, uniquement par plusieurs procédés d'hydrotraitement uniquement par plusieurs étapes en série ne comprenant que des étapes de raffinage
• C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to a low sulphur fuel blend of a first fuel blend component containing renewable hydrocarbon component(-s) and a second fuel blend component containing hydrocarbon to form at least part of a final low sulphur fuel blend having a sulphur content of less than 0,5 wt.%, where the first fuel blend component is characterised by having the characteristics (d d1 , d ?1 , d h1 ) = (17-20, 6-10, 6-10); where the first fuel blend component comprises a fuel substance comprising 70 % by weight of compounds having a boiling point above 220 °C and is further characterized by having the characteristics (d d , d ? , d h ) = (17-20, 6-15, 6-12) and a linker substance comprising one or more sulphur containing solvents characterised by having the characteristics ( d d3 ,d ?3 , d h3 )= (17-20, 3-6, 4-6); where the fuel substance is present in the first fuel blend component in a relative amount of 90-99,5 wt.%, and the linker substance is present in the first fuel blend component in a relative amount of 0.5 to 10 wt.%; where the second fuel blend component is characterised by having the characteristics (d d2 , d ?2 , d h 2) = (17-20, 3-5, 4-7) and selected from the group of ultra low sulfur fuel oils (ULSFO) such as RMG 180, low sulphur fuel oil, marine gas oil, marine diesel oil, vacuum gas oil, and combinations thereof, where the first fuel blend component is present in the final low sulphur fuel blend in a relative amount of up to 80 wt.%.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10L 1/02 - Combustibles carbonés liquides à base essentielle de composants formés uniquement de carbone, d'hydrogène et d'oxygène
• C10L 1/10 - Combustibles carbonés liquides contenant des additifs

Abrégé

The invention relates to a hydrocarbon blend for input to a refinery and comprising a first blend component containing a renewable hydrocarbon component and a second blend component containing petroleum derived hydrocarbon to form at least part of a final hydrocarbon blend for processing in a refinery where the first blend component is characterized by comprising a hydrocarbon substance with at least 70 % by weight having a boiling point above 220 °C and by having the characteristics (d d1 , d ?1 , d h1 ) = (17-20, 6-12, 6-12) and; where the second blend component is characterised by having the characteristics (d ?2 , d ?2 , d h2 ) = (17-20, 3-5, 4-7), where the first blend component is present in the final hydrocarbon blend in a relative amount of up to 80 wt %.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10L 1/02 - Combustibles carbonés liquides à base essentielle de composants formés uniquement de carbone, d'hydrogène et d'oxygène
• C10L 1/04 - Combustibles carbonés liquides à base essentielle de mélanges d'hydrocarbures

Abrégé

δd1d1 , δρ1ρ1 , δh1h1 )δdd , δρρ , δhh δd3d3 ,δρ3ρ3 , δh3h3 δd2d2 , δρ2ρ2 , δhh 22) = (17-20, 3-5, 4-7) and selected from the group of ultra low sulfur fuel oils (ULSFO) such as RMG 180, low sulphur fuel oil, marine gas oil, marine diesel oil, vacuum gas oil, and combinations thereof, where the first fuel blend component is present in the final low sulphur fuel blend in a relative amount of up to 80 wt.%.

Classes IPC  ?

• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10L 1/18 - Composés organiques contenant de l'oxygène
• C10L 1/02 - Combustibles carbonés liquides à base essentielle de composants formés uniquement de carbone, d'hydrogène et d'oxygène

Abrégé

δd1d1 , δρ1ρ1 , δh1h1 δά2ά2 , δρ2ρ2 , δh2h2 h2 ) = (17-20, 3-5, 4-7), where the first blend component is present in the final hydrocarbon blend in a relative amount of up to 80 wt %.

Classes IPC  ?

• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10L 1/18 - Composés organiques contenant de l'oxygène
• C10L 1/02 - Combustibles carbonés liquides à base essentielle de composants formés uniquement de carbone, d'hydrogène et d'oxygène

Abrégé

The invention relates to a catalytic process for upgrading a renewable crude oil produced from biomass and/or waste comprising providing a renewable crude oil and pressurizing it to a pressure in the range in the range 60 to 150 bar, contacting the pressurized renewable crude oil with hydrogen and at least one heterogeneous catalyst contained in a first reaction zone at a weight based hourly space velocity (WHSV) in the range 0.1 to 2.0 h-1 and at a temperature in the range of 150 °C to 360 °C, hereby providing a partially upgraded renewable crude oil, separating the partially upgraded renewable crude oil from the first reaction zone to a partially upgraded heavy renewable oil fraction, a partially upgraded light renewable oil fraction, a water stream and a process gas stream, introducing the separated and partially upgraded heavy renewable oil fraction and separated process gas to a second reaction zone comprising at least two reactors arranged in parallel and being adapted to operate in a first and a second mode of operation, the reactors comprising dual functioning heterogeneous catalyst(-s) capable of performing a catalytic steam cracking reaction in a first mode of operation or a steam reforming reaction in a second mode of operation, where the partially upgraded heavy renewable oil fraction from the first reaction zone is contacted with the dual functioning heterogeneous catalyst and steam at a pressure of 10 to 150 bar and a temperature of 350 °C to 430 °C whereby a catalytic steam cracking of the partially upgraded heavy renewable oil is performed in the reactors in the first mode of operation, hereby providing a further upgraded heavy renewable oil fraction, while separated process gas from the first and/or second reaction zone is contacted with the dual functioning catalyst and steam at a pressure of 0.1 to 10 bar and a temperature of 350 to 600 °C in the reactors in the second mode of operation and contacted with the dual functioning catalyst, thereby producing a hydrogen enriched gas, separating the further upgraded heavy renewable oil fraction from the catalytically steam cracking reactor to at least one light renewable oil fraction, a heavy renewable oil fraction, a hydrogen rich process gas and a water phase, separating hydrogen from the hydrogen enriched gas from the catalytic steam cracking zone and/or from the catalytic steam reforming and recycling it to the first reaction zone, alternating the reactors between the first mode of operation and the second mode of operation at predetermined time intervals thereby allowing for regeneration of the heterogeneous catalyst for the catalytic steam cracking in the first mode of operation while performing the steam reforming reaction of the hydrocarbons contained in the process gas in the second mode of operation;

Classes IPC  ?

• C01B 3/32 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds
• C10G 49/00 - Traitement des huiles d'hydrocarbures, en présence d'hydrogène ou de composés donneurs d'hydrogène, non prévu dans un seul des groupes , , , ou
• C10G 51/06 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, uniquement par plusieurs procédés de craquage uniquement par plusieurs étapes en parallèle
• C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène

Abrégé

-1-1 and at a temperature in the range of 150 °C to 360 °C, hereby providing a partially upgraded renewable crude oil, separating the partially upgraded renewable crude oil from the first reaction zone to a partially upgraded heavy renewable oil fraction, a partially upgraded light renewable oil fraction, a water stream and a process gas stream, introducing the separated and partially upgraded heavy renewable oil fraction and separated process gas to a second reaction zone comprising at least two reactors arranged in parallel and being adapted to operate in a first and a second mode of operation, the reactors comprising dual functioning heterogeneous catalyst(-s) capable of performing a catalytic steam cracking reaction in a first mode of operation or a steam reforming reaction in a second mode of operation, where the partially upgraded heavy renewable oil fraction from the first reaction zone is contacted with the dual functioning heterogeneous catalyst and steam at a pressure of 10 to 150 bar and a temperature of 350 °C to 430 °C whereby a catalytic steam cracking of the partially upgraded heavy renewable oil is performed in the reactors in the first mode of operation, hereby providing a further upgraded heavy renewable oil fraction, while separated process gas from the first and/or second reaction zone is contacted with the dual functioning catalyst and steam at a pressure of 0.1 to 10 bar and a temperature of 350 to 600 °C in the reactors in the second mode of operation and contacted with the dual functioning catalyst, thereby producing a hydrogen enriched gas, separating the further upgraded heavy renewable oil fraction from the catalytically steam cracking reactor to at least one light renewable oil fraction, a heavy renewable oil fraction, a hydrogen rich process gas and a water phase, separating hydrogen from the hydrogen enriched gas from the catalytic steam cracking zone and/or from the catalytic steam reforming and recycling it to the first reaction zone, alternating the reactors between the first mode of operation and the second mode of operation at predetermined time intervals thereby allowing for regeneration of the heterogeneous catalyst for the catalytic steam cracking in the first mode of operation while performing the steam reforming reaction of the hydrocarbons contained in the process gas in the second mode of operation;

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds
• C01B 3/32 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air
• C10G 51/06 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, uniquement par plusieurs procédés de craquage uniquement par plusieurs étapes en parallèle
• C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 49/00 - Traitement des huiles d'hydrocarbures, en présence d'hydrogène ou de composés donneurs d'hydrogène, non prévu dans un seul des groupes , , , ou

Abrégé

The invention relates to a method of separating and purifying products from a high pressure processing system adapted for processing a feed stream comprising carbonaceous material at a pressure of at least 150 bar and a temperature of at least 300° C., where the converted feed stream (product mixture) is cooled to a temperature in the range 50 to 250° C., and depressurized to a pressure in the range 1 to 150 bar, the method comprising separating the depressurized product mixture in gas phase, an oil phase (liquid hydrocarbon), and a water phase comprising water soluble organics, dissolved salts and optionally suspended particles in a first phase separator and purifying the oil phase from the first phase separator by mixing it with one or more washing agents, at least one of which comprises water, and separating the oil phase from the one or more washing agents in a further separation step.

Classes IPC  ?

• C10G 31/06 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par chauffage, refroidissement ou traitement par la pression
• C10G 31/08 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par traitement à l'eau
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 53/10 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par plusieurs procédés de raffinage uniquement par plusieurs étapes en série comprenant au moins une étape traitement acide
• C10G 67/14 - Traitement des huiles d'hydrocarbures, uniquement par au moins un procédé d'hydrotraitement et au moins un procédé de raffinage en l'absence d'hydrogène uniquement par plusieurs étapes en série comprenant au moins deux étapes de raffinage différentes, en l'absence d'hydrogène
• C10G 33/00 - Déshydratation ou désémulsification des huiles d'hydrocarbures

Abrégé

The invention relates to a pressure reduction unit for use in processing equipment handling high pressure fluid, where the pressure reduction unit comprises at least one inlet and an outlet, the pressure reduction unit being adapted to receive a pressurized fluid at process pressure level at the inlet, being adapted to isolate the received pressurized fluid from the upstream process and from the outlet and being adapted to reduce the pressure of the fluid to a lower predetermined level and further being adapted to output the fluid through the outlet while still isolated towards the upstream process.

Classes IPC  ?

• F15B 3/00 - Amplificateurs ou convertisseurs de pression de fluide, p. ex. échangeurs de pressionTransmission de la pression d'un système à fluide à un autre, sans contact entre les fluides
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• G05D 16/20 - Commande de la pression d'un fluide caractérisée par l'utilisation de moyens électriques
• G05D 16/00 - Commande de la pression d'un fluide
• F04B 9/117 - "Machines" ou pompes à piston caractérisées par les moyens entraînants ou entraînés liés à leurs organes de travail les moyens étant à fluide le fluide étant liquide avec plusieurs chambres de pompage les organes de pompage n'étant pas liés mécaniquement entre eux

Abrégé

The invention relates to a pressurization unit for use in processing equipment handling high pressure fluid, where the pressurization unit comprises at least one inlet and an outlet, the pressurization unit being adapted to receive a feed fluid at a feed pressure level at the inlet, being adapted to isolate the received feed fluid from the inlet and from the outlet and being adapted to increase the pressure of the fluid to a higher predetermined level and further being adapted to output the fluid through the outlet into the high pressure process while still isolated towards the inlet.

Classes IPC  ?

• F04B 15/00 - Pompes adaptées pour travailler avec des fluides particuliers, p. ex. grâce à l'emploi de matériaux spécifiés pour la pompe elle-même ou certaines de ses parties
• F04B 49/00 - Commande des "machines", pompes ou installations de pompage ou mesures de sécurité les concernant non prévues dans les groupes ou présentant un intérêt autre que celui visé par ces groupes
• F04B 49/06 - Commande utilisant l'électricité
• F04B 49/08 - Régulation par la pression de refoulement
• F04B 49/22 - Commande des "machines", pompes ou installations de pompage ou mesures de sécurité les concernant non prévues dans les groupes ou présentant un intérêt autre que celui visé par ces groupes par clapets
• F04B 53/08 - RefroidissementChauffagePrévention du gel
• G05D 16/20 - Commande de la pression d'un fluide caractérisée par l'utilisation de moyens électriques

Abrégé

The invention relates to a process for producing an upgraded renewable oil from renewable carbonaceous material(-s) comprising providing an oxygen containing renewable crude oil having an oxygen content in the range of 3.0 to 20 % by weight, a water content of less than 1.5 wt. %, a total acid number in the range from 5 to 80 mg KOH/g, a fraction of the oil having a boiling point below than 350 °C of less than 70 % by weight, and a residue fraction having a boiling point of more than 450 °C of at least 10 %by weight, pressurisingthe oxygen containing renewable crude oil to an operational pressure in the range 60 to 200 bar; adding and mixing hydrogen to the pressurized oxygen containing renewable crude oil,contacting the pressurized mixture with at least one heterogeneous catalyst contained in a first reaction zone at a temperature of 260 to 350 °C having a weight based hourly space velocity (WHSV) in the range 0.1 to 1 h-1so as to produce a partially hydrogenated and deoxygenated oil,separating water, gas and optionally a low boiling fraction from the partially hydrogenated and deoxygenatedoil from the first reaction zone, heating the partially hydrogenated and deoxygenated oil from the first reaction zone to a temperature in the range 350 to 400 °C,contacting the partially hydrogenated and deoxygenated oil with at least one heterogeneous catalysts in a second reaction zone at a temperature of 350 to 400 °C at weight based hourly space velocity (WHSV) in the range 0.1 to 1.5 h-1, separating the product from the second reaction zone into a at least a gas fraction, a water fraction, a low boiling point renewable liquid hydrocarbon fraction and a high boiling point renewable liquid hydrocarbon fraction, contacting the low boiling point fraction from the second reaction zone with hydrogen and one or more heterogeneous catalysts at a temperature in the range 350 to 390 °C in a third reaction zone having a weight based space velocity in the range 0.1 to 1 h-1, thereby producing a first product stream and contacting the high boiling point oil fraction with hydrogen and one or more heterogeneous catalysts at a temperature in the range 360-420 °C in a fourth reaction zone having a weight based space velocity in the range 0.1 to 1 h-1, thereby producing a second product stream.

Classes IPC  ?

• C10G 65/04 - Traitement des huiles d'hydrocarbures, uniquement par plusieurs procédés d'hydrotraitement uniquement par plusieurs étapes en série ne comprenant que des étapes de raffinage
• C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon

Abrégé

The invention relates to a process for producing upgraded renewable oil from renewable carbonaceous material(-s) comprising providing and pressurising oxygen-containing renewable crude oil; adding hydrogen to the pressurized oxygen-containing renewable crude oil, contacting the pressurized mixture with heterogeneous catalyst(s) in a first reaction zone to produce a partially hydrogenated and deoxygenated oil; separating water, gas and optional low boiling fraction from the partially hydrogenated and deoxygenated oil; heating and contacting the partially hydrogenated and deoxygenated oil with heterogeneous catalyst(s) in a second reaction zone; separating the second reaction zone product into a gas fraction, water fraction, and low and high boiling point renewable liquid hydrocarbon fractions; contacting the low boiling point fraction with hydrogen and heterogeneous catalyst(s) in a third reaction zone, producing a first product stream; and contacting the high boiling point oil fraction with hydrogen and heterogeneous catalysts in a fourth reaction zone, producing a second product stream.

Classes IPC  ?

• C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 65/04 - Traitement des huiles d'hydrocarbures, uniquement par plusieurs procédés d'hydrotraitement uniquement par plusieurs étapes en série ne comprenant que des étapes de raffinage

Abrégé

Products from a high pressure processing system are separated and purified. The processing system is adapted for pressurizing and heating a feed mixture comprising carbonaceous material(-s) in the presence of homogeneous catalysts and liquid organic compounds to produce a converted feed mixture. The converted feed mixture is cooled and depressurized, and then separated into: a gas phase, an oil phase, and a water phase comprising liquid organic compounds and dissolved homogeneous catalysts comprising potassium and/or sodium. The liquid organic compounds and dissolved homogenous catalysts are at least partly recovered from said water phase, thereby producing a first water phase stream enriched in liquid organic compounds and homogeneous catalysts and a second water phase stream depleted in liquid organic compounds and homogeneous catalysts. The first water phase is at least partly recycled to the feed mixture, with a bleed stream being withdrawn therefrom prior to recycling.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/04 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par extraction
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc

Abrégé

The invention relates to a method of separating and purifying products from a high pressure processing system adapted for processing a feed mixture comprising carbonaceous material(-s) at a pressure of from about 150 bar to about 400 bar and a temperature from about 300⁰C to about 430 ⁰C in the presence of homogeneous catalysts in the form of potassium and/or sodium in a concentration of at least 0,5 % by weight and liquid organic compounds in a concentration from about 5 % to about 40 % by weight in a predefined time thereby producing a converted feed mixture, wherein the converted feed mixture is cooled to a temperature in the range 50 to 250°C, and depressurized to a pressure in the range 1 to 150 bar, and where the converted feed mixture is separated in to a gas phase comprising carbon dioxide, hydrogen, and methane, an oil phase comprising oil phase liquid organic compounds, and a water phase comprising water phase liquid organic compounds, dissolved salts and optionally suspended particles, where the water phase liquid organic compounds and dissolved homogenous catalysts in the form of potassium and/or sodium areat least partly recovered from said water phase thereby producing a first water phase stream enriched in water phase liquid organic compounds and homogeneous catalysts in the form of potassium and sodium, and a second water phase stream depleted in water phase liquid organic compounds and homogeneous catalysts in the form of potassium and sodium, where the first water phase is at least partly recycled to said the feed mixture to provide at least part of said liquid organic compounds and homogeneous catalysts in the feed mixture,and where further a bleed stream is withdrawn from said water phase enriched in water phase liquid organic compounds and homogeneous catalysts in the form of potassium and sodium prior to recycling said first recycle stream to the feed mixture.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• B01J 47/00 - Procédés d'échange d'ions en généralAppareillage à cet effet
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• C10G 31/06 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par chauffage, refroidissement ou traitement par la pression
• C10G 31/08 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par traitement à l'eau
• C02F 1/42 - Traitement de l'eau, des eaux résiduaires ou des eaux d'égout par échange d'ions

Abrégé

The invention relates to a processing system comprising at least one pressurization device; at least one separation device; at least one conversion section;at least one valve unit between the at least one pressurization device and the at least one conversion part;at least one valve unit between the at least one conversion part and the at least one separation unit;where the conversion section comprises at least two parallel conversion units;where each conversion unit comprises at least one heating device, at least one reactor device, and at least one cooling device.

Classes IPC  ?

• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 31/06 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par chauffage, refroidissement ou traitement par la pression
• C10G 53/16 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par plusieurs procédés de raffinage uniquement par plusieurs étapes en parallèle

Abrégé

The invention relates to a method of separating and purifying products from a high pressure processing system adapted for processing a feed mixture comprising carbonaceous material(-s) at a pressure of from about 150 bar to about 400 bar and a temperature from about 300°C to about 430 °C in the presence of homogeneous catalysts in the form of potassium and/or sodium in a concentration of at least 0,5 % by weight and liquid organic compounds in a concentration from about 5 % to about 40 % by weight in a predefined time thereby producing a converted feed mixture, wherein the converted feed mixture is cooled to a temperature in the range 50 to 250°C, and depressurized to a pressure in the range 1 to 150 bar, and where the converted feed mixture is separated in to a gas phase comprising carbon dioxide, hydrogen, and methane, an oil phase comprising oil phase liquid organic compounds, and a water phase comprising water phase liquid organic compounds, dissolved salts and optionally suspended particles, where the water phase liquid organic compounds and dissolved homogenous catalysts in the form of potassium and/or sodium areat least partly recovered from said water phase thereby producing a first water phase stream enriched in water phase liquid organic compounds and homogeneous catalysts in the form of potassium and sodium, and a second water phase stream depleted in water phase liquid organic compounds and homogeneous catalysts in the form of potassium and sodium, where the first water phase is at least partly recycled to said the feed mixture to provide at least part of said liquid organic compounds and homogeneous catalysts in the feed mixture,and where further a bleed stream is withdrawn from said water phase enriched in water phase liquid organic compounds and homogeneous catalysts in the form of potassium and sodium prior to recycling said first recycle stream to the feed mixture.

Classes IPC  ?

• B01J 47/00 - Procédés d'échange d'ions en généralAppareillage à cet effet
• C02F 1/42 - Traitement de l'eau, des eaux résiduaires ou des eaux d'égout par échange d'ions
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 31/06 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par chauffage, refroidissement ou traitement par la pression
• C10G 31/08 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par traitement à l'eau

Abrégé

The invention relates to a processing system comprising at least one pressurization device; at least one separation device; at least one conversion section;at least one valve unit between the at least one pressurization device and the at least one conversion part;at least one valve unit between the at least one conversion part and the at least one separation unit;where the conversion section comprises at least two parallel conversion units;where each conversion unit comprises at least one heating device, at least one reactor device, and at least one cooling device.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 31/06 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par chauffage, refroidissement ou traitement par la pression
• C10G 53/16 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, par plusieurs procédés de raffinage uniquement par plusieurs étapes en parallèle

Abrégé

The invention relates to a processing system comprising at least one pressurization device; at least one separation device; at least one conversion section; at least one valve unit between the at least one pressurization device and the at least one conversion part; at least one valve unit between the at least one conversion part and the at least one separation unit; where the conversion section comprises at least two parallel conversion units; where each conversion unit comprises at least one heating device, at least one reactor device, and at least one cooling device.

Classes IPC  ?

• C10G 65/14 - Traitement des huiles d'hydrocarbures, uniquement par plusieurs procédés d'hydrotraitement uniquement par plusieurs étapes en parallèle
• B01J 19/24 - Réacteurs fixes sans élément interne mobile
• B01J 19/00 - Procédés chimiques, physiques ou physico-chimiques en généralAppareils appropriés

Abrégé

The invention relates to a method of separating and purifying products from a high pressure processing system adapted for processing a feed stream comprising carbonaceous material at a pressure of at least 150 bar and a temperature of at least 300°C, where the converted feed stream (product mixture) is cooled to a temperature in the range 50 to 250 °C, and depressurized to a pressure in the range 1 to 150 bar, the method comprising separating the depressurized product mixture in gas phase, an oil phase (liquid hydrocarbon), and a water phase comprising water soluble organics, dissolved salts and optionally suspended particles in a first phase separator and purifying the oil phase from the first phase separator by mixing it with one or more washing agents, at least one of which comprises water, and separating the oil phase from the one or more washing agents in a further separation step.

Classes IPC  ?

• C10G 1/08 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive avec catalyseurs mobiles
• C10G 17/02 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, avec des acides, des composés libérant un acide ou des liquides contenant un acide, p. ex. avec une boue acide avec des acides ou des liquides contenant un acide, p. ex. avec une boue acide
• C10G 31/06 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par chauffage, refroidissement ou traitement par la pression
• C10G 31/08 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par traitement à l'eau

Abrégé

The invention relates to a method of separating and purifying products from a high pressure processing system adapted for processing a feed stream comprising carbonaceous material at a pressure of at least 150 bar and a temperature of at least 300°C, where the converted feed stream (product mixture) is cooled to a temperature in the range 50 to 250 °C, and depressurized to a pressure in the range 1 to 150 bar, the method comprising separating the depressurized product mixture in gas phase, an oil phase (liquid hydrocarbon), and a water phase comprising water soluble organics, dissolved salts and optionally suspended particles in a first phase separator and purifying the oil phase from the first phase separator by mixing it with one or more washing agents, at least one of which comprises water, and separating the oil phase from the one or more washing agents in a further separation step.

Classes IPC  ?

• C10G 31/06 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par chauffage, refroidissement ou traitement par la pression
• C10G 31/08 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, par des méthodes non prévues ailleurs par traitement à l'eau
• C10G 1/08 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive avec catalyseurs mobiles
• C10G 17/02 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, avec des acides, des composés libérant un acide ou des liquides contenant un acide, p. ex. avec une boue acide avec des acides ou des liquides contenant un acide, p. ex. avec une boue acide

Produits et services

Chemical products for industrial, scientific and photographic purposes; chemical products for use in agriculture, horticulture and forestry; synthetic resins, unprocessed; plastics, unprocessed; manures; nutrients for plants; nutrients for algae; fire extinguishing compositions; tempering and soldering preparations; chemical substances for preserving foodstuffs; tanning substances; adhesives for industrial use; industrial organic chemicals; chemicals for use in the oil industry; chemicals for use in the refining of oils; oil-separating chemicals; chemicals for use in the treatment of oils; chemical additives; additives, chemical, to motor fuel; gasoline additives; chemical additives for diesel fuels; chemical additives for oils; hydraulic fluids for use in the oil industry; chemical fluids for use in the oil industry; fluids to use as additives in the oil industry; fluids to use as additives in the oil industry in order to mix oils; chemical additives for lubricants; chemical preparations and organic substances for use in the manufacture of plastics and /or bio-plastic; additives (chemical -) for use in plastics and /or bio-plastic; carbon dioxide [other than for medical or veterinary use]; hydrocarbons; gases for industrial purposes; refrigerant chemicals; additives (chemical -) for cooling agents; petrol additives [petrochemical]. Mineral oils and greases for industrial purposes [not for fuel]; lubricants; compositions for absorbing, dust wetting and controlling of dust; fuels and illuminants; candles and wicks for lighting; fuel; biofuels; biomass fuel; fuel for ships, trucks, trains and aircrafts; non-chemical fuel additives; fuel oil; oil based lubricants; oils derived from biomass and/or other organic matters and by-products; synthetic oils; mineral oils; carbon dioxide for lighting; solidified gases [fuel]; liquefied gases for driving motor vehicles and means of transport; gases for use in heating; gas for lighting; fuels and biofuels blended with chemicals and/or biological products; renewable fuel. Treatment and processing of material and goods, namely, processing of oil and/or of hydrocarbons and/or hydrocarbon compounds and/or gases and/or water from biomass and/or other organic material; treatment and processing of material and goods, namely, conversion of biomass and/or other organic material for fuel and/or biomass-fuel and/or hydrocarbons and/or hydrocarbon compounds and/or gases and/or water; oil liquefaction; recovery of hydrocarbons from biomass or other organic material; processing of hydrocarbons; processing of organic chemical liquids and material; recycling of waste; chemical recycling of waste products; chemical treatment of waste products; chemical recycling of waste products; refining services; processing of oil; refining of oil; production, treatment and refinement of fuel, diesel fuel, biofuel and/or biodiesel fuel for others; treatment and processing of plastics; production of chemicals and other material for use in the production of plastics and/or bio-plastics; recovery of hydrocarbons and other gases and chemicals from biomass and other organic material; providing information, advice and consultancy in connection with the aforementioned services. Science and technology services and research and design relating thereto; industrial analysis and research; design and development of computer hardware and computer software; scientific, technological and research consultation in the field of fuels, diesel fuel, biofuel and biodiesel fuel; analysis and testing for oil workings; analysis for oil-field exploitation; analysis and testing services for the oil industry; analysis and testing services for the biofuels industry; analysis and testing services in the field of oil exploration; analysis and testing services in the field of oil exploitation; analysis and testing services in the field of exploitation of biomass and other organic material; research in the field of energy; technological consultancy in the fields of energy production and use; engineering services in the field of energy technology; technological consultancy in the fields of biomass exploitation; design of plants for others for the use of biomass and other organic material in connection with the production of oil and / or fuel and/or biofuel and / or hydrocarbons and / or hydrocarbon compounds and / or gases and / or water; design of plants for the production of chemical products for industrial purposes and for agricultural, horticultural and forestry applications for others; research and development of new products for others in the field of plastic materials and bio-plastic materials; providing information, advice and consultancy services in relation to all the aforementioned services.

Abrégé

ABSTRACTThe invention relates to a method of heating and cooling a feed mixture in a continuous high pressure process for transforming carbonaceous materials into hydrocarbons in a high pressure processing system , the high pressure processing system comprising first and second heat exchangers having a heat transfer fluid circulating therethrough, a high pressure water heater and a high pressure water cooler between the two heat exchangers, where a pressurized feed mixture is heated in the first heat exchanger, the heat transfer fluid is heated and pressurized at the input to the first heat exchanger, where cooled heat transfer fluid from the first heat exchanger is further cooled in the high pressure water cooler prior to entering the second heat exchanger to cool a converted feed mixture, and the partly heated heat transfer fluid is further heated in the high pressure water heater before re-entering the first heat exchanger.Date Recue/Date Received 2020-09-28

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• F27B 5/14 - Aménagement des dispositifs de chauffage
• F27B 9/06 - Fours dans lesquels la charge est déplacée mécaniquement, p. ex. du type tunnel Fours similaires dans lesquels la charge se déplace par gravité chauffés sans contact entre gaz de combustion et la chargeFours dans lesquels la charge est déplacée mécaniquement, p. ex. du type tunnel Fours similaires dans lesquels la charge se déplace par gravité chauffés électriquement
• F27B 9/12 - Fours dans lesquels la charge est déplacée mécaniquement, p. ex. du type tunnel Fours similaires dans lesquels la charge se déplace par gravité avec dispositions particulières pour le préchauffage ou le refroidissement de la charge

Abrégé

The invention relates to a method of heating and cooling a feed mixture in a continuous high pressure process for transforming carbonaceous materials into liquid hydrocarbon products in a high pressure processing system adapted for processing a feed mixture at a temperature of at least 340°C and a pressure of at least 150 bar, the high pressure processing system comprising a first and a second heat exchanger having a heat transfer fluid comprising at least 90 % water, preferably at least 99 % water circulating in the external part of the first and the second heat exchanger, the first heat exchanger comprising a cold internal input side and a hot internal output side, the second heat exchanger comprising a hot internal input side and a cold internal output side, the system further comprising a high pressure water heater and a high pressure water cooler between the first and the second heat exchanger, where the pressurized feed mixture is heated by feeding the feed mixture to the cold internal side of the first heat exchanger, heating and pressurizing the heat transfer fluid to a pressure of at least 240 bar and a temperature of at least 400 °C at the input to the hot external side of the first heat exchanger, where the cooled heat transfer fluid from the first heat exchanger having a temperature in the range 150 to 300 °C is further cooled to a temperature of 60 to 150 °C in the high pressure water cooler prior to entering the cold external side of the second heat exchanger, where the pressurized, heated and converted feed mixture is cooled to a temperature in the range 60 to 200 °C by feeding it to the internal side of the second heat exchanger, and where the partly heated heat transfer fluid is further heated in the high pressure water heater before entering the first heat exchanger.

Classes IPC  ?

• C10J 3/78 - Appareils à haute pression
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Produits et services

Chemical products for industrial, scientific and photographic purposes; chemical products for use in agriculture, horticulture and forestry; synthetic resins, unprocessed; plastics, unprocessed; manures; nutrients for plants; nutrients for algae; fire extinguishing compositions; tempering and soldering preparations; chemical substances for preserving foodstuffs; tanning substances; adhesives for industrial use; industrial organic chemicals; chemicals for use in the oil industry; chemicals for use in the refining of oils; oil-separating chemicals; chemicals for use in the treatment of oils; chemical additives; additives, chemical, to motor fuel; gasoline additives; chemical additives for diesel fuels; chemical additives for oils; hydraulic fluids for use in the oil industry; chemical fluids for use in the oil industry; fluids to use as additives in the oil industry; fluids to use as additives in the oil industry in order to mix oils; chemical additives for lubricants; chemical preparations and organic substances for use in the manufacture of plastics and/or bio-plastic; additives (chemical -) for use in plastics and/or bio-plastic; carbon dioxide [other than for medical or veterinary use]; hydrocarbons; solidified gases for industrial purposes; liquefied gases for industrial purposes, not to use as fuel; refrigerant chemicals; additives (chemical -) for cooling agents; petrol additives [petrochemical]. Mineral oils and greases for industrial purposes [not for fuel]; lubricants; compositions for absorbing, dust wetting and controlling of dust; fuels and illuminants; candles and wicks for lighting; fuel; biofuels; biomass fuel; fuel for ships, trucks, trains and aircrafts; non-chemical fuel additives; fuel oil; oil based lubricants; oils derived from biomass and/or other organic matters and by-products; synthetic oils; mineral oils; carbon dioxide for lighting; solidified gases [fuel]; liquefied gases for driving motor vehicles and means of transport; gases for use in heating; gas for lighting; gases for industrial purposes, for use as fuel; fuels and biofuels blended with chemicals and/or biological products; renewable fuel. Treatment and processing of material and goods, namely, processing of oil and/or of hydrocarbons and/or hydrocarbon compounds and/or gasses and/or water from biomass and/or other organic material; treatment and processing of material and goods, namely, conversion of biomass and/or other organic material for fuel and/or biomass-fuel and/or hydrocarbons and/or hydrocarbon compounds and/or gasses and/or water; oil liquefaction; recovery of hydrocarbons from biomass or other organic material; processing of hydrocarbons; processing of organic chemical liquids and material; recycling of waste; chemical recycling of waste products; chemical treatment of waste products; chemical recycling of waste products; refining services; processing of oil; refining of oil; production, treatment and refinement of fuel, diesel fuel, biofuel and/or biodiesel fuel for others; treatment and processing of plastics; production of chemicals and other material for use in the production of plastics and/or bio-plastics; recovery of hydrocarbons and other gasses and chemicals from biomass and other organic material; providing information, advice and consultancy in connection with the aforementioned services.

Abrégé

The invention relates to a pressure reduction unit for use in processing equipment handling high pressure fluid, where the pressure reduction unit comprises at least one inlet and an outlet, the pressure reduction unit being adapted to receive a pressurized fluid at process pressure level at the inlet, being adapted to isolate the received pressurized fluid from the upstream process and from the outlet and being adapted to reduce the pressure of the fluid to a lower predetermined level and further being adapted to output the fluid through the outlet while still isolated towards the upstream process.

Classes IPC  ?

• F04D 13/00 - Installations ou systèmes de pompage
• F15B 13/00 - Parties constitutives des systèmes de servomoteurs
• G05D 16/20 - Commande de la pression d'un fluide caractérisée par l'utilisation de moyens électriques

Abrégé

The invention relates to a pressurization unit for use in processing equipment handling high pressure fluid, where the pressurization unit comprises at least one inlet and an outlet, the pressurization unit being adapted to receive a feed fluid at a feed pressure level at the inlet, being adapted to isolate the received feed fluid from the inlet and from the outlet and being adapted to increase the pressure of the fluid to a higher predetermined level and further being adapted to output the fluid through the outlet into the high pressure process while still isolated towards the inlet.

Classes IPC  ?

• G05D 16/20 - Commande de la pression d'un fluide caractérisée par l'utilisation de moyens électriques

Abrégé

The invention relates to a pressurization unit for use in processing equipment handling high pressure fluid, where the pressurization unit comprises at least one inlet and an outlet, the pressurization unit being adapted to receive a feed fluid at a feed pressure level at the inlet, being adapted to isolate the received feed fluid from the inlet and from the outlet and being adapted to increase the pressure of the fluid to a higher predetermined level and further being adapted to output the fluid through the outlet into the high pressure process while still isolated towards the inlet.

Classes IPC  ?

• G05D 16/20 - Commande de la pression d'un fluide caractérisée par l'utilisation de moyens électriques

Abrégé

The invention relates to a pressure reduction unit for use in processing equipment handling high pressure fluid, where the pressure reduction unit comprises at least one inlet and an outlet, the pressure reduction unit being adapted to receive a pressurized fluid at process pressure level at the inlet, being adapted to isolate the received pressurized fluid from the upstream process and from the outlet and being adapted to reduce the pressure of the fluid to a lower predetermined level and further being adapted to output the fluid through the outlet while still isolated towards the upstream process.

Classes IPC  ?

• G05D 16/20 - Commande de la pression d'un fluide caractérisée par l'utilisation de moyens électriques
• F04D 13/00 - Installations ou systèmes de pompage
• F15B 13/00 - Parties constitutives des systèmes de servomoteurs

Produits et services

Chemical products for industrial, scientific and photographic purposes; chemical products for use in agriculture, horticulture and forestry; synthetic resins, unprocessed; plastics, unprocessed; manures; nutrients for plants; nutrients for algae; fire extinguishing compositions; tempering and soldering preparations; chemical substances for preserving foodstuffs; tanning substances; adhesives for industrial use; industrial organic chemicals; chemicals for use in the oil industry; chemicals for use in the refining of oils; oil-separating chemicals; chemicals for use in the treatment of oils; chemical additives; additives, chemical, to motor fuel; gasoline additives; chemical additives for diesel fuels; chemical additives for oils; fluids for use in the oil industry; chemical additives for lubricants; chemical preparations and organic substances for use in the manufacture of plastics and/or bio-plastic; additives (chemical -) for use in plastics and/or bio-plastic; carbon dioxide (other than for medical or veterinary use); hydrocarbons; gases for industrial purposes; refrigerant chemicals; additives (chemical -) for cooling agents. Mineral oils and greases for industrial purposes [not for fuel]; lubricants; compositions for absorbing, dust wetting and controlling of dust; fuels and illuminants; candles and wicks for lighting; fuel; biofuels; biomass fuel; fuel for ships, trucks, trains and aircrafts; non-chemical fuel additives; petrol additives [petrochemical]; fuel oil; oil based lubricants; oils derived from biomass and/or other organic matters and by-products; synthetic oils; mineral oils; carbon dioxide for lighting; solidified gases [fuel]; liquefied gases for driving motor vehicles and means of transport; gases for use in heating; gas for lighting; fuels and biofuels wended with chemicals and/or biological products; renewable fuel. Treatment and processing of material and goods, namely, processing of oil and/or of hydrocarbons and/or hydrocarbon compounds and/or gasses and/or water from biomass and/or other organic material; treatment and processing of material and goods, namely, conversion of biomass and/or other organic material for fuel and/or biomass-fuel and/or hydrocarbons and/or hydrocarbon compounds and/or gasses and/or water oil liquefaction; recovery of hydrocarbons from biomass or other organic material; processing of hydrocarbons; processing of organic chemical liquids and material; recycling of waste; chemical recycling of waste products; chemical treatment of waste products; chemical recycling of waste products: refining services; processing of oil; refining of oil; production, treatment and refinement of fuel, diesel fuel, biofuel and/or biodlesel fuel for others; treatment and processing of plastics; production of chemicals and other material for use in the production of plastics and/or bio-plastics; recovery of hydrocarbons and other gasses and chemicals from biomass and other organic material; providing information, advice and consultancy in connection with the aforementioned services. Science and technology services and research and design relating thereto; industrial analysis and research; design and development of computer hardware and computer software; scientific, technological and research consultation in the held of fuels, diesel fuel, biofuel and biodiesel fuel; analysis and testing for oil workings; analysis for oil-field exploitation; analysis and testing services for the oil industry; analysis and testing services for the biofuels industry; analysis and testing services in the field of oil exploration; analysis and testing services in the field of oil exploitation; analysis and testing services in the field of exploitation of biomass and other organic material; research in the field of energy; technological consultancy in the fields of energy production and use; engineering services in the field of energy technology; technological consultancy in the fields of biomass exploitation; design of plants for others for the use of biomass and other organic material in connection with the production of oil and/or fuel andfor biofuel and/or hydrocarbons and/or hydrocarbon compounds and/or gases and / or water; design of plants for the production of chemical products for industrial purposes and for agricultural, horticultural and forestry applications for others; research and development of new products for others in the field of plastic materials and bio-plastic materials; providing information, advice and consultancy services in relation to all the aforementioned services.

Produits et services

Treatment and processing of material and goods, namely, processing of oil, hydrocarbons, hydrocarbon compounds, gasses, and water from biomass, and other organic material in the nature of wood, lignocellulosic materials, organic waste, organic household waste, organic sludge from waste water treatment, algae, and organic agriculture products; treatment and processing of material and goods, namely, conversion of biomass and organic material in the nature of in the nature of wood, lignocellulosic materials, organic waste, organic household waste, organic sludge from waste water treatment, algae, and organic agriculture products for fuel and biomass-fuel, hydrocarbons, hydrocarbon compounds, and gasses, and water treatment for oil liquefaction; reclamation of usable materials from waste, namely, recovery of hydrocarbons from biomass or other organic material, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, organic household waste, organic sludges from waste water treatment, manures, algae; processing of hydrocarbons; processing of organic chemical liquids and material; recycling of waste; chemical recycling of waste products; chemical treatment of waste products; chemical recycling of waste products; refining services, namely, refining of oil and refining chemicals and gases; processing of oil; refining of oil; production, treatment and refinement of fuel, diesel fuel, biofuel, and biodiesel fuel for others; treatment and processing of plastics; production, namely, extraction of chemicals and other re-usable organic and inorganic material from wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, manures, algae, for use in the production of plastic and bio-plastic; recovery of hydrocarbons and other gasses and chemicals from biomass and other organic material, namely, reclamation of hydrocarbons and gasses from biomass and other bio-organic materials by hydrothermal and solvothermal liquefaction; Providing information, advice and consultancy in the fields of reclamation, treatment and processing of usable materials and substances from waste, low-value biomass and other organic material in the nature of wood, lignocellulosic materials, organic waste, organic household waste, organic sludge from waste water treatment, algae, and organic agriculture products, in connection with the aforementioned services; providing information, advice and consultancy in the field of biofuels production, in connection with the aforementioned services Chemicals for industrial, scientific and photographic purposes; chemicals for use in agriculture, horticulture and forestry, except fungicides, herbicides, insecticides, and parasiticides; synthetic resins, unprocessed; plastics, unprocessed; manures; nutrients for plants; nutrients for algae; fire extinguishing compositions; tempering and soldering preparations; chemical substances for preserving foodstuffs; adhesives for industrial use; industrial organic chemicals; chemicals for use in the oil industry; chemicals for use in the refining of oils; oil-separating chemicals; chemicals for use in the treatment of oils, namely, oil separating chemicals, oil purifying chemicals, oil blending chemicals; chemical additives for gasoline, for oil well drilling fluids, for enhancing the performance of lubricating oils, greases and internal combustion engine fuels, for fuel treatment, and for use as binding agents in feed pellets; additives, chemical, to motor fuel; chemical gasoline additives; chemical additives for diesel fuels; chemical additives for oils; hydraulic fluids for use in the oil industry; chemical fluids for use in the oil industry, namely, chemical fracturing fluids for use in the oil and gas industry, oil reclamation fluid for separation of crude oil from soil and water, and fluids for use in blending hydrocarbons; chemical additives for lubricants; Chemical preparations for use in the manufacture of plastics; chemical preparations for use in the manufacture of bio-plastic; chemical additives for use in plastics; chemical additives for use in bio-plastic; carbon dioxide, other than for medical or veterinary use, namely, liquid carbon dioxide, gaseous carbon dioxide; hydrocarbons, namely, aromatic hydrocarbons, hydrocarbon chemical substances; liquefied gases for industrial purposes, not to use as fuel, namely, sulphorous acid gas, and hydrogen gases; chemical additives for cooling agents Mineral oils and greases for industrial purposes not for fuel; lubricants, namely, synthetic lubricating oils, lubricating oil, industrial lubricants, drilling lubricants, automotive lubricants; fuels; candles and wicks for lighting candles; fuel; biofuels; biomass fuel; fuel for ships, trucks, trains and aircrafts; non-chemical fuel additives; fuel oil; oil based lubricants, namely, synthetic lubricating oils, lubricating oil, industrial lubricants, drilling lubricants, and automotive lubricants; oils derived from biomass and other organic matters and by-products, namely, mineral oils for industrial purposes, lubricating oil, and fuel oils; synthetic oils, namely, industrial oils, automotive engine oils, synthetic lubricating oils, and fuel oils; mineral oils, namely, mineral oil for industrial lubrication, mineral lubricating oils, mineral oils for use in the manufacture of other products, mineral oils for industrial purposes, namely, heating oils, transport fuels for driving motor vehicles and means for transport; solidified fuel gases; liquefied gases for driving motor vehicles and means of transport, namely, liquefied natural gas (LNG) and liquefied petroleum gas (LPG); gases for use in heating, namely, liquefied natural gas; gas for lighting, namely, lighting fuel gas; gases for industrial purposes, namely, fuel gas; fuels and biofuels blended with chemicals and/or biological products; renewable fuel

Produits et services

Treatment and processing of material and goods, namely, processing of oil, hydrocarbons, hydrocarbon compounds, gasses, and water from biomass, and other organic material in the nature of wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste; treatment and processing of material and goods, namely, conversion of biomass and organic material in the nature of in the nature of wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into fuel and biomass-fuel, hydrocarbons, hydrocarbon compounds, and gasses; water treatment for oil liquefaction; Recovery of hydrocarbons, namely, conversion from biomass or other organic material, namely, in the nature of wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae; processing of hydrocarbons; processing of organic chemical liquids and material; recycling of waste; chemical recycling of waste products; chemical treatment of waste products; chemical recycling of waste products: refining services, namely, refining of oil and refining chemicals and gases; processing of oil; refining of oil; production, treatment and refinement of fuel, diesel fuel, biofuel, and biodlesel fuel for others; treatment and processing of plastics; production, namely, manufacturing of plastic and bio- plastic, using reclaimed chemicals and other re-usable organic and inorganic material from wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, manures, and algae; recovery of hydrocarbons and other gasses and chemicals from biomass and other organic material, namely, reclamation of hydrocarbons and gasses from biomass and other bio-organic materials by hydrothermal and solvothermal liquefaction; providing information, advice and consultancy in connection with the aforementioned services Chemicals for industrial, scientific and photographic purposes; chemicals for use in agriculture, horticulture and forestry, except fungicides, herbicides, insecticides, and parasiticides; synthetic resins, unprocessed; plastics, unprocessed; manures; nutrients for plants; nutrients for algae; fire extinguishing compositions; tempering and soldering preparations; chemical substances for preserving foodstuffs; adhesives for industrial use; industrial organic chemicals; chemicals for use in the oil industry; chemicals for use in the refining of oils; oil-separating chemicals; chemicals for use in the treatment of oils, namely, oil separating chemicals, oil purifying chemicals, oil blending chemicals; chemical additives for gasoline, for oil well drilling fluids, for enhancing the performance of lubricating oils, greases and internal combustion engine fuels, for fuel treatment, and for use as binding agents in feed pellets; additives, chemical, to motor fuel; chemical gasoline additives; chemical additives for diesel fuels; chemical additives for oils; fluids for use in the oil industry, namely, chemical fracturing fluids for use in the oil and gas industry, oil reclamation fluid for separation of crude oil from soil and water, and chemical fluids for use in blending hydrocarbons; chemical additives for lubricants; Chemical preparations for use in the manufacture of plastics; chemical preparations for use in the manufacture of bio- plastic; chemical additives for use in plastics; chemical additives for use in bio-plastic; carbon dioxide, other than for medical or veterinary use, namely, liquid carbon dioxide, gaseous carbon dioxide; hydrocarbons, namely, aromatic hydrocarbons; Gases for industrial purposes, namely, sulphorous acid gas, and hydrogen gases to be used for the production of ammonia, cyclohexane and methanol, and for removing sulphur from fuels during oil-refining; chemical additives for cooling agents Mineral oils and greases for industrial purposes not for fuel; lubricants, namely, synthetic lubricating oils, lubricating oil, industrial lubricants, drilling lubricants, automotive lubricants; fuels; candles and wicks for lighting candles; fuel; biofuels; biomass fuel; fuel for ships, trucks, trains and aircrafts; non-chemical fuel additives; fuel oil; oil based lubricants, namely, synthetic lubricating oils, lubricating oil, industrial lubricants, drilling lubricants, and automotive lubricants; oils derived from biomass and other organic matters and by-products, namely, mineral oils for industrial purposes, lubricating oil, and fuel oils; synthetic oils, namely, industrial oils, automotive engine oils, synthetic lubricating oils, and fuel oils; mineral oils, namely, mineral oil for industrial lubrication, mineral lubricating oils, mineral oils for use in the manufacture of other products, and mineral oils for industrial purposes in the nature of, namely, heating oils; solidified fuel gases; liquefied hydrocarbon gases for driving motor vehicles and means of transport; fuels and biofuels wended with chemicals; fuels and biofuels wended with biological products; renewable fuel Science and technology services and research and design relating thereto, namely, chemical engineering, technology consultation services in the field of alternative energy, namely, gasifying and combusting alternative fuels, research and development of renewable forms of energy, scientific laboratory services, technical consultation in the field of environmental science, engineering services, design for others in the field of environmental engineering, designing and testing of new environmentally friendly products for others, engineering services in the field of energy efficiency; industrial analysis and research in the field of hydrocarbon recovery from biomass and organic matter; design and development of computer hardware and computer software; scientific and research consultation and technological consultation in the nature of engineering consulting, all in the field of fuels, diesel fuel, biofuel and biodiesel fuel hydrocarbon recovery from biomass or organic matter; analysis and testing for oil workings; analysis for oil-field exploitation; analysis and testing services for the oil industry, namely, analysis for hydrocarbon oil research; Analysis and testing services for the biofuels industry, namely, testing the feedstock goods of others to determine chemical content, testing production output to determine chemical content; analysis and testing services in the field of oil exploration; analysis and testing services in the field of oil exploitation; analysis and testing services in the field of exploitation of biomass and other organic material, namely, laboratory analysis of the chemical composition of biomass and organic fuels; research in the field of energy; Technological consulting services in the field of alternative energy generation; engineering services in the field of energy technology; technological consultancy, namely, engineering consulting in the field of renewable energy and technological consultancy in field of technology used for biomass exploitation; design of hydrocarbon recovery plants, hydrocarbon upgrading plants, and hydrocarbon refining plants, for others, namely, design of production facilities for the use of biomass and other organic material in connection with the production of oil, fuel, biofuel, hydrocarbons, hydrocarbon compounds, gases, and water; design of plants in the nature of hydrocarbon recovery plants, hydrocarbon upgrading plants, and hydrocarbon refining plants, namely, designing plant production equipment and plant components for the production of chemical products for industrial purposes and for agricultural, horticultural and forestry applications for others; research and development of new products for others in the field of plastic materials and bio-plastic materials; providing information, advice and consultancy services in relation to all the aforementioned services

Produits et services

Treatment and processing of material and goods, namely, processing of oil, hydrocarbons, hydrocarbon compounds, gasses, and water from biomass, and other organic material in the nature of wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste; treatment and processing of material and goods, namely, conversion of biomass and organic material in the nature of in the nature of wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste into fuel and biomass-fuel, hydrocarbons, hydrocarbon compounds, and gasses; water treatment for oil liquefaction; Recovery of hydrocarbons, namely, conversion from biomass or other organic material, namely, in the nature of wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae; processing of hydrocarbons; processing of organic chemical liquids and material; recycling of waste; chemical recycling of waste products; chemical treatment of waste products; chemical recycling of waste products: refining services, namely, refining of oil and refining chemicals and gases; processing of oil; refining of oil; production, treatment and refinement of fuel, diesel fuel, biofuel, and biodlesel fuel for others; treatment and processing of plastics; production, namely, conversion of chemicals and other re-usable organic and inorganic material from wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, manures, and algae, for use in the production of plastic and bio-plastic; recovery of hydrocarbons and other gasses and chemicals from biomass and other organic material, namely, reclamation of hydrocarbons and gasses from biomass and other bio-organic materials by hydrothermal and solvothermal liquefaction; providing information, advice and consultancy in connection with the aforementioned services Chemicals for industrial, scientific and photographic purposes; chemicals for use in agriculture, horticulture and forestry, except fungicides, herbicides, insecticides, and parasiticides; synthetic resins, unprocessed; plastics, unprocessed; manures; nutrients for plants; nutrients for algae; fire extinguishing compositions; tempering and soldering preparations; chemical substances for preserving foodstuffs; adhesives for industrial use; industrial organic chemicals; chemicals for use in the oil industry; chemicals for use in the refining of oils; oil-separating chemicals; chemicals for use in the treatment of oils, namely, oil separating chemicals, oil purifying chemicals, oil blending chemicals; chemical additives for gasoline, for oil well drilling fluids, for enhancing the performance of lubricating oils, greases and internal combustion engine fuels, for fuel treatment, and for use as binding agents in feed pellets; additives, chemical, to motor fuel; chemical gasoline additives; chemical additives for diesel fuels; chemical additives for oils; fluids for use in the oil industry, namely, chemical fracturing fluids for use in the oil and gas industry, oil reclamation fluid for separation of crude oil from soil and water, and chemical fluids for use in blending hydrocarbons; chemical additives for lubricants; Chemical preparations for use in the manufacture of plastics; chemical preparations for use in the manufacture of bio-plastic; chemical additives for use in plastics; chemical additives for use in bio-plastic; carbon dioxide, other than for medical or veterinary use, namely, liquid carbon dioxide, gaseous carbon dioxide; hydrocarbons, namely, aromatic hydrocarbons and hydrocarbon chemical substances with solvents; gases for industrial purposes, namely, sulphorous acid gas, and hydrogen gases to be used for the production of ammonia, cyclohexane, and methyl alcohol (methanol) for industrial purposes, oil purifying and separating chemicals for removing sulphur from fuels during oil-refining; chemical additives for cooling agents Mineral oils and greases for industrial purposes not for fuel; lubricants, namely, synthetic lubricating oils, lubricating oil, industrial lubricants, drilling lubricants, automotive lubricants; fuels; candles and wicks for lighting candles; fuel; biofuels; biomass fuel; fuel for ships, trucks, trains and aircrafts; non-chemical fuel additives; fuel oil; oil based lubricants, namely, synthetic lubricating oils, lubricating oil, industrial lubricants, drilling lubricants, and automotive lubricants; oils derived from biomass and other organic matters and by-products, namely, mineral oils for industrial purposes, lubricating oil, and fuel oils; synthetic oils, namely, industrial oils, automotive engine oils, synthetic lubricating oils, and fuel oils; mineral oils, namely, mineral oil for industrial lubrication, mineral lubricating oils, mineral oils for use in the manufacture of other products, and mineral oils for industrial purposes in the nature of heating oils; solidified fuel gases; liquefied hydrocarbon gases for driving motor vehicles and means of transport; fuels and biofuels wended with chemicals; fuels and biofuels wended with biological products; renewable fuel Science and technology services and research and design relating thereto, namely, chemical engineering, technology consultation services in the field of alternative energy, namely, gasifying and combusting alternative fuels, research and development of renewable forms of energy, scientific laboratory services, technical consultation in the field of environmental science, engineering services, design for others in the field of environmental engineering, designing and testing of new environmentally friendly products for others, engineering services in the field of energy efficiency; industrial analysis and research in the field of hydrocarbon recovery from biomas and organic matter; design and development of computer hardware and computer software; scientific and research consultation and technological consultation in the nature of engineering consulting, all in the field of fuels, diesel fuel, biofuel and biodiesel fuel hydrocarbon recovery form from biomass or organic matter; analysis and testing for oil workings; analysis for oil-field exploitation; analysis and testing services for the oil industry, namely, analysis for hydrocarbon oil research; Analysis and testing services for the biofuels industry, namely, testing the feedstock goods of others to determine chemical content, testing production output to determine chemical content; analysis and testing services in the field of oil exploration; analysis and testing services in the field of oil exploitation; analysis and testing services in the field of exploitation of biomass and other organic material, namely, laboratory analysis of the chemical composition of biomass and organic fuels; research in the field of energy; technological consultancy in the technology field of energy production and use; Technological consulting services in the field of alternative energy generation; engineering services in the field of energy technology; technological consultancy, namely, renewable energy technology consulting and technological consultancy in the technology field of biomass exploitation; design of hydrocarbon recovery plants, hydrocarbon upgrading plants, and hydrocarbon refining plants, for others, namely, design of production facilities for the use of biomass and other organic material in connection with the production of oil, fuel, biofuel, hydrocarbons, hydrocarbon compounds, gases, and water; design of plants in the nature of hydrocarbon recovery plants, hydrocarbon upgrading plants, and hydrocarbon refining plants, namely, designing plant production equipment and plant components for the production of chemical products for industrial purposes and for agricultural, horticultural and forestry applications for others; research and development of new products for others in the field of plastic materials and bio-plastic materials; providing information, advice and consultancy services in relation to all the aforementioned services

Produits et services

(1) Chemicals for use in agriculture, horticulture and forestry; Synthetic resins, unprocessed; Plastics, unprocessed; Manures; Nutrients for plants; Nutrients for algae; Fire extinguishing compositions; Chemical substances for preserving foodstuffs; Industrial organic chemicals for use in plastics, paints and lubricants; Industrial gases, namely solidified gases for industrial purposes; Refrigerant chemicals (2) Chemicals for use in the oil industry, namely, oil-purifying chemicals, oil-separating chemicals; Chemicals for use in the refining of oils; Oil-separating chemicals; Chemicals for use in the treatment of oils; Chemical additives for drilling lubricants; Chemical additives for industrial lubricants; Chemical additives for lubricants for machines; Chemical additives for all-purpose lubricants; Chemical additives for engines; Chemical additives for transmissions; Additives, chemical, to motor fuel; Chemical gasoline additives; Chemical additives for diesel fuels; Chemical additives for oils; Fluids for use in the oil industry, namely, chemical fracturing fluids for use in the oil and gas industry, oil reclamation fluid for separation of crude oil from soil and water, and chemical fluids for use in blending hydrocarbons; Chemical additives for lubricants; Chemical preparations for use in the manufacture of plastics; Chemical preparations for use in the manufacture of bioplastic; Chemical additives for use in the manufacture of plastics and bio-plastics; Carbon dioxide [other than for medical or veterinary use]; Carbon dioxide; Petrol chemical additives for use in petrochemicals, namely linkers, binders, blending enablers (3) Hydrocarbons, namely, aromatic hydrocarbons and hydrocarbon chemical substances with solvents for use as fuels, lubricants, additives in chemical compositions such as plastics and paints (4) Mineral oils and greases for industrial purposes [not for fuel]; Fuels, namely, diesel fuel, ethanol fuel, fuels for ships, aviation fuel; Biofuels; Biomass fuel used to generate electric power and heat; Fuel for ships, trucks, trains and aircrafts; Fuel oil; Crude oils derived from biomass and other organic matters and byproducts; Mineral oils derived from biomass and other organic matters and by-products; Mineral oils; Renewable fuel, namely, fuel gas derived from renewable resources, fuel gas obtained from renewable resources, biofuel derived from renewable resources, biofuel derived from renewable resources (5) Lubricants, namely, all-purpose lubricants, drilling lubricants, industrial lubricants; Oil based lubricants, namely, industrial lubricating oils and mineral lubricating oils; Fuels and biofuels blended with chemicals and biological products for use in combustion engines; Non-chemical additives for gasoline (6) Candles and wicks for lighting; Non- chemical fuel additives; Synthetic oils, namely, synthetic gas oil, fuel oil, industrial oil, industrial lubricating oils; Solidified gases for fuel; Liquefied natural gases for driving motor vehicles and means of transport; Liquefied petroleum gases for driving motor vehicles and means of transport; Gases for use in heating, namely, coal gas, fuel gas, natural gas; Industrial gases, namely industrial liquefied gases (1) Treatment and processing of material and goods, namely, processing of oil, hydrocarbons, hydrocarbon compounds, gasses, and water from biomass, and other organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste; Treatment and processing of material and goods, namely, conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into fuel and biomass-fuel, hydrocarbons, hydrocarbon compounds, and gasses; Oil liquefaction; Recovery of hydrocarbons from biomass and other organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste; Processing of hydrocarbons for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives; Processing of organic chemical liquids and material for use in the conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into oil; Recycling of waste; Chemical recycling of waste products; Chemical treatment of waste products; Chemical recycling of waste products; Refining services, namely, refining of oil and refining chemicals and gases; Processing of oil for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives; Refining of oil; Recovery of hydrocarbons through the conversion from biomass or other organic material, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae; Providing information, advice and consultancy in connection with the treatment and processing of material and goods, namely, processing of oil, hydrocarbons, hydrocarbon compounds, gasses, and water from biomass, and other organic material namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, the treatment and processing of material and goods, namely, conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into fuel and biomass-fuel, hydrocarbons, hydrocarbon compounds, and gasses, oil liquefaction, the recovery of hydrocarbons from biomass and other organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, the processing of hydrocarbons for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives, the processing of organic chemical liquids and material for use in the conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into oil, recycling of waste, chemical recycling of waste products, chemical treatment of waste products, chemical recycling of waste products, refining services, namely, refining of oil and refining chemicals and gases, processing of oil for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives, refining of oil, recovery of hydrocarbons through the conversion from biomass or other organic material, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae (2) Production, namely, conversion of chemicals and other re-usable organic and inorganic material from wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, manures, and algae, for use in the production of plastic and bio-plastic

Produits et services

(1) Chemicals for use in agriculture, horticulture and forestry; Synthetic resins, unprocessed; Plastics, unprocessed; Manures; Nutrients for plants; Nutrients for algae; Fire extinguishing compositions; Chemical substances for preserving foodstuffs; Industrial organic chemicals for use in plastics, paints and lubricants; Chemical gasoline additives; Industrial gases, namely, solidified gases for industrial purposes; Refrigerant chemicals (2) Hydrocarbons, namely, aromatic hydrocarbons and hydrocarbon chemical substances with solvents for use as fuels, lubricants, additives in chemical compositions such as plastics and paints (3) Chemicals for use in the oil industry, namely, oil-purifying chemicals, oil-separating chemicals; Chemicals for use in the refining of oils; Oil-separating chemicals; Chemicals for use in the treatment of oils; Chemical additives for drilling lubricants; Chemical additives for industrial lubricants; Chemical additives for lubricants for machines; Chemical additives for all-purpose lubricants; Chemical additives for engines; Chemical additives for transmissions; Additives, chemical, to motor fuel; Chemical additives for diesel fuels; Chemical additives for oils; Fluids for use in the oil industry, namely, chemical fracturing fluids for use in the oil and gas industry, oil reclamation fluid for separation of crude oil from soil and water, and chemical fluids for use in blending hydrocarbons; Chemical additives for lubricants; Chemical preparations for use in the manufacture of plastics; Chemical preparations for use in the manufacture of bio-plastic; Chemical additives for use in the manufacture of plastics and bio-plastics; Carbon dioxide [other than for medical or veterinary use]; Carbon dioxide; Petrol chemical additives for use in petrochemicals, namely linkers, binders, blending enablers (4) Candles and wicks for lighting; Non- chemical fuel additives; Synthetic oils, namely, synthetic gas oil, fuel oil, industrial oil, industrial lubricating oils; Solidified gases for fuel; Liquefied natural gases for driving motor vehicles and means of transport; Liquefied petroleum gases for driving motor vehicles and means of transport; Gases for use in heating, namely, coal gas, fuel gas, natural gas; Fuels and biofuels blended with chemicals and biological products for use in combustion engines; Non-chemical additives for gasoline; Industrial gases, namely, industrial liquefied gases (5) Mineral oils and greases for industrial purposes [not for fuel]; Lubricants, namely, all-purpose lubricants, drilling lubricants, industrial lubricants; Fuels, namely, diesel fuel, ethanol fuel, fuels for ships, aviation fuel; Biofuels; Biomass fuel used as an energy source for heating; Biomass fuel used to generate electric power and heat; Fuel for ships, trucks, trains and aircrafts; Fuel oil; Oil based lubricants, namely, industrial lubricating oils and mineral lubricating oils; Crude oils derived from biomass and other organic matters and by-products; Mineral oils derived from biomass and other organic matters and by-products; Mineral oils; Renewable fuel, namely, fuel gas derived from renewable resources, fuel gas obtained from renewable resources, biofuel derived from renewable resources, biofuel derived from renewable resources (1) Treatment and processing of material and goods, namely, processing of oil, hydrocarbons, hydrocarbon compounds, gasses, and water from biomass, and other organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste; Treatment and processing of material and goods, namely, conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into fuel and biomass-fuel, hydrocarbons, hydrocarbon compounds, and gasses; Oil liquefaction; Recovery of hydrocarbons from biomass and other organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste; Processing of hydrocarbons for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives; Processing of organic chemical liquids and material for use in the conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into oil; Recycling of waste; Chemical recycling of waste products; Chemical treatment of waste products; Chemical recycling of waste products; Refining services, namely, refining of oil and refining chemicals and gases; Processing of oil for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives; Refining of oil; Recovery of hydrocarbons through the conversion from biomass or other organic material, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae; Providing information, advice and consultancy in connection with the treatment and processing of material and goods, namely, processing of oil, hydrocarbons, hydrocarbon compounds, gasses, and water from biomass, and other organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, the treatment and processing of material and goods, namely, conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into fuel and biomass-fuel, hydrocarbons, hydrocarbon compounds, and gasses, oil liquefaction, the recovery of hydrocarbons from biomass and other organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, the processing of hydrocarbons for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives, the processing of organic chemical liquids and material for use in the conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into oil, recycling of waste, chemical recycling of waste products, chemical treatment of waste products, chemical recycling of waste products, refining services, namely, refining of oil and refining chemicals and gases, processing of oil for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives, refining of oil, recovery of hydrocarbons through the conversion from biomass or other organic material, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae (2) Production, namely, conversion of chemicals and other re-usable organic and inorganic material from wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, manures, and algae, for use in the production of plastic and bio-plastic (3) Science and technology services and research and design relating thereto, namely, chemical engineering, technology consultation services in the field of alternative energy, namely, gasifying and combusting alternative fuels, research and development of renewable forms of energy, scientific laboratory services, namely, laboratory research and testing of biomass and feed stock, including fuels and biofuels, technical consultation in the field of environmental science, engineering services in the field of energy production and supply, design for others in the field of environmental engineering, designing and testing of new environmentally friendly products for others, engineering services in the field of energy efficiency; Analysis for oil-field exploitation; Analysis and testing services for the oil production industry; Analysis and testing services in the field of oil exploration; Analysis and testing services in the field of oil exploitation (4) Industrial analysis and research in the field of hydrocarbon recovery from biomass and organic matter, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae; Design and development of computer hardware and computer software; Scientific, technological and research consultation in the field of fuels, diesel fuel, biofuel and biodiesel fuel; Analysis and testing for oil workings for the oil production industry; Analysis and testing services for the biofuels industry, namely, testing the feedstock goods of others to determine chemical content, testing production output to determine chemical content; Analysis and testing services in the field of exploitation of biomass and other organic material, namely, laboratory analysis of the chemical composition of biomass and organic fuels; Research in the field of energy, namely, biomass energy and sustainable energy; Technological consultancy in the fields of energy, namely, biomass energy and sustainable energy production and use; Engineering services in the field of energy generation technology, namely, biomass energy and sustainable energy; Technological consultancy, namely, renewable energy technology consulting and technological consultancy in the technology field of biomass exploitation; Design of plants for others for the use of biomass and other organic material in connection with the production of oil and fuel and biofuel and hydrocarbons and hydrocarbon compounds and gases and water; Design of plants for the production of chemical products for industrial purposes and for agricultural, horticultural and forestry applications for others; Research and development of new products for others in the field of plastic materials and bio-plastic materials; Providing information, advice and consultancy services in relation to industrial analysis and research in the field of hydrocarbon recovery from biomass and organic matter, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae, design and development of computer hardware and computer software, scientific, technological and research consultation in the field of fuels, diesel fuel, biofuel and biodiesel fuel, analysis and testing for oil workings for the oil production industry, analysis and testing services for the biofuels industry, namely, testing the feedstock goods of others to determine chemical content, testing production output to determine chemical content, analysis and testing services in the field of exploitation of biomass and other organic material, namely, laboratory analysis of the chemical composition of biomass and organic fuels, research in the field of energy, namely, biomass energy and sustainable energy, technological consultancy in the fields of energy, namely, biomass energy and sustainable energy production and use, engineering services in the field of energy generation technology, namely, biomass energy and sustainable energy, technological consultancy, namely, renewable energy technology consulting and technological consultancy in the technology field of biomass exploitation, design of plants for others for the use of biomass and other organic material in connection with the production of oil and fuel and biofuel and hydrocarbons and hydrocarbon compounds and gases and water, design of plants for the production of chemical products for industrial purposes and for agricultural, horticultural and forestry applications for others, research and development of new products for others in the field of plastic materials and bio-plastic materials

Produits et services

(1) Chemicals for use in agriculture, horticulture and forestry; Synthetic resins, unprocessed; Plastics, unprocessed; Manures; Nutrients for plants; Nutrients for algae; Fire extinguishing compositions; Chemical substances for preserving foodstuffs; Industrial organic chemicals for use in plastics, paints and lubricants; Chemical gasoline additives; Industrial gases, namely solidified gases for industrial purposes; Refrigerant chemicals (2) Hydrocarbons, namely, aromatic hydrocarbons and hydrocarbon chemical substances with solvents for use as fuels, lubricants, additives in chemical compositions such as plastics and paints (3) Chemicals for use in the oil industry, namely, oil-purifying chemicals, oil-separating chemicals; Chemicals for use in the refining of oils; Oil-separating chemicals; Chemicals for use in the treatment of oils; Chemical additives for drilling lubricants; Chemical additives for industrial lubricants; Chemical additives for lubricants for machines; Chemical additives for all-purpose lubricants; Chemical additives for engines; Chemical additives for transmissions; Additives, chemical, to motor fuel; Chemical additives for diesel fuels; Chemical additives for oils; Fluids for use in the oil industry, namely, chemical fracturing fluids for use in the oil and gas industry, oil reclamation fluid for separation of crude oil from soil and water, and chemical fluids for use in blending hydrocarbons; Chemical additives for lubricants; Chemical preparations for use in the manufacture of plastics; Chemical preparations for use in the manufacture of bio-plastic; Chemical additives for use in the manufacture of plastics and bio-plastics; Carbon dioxide [other than for medical or veterinary use]; Carbon dioxide; Petrol chemical additives for use in petrochemicals, namely linkers, binders, blending enablers (4) Candles and wicks for lighting; Non- chemical fuel additives; Synthetic oils, namely, synthetic gas oil, fuel oil, industrial oil, industrial lubricating oils; Solidified gases for fuel; Liquefied natural gases for driving motor vehicles and means of transport; Liquefied petroleum gases for driving motor vehicles and means of transport; Gases for use in heating, namely, coal gas, fuel gas, natural gas; Fuels and biofuels blended with chemicals and biological products for use in combustion engines; Non-chemical additives for gasoline; Industrial gases, namely liquefied gases (5) Mineral oils and greases for industrial purposes [not for fuel]; Lubricants, namely, all-purpose lubricants, drilling lubricants, industrial lubricants; Fuels, namely, diesel fuel, ethanol fuel, fuels for ships, aviation fuel; Biofuels; Biomass fuel used as an energy source for heating; Biomass fuel used to generate electric power and heat; Fuel for ships, trucks, trains and aircrafts; Fuel oil; Oil based lubricants, namely, industrial lubricating oils and mineral lubricating oils; Crude oils derived from biomass and other organic matters and by-products; Mineral oils derived from biomass and other organic matters and by-products; Mineral oils; Renewable fuel, namely, fuel gas derived from renewable resources, fuel gas obtained from renewable resources, biofuel derived from renewable resources, biofuel derived from renewable resources (1) Treatment and processing of material and goods, namely, processing of oil, hydrocarbons, hydrocarbon compounds, gasses, and water from biomass, and other organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste; Treatment and processing of material and goods, namely, conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into fuel and biomass-fuel, hydrocarbons, hydrocarbon compounds, and gasses; Oil liquefaction; Recovery of hydrocarbons from biomass and other organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste; Processing of hydrocarbons for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives; Processing of organic chemical liquids and material for use in the conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into oil; Recycling of waste; Chemical recycling of waste products; Chemical treatment of waste products; Chemical recycling of waste products; Refining services, namely, refining of oil and refining chemicals and gases; Processing of oil for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives; Refining of oil; Recovery of hydrocarbons through the conversion from biomass or other organic material, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae; Providing information, advice and consultancy in connection with the treatment and processing of material and goods, namely, processing of oil, hydrocarbons, hydrocarbon compounds, gasses, and water from biomass, and other organic material namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, the treatment and processing of material and goods, namely, conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into fuel and biomass-fuel, hydrocarbons, hydrocarbon compounds, and gasses, oil liquefaction, the recovery of hydrocarbons from biomass and other organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, the processing of hydrocarbons for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives, the processing of organic chemical liquids and material for use in the conversion of biomass and organic material, namely, wood, and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, algae, agriculture products, and waste, into oil, recycling of waste, chemical recycling of waste products, chemical treatment of waste products, chemical recycling of waste products, refining services, namely, refining of oil and refining chemicals and gases, processing of oil for the production of hydrocarbon derivatives with different characteristics for use as fuels, lubricants, plastics, chemical additives, refining of oil, recovery of hydrocarbons through the conversion from biomass or other organic material, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae (2) Production, namely, conversion of chemicals and other re-usable organic and inorganic material from wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludge from waste water treatment, manures, and algae, for use in the production of plastic and bio-plastic (3) Science and technology services and research and design relating thereto, namely, chemical engineering, technology consultation services in the field of alternative energy, namely, gasifying and combusting alternative fuels, research and development of renewable forms of energy, scientific laboratory services, namely, laboratory research and testing of biomass and feed stock, including fuels and biofuels, technical consultation in the field of environmental science, engineering services in the field of energy production and supply, design for others in the field of environmental engineering, designing and testing of new environmentally friendly products for others, engineering services in the field of energy efficiency; Analysis for oil-field exploitation; Analysis and testing services for the oil production industry; Analysis and testing services in the field of oil exploration; Analysis and testing services in the field of oil exploitation (4) Industrial analysis and research in the field of hydrocarbon recovery from biomass and organic matter, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae; Design and development of computer hardware and computer software; Scientific, technological and research consultation in the field of fuels, diesel fuel, biofuel and biodiesel fuel; Analysis and testing for oil workings for the oil production industry; Analysis and testing services for the biofuels industry, namely, testing the feedstock goods of others to determine chemical content, testing production output to determine chemical content; Analysis and testing services in the field of exploitation of biomass and other organic material, namely, laboratory analysis of the chemical composition of biomass and organic fuels; Research in the field of energy, namely, biomass energy and sustainable energy; Technological consultancy in the fields of energy, namely, biomass energy and sustainable energy production and use; Engineering services in the field of energy generation technology, namely, biomass energy and sustainable energy; Technological consultancy, namely, renewable energy technology consulting and technological consultancy in the technology field of biomass exploitation; Design of plants for others for the use of biomass and other organic material in connection with the production of oil and fuel and biofuel and hydrocarbons and hydrocarbon compounds and gases and water; Design of plants for the production of chemical products for industrial purposes and for agricultural, horticultural and forestry applications for others; Research and development of new products for others in the field of plastic materials and bio-plastic materials; Providing information, advice and consultancy services in relation to industrial analysis and research in the field of hydrocarbon recovery from biomass and organic matter, namely, wood, agricultural residues and other lignocellulosic materials, organic waste, household waste, sludges from waste water treatment, manures, and algae, design and development of computer hardware and computer software, scientific, technological and research consultation in the field of fuels, diesel fuel, biofuel and biodiesel fuel, analysis and testing for oil workings for the oil production industry, analysis and testing services for the biofuels industry, namely, testing the feedstock goods of others to determine chemical content, testing production output to determine chemical content, analysis and testing services in the field of exploitation of biomass and other organic material, namely, laboratory analysis of the chemical composition of biomass and organic fuels, research in the field of energy, namely, biomass energy and sustainable energy, technological consultancy in the fields of energy, namely, biomass energy and sustainable energy production and use, engineering services in the field of energy generation technology, namely, biomass energy and sustainable energy, technological consultancy, namely, renewable energy technology consulting and technological consultancy in the technology field of biomass exploitation, design of plants for others for the use of biomass and other organic material in connection with the production of oil and fuel and biofuel and hydrocarbons and hydrocarbon compounds and gases and water, design of plants for the production of chemical products for industrial purposes and for agricultural, horticultural and forestry applications for others, research and development of new products for others in the field of plastic materials and bio-plastic materials

Abrégé

A continuous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurizing the feed mixture to a pressure in the range 250-400 bar; heating the feed mixture to a temperature in the range 370-450° C., and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product.

Classes IPC  ?

• C10G 1/04 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par extraction
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• C12M 1/00 - Appareillage pour l'enzymologie ou la microbiologie
• C12P 5/02 - Préparation des hydrocarbures acycliques

Abrégé

A continuous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 250-400 bar; heating the feed mixture to a temperature in the range 370-450° C., and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product.

Classes IPC  ?

• C10G 1/04 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par extraction
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• C12M 1/00 - Appareillage pour l'enzymologie ou la microbiologie
• C12P 5/02 - Préparation des hydrocarbures acycliques

Abrégé

The invention relates to a process for producing an upgraded renewable oil from renewable carbonaceous material(-s) comprising providing a low sulphur oxygen containing renewable crude oil having a sulphur content of less than 0.5 wt % and an oxygen content from about 2.0 wt to about 20 wt %, pressurising the low sulphur oxygen containing renewable crude oil to an operational pressure in the range 20 to 200 bar, adding and mixing hydrogen to the pressurized low sulphur oxygen containing crude oil, heating the oil to an operational temperature in the range 180-410 °C in one or more steps, contacting said oil with at least one heterogeneous catalyst contained in a first reaction zone, contacting the effluent from said first reaction zone with at least one heterogeneous catalyst contained in a second reaction zone, where in at least one of the heterogeneous catalaysts in the first reaction zone and/or the second reaction zone is on a non-suplhided form.

Classes IPC  ?

• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to a process for producing an upgraded renewable oil from renewable carbonaceous material(-s) comprising providing a low sulphur oxygen containing renewable crude oil having a sulphur content of less than 0.5 wt % and an oxygen content from about 2.0 wt to about 20 wt %, pressurising the low sulphur oxygen containing renewable crude oil to an operational pressure in the range 20 to 200 bar, adding and mixing hydrogen to the pressurized low sulphur oxygen containing crude oil, heating the oil to an operational temperature in the range 180-410 °C in one or more steps, contacting said oil with at least one heterogeneous catalyst contained in a first reaction zone, contacting the effluent from said first reaction zone with at least one heterogeneous catalyst contained in a second reaction zone, where in at least one of the heterogeneous catalaysts in the first reaction zone and/or the second reaction zone is on a non-suplhided form.

Classes IPC  ?

• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to a feed mixture for use in a process for producing hydrocarbons under increased pressure and temperature conditions, where the feed mixture comprises one or more carbonaceous feedstocks and water, where further a texturing agent has been added to the feed mixture, the texturing agent being adapted to stabilize the feed mixture to prevent separation and further to maintain the feed mixture as a homogenous mixture during a pressurization. Further the invention relates to processes for manufacturing such feed mixture.

Classes IPC  ?

• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10B 53/02 - Distillation destructive spécialement conçue pour des matières premières solides particulières ou sous forme spéciale de matières contenant de la cellulose
• C10B 57/06 - Autres procédés de carbonisation ou de cokéfactionCaractéristiques générales des procédés de distillation destructive utilisant des charges de composition spéciale contenant des additifs
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon

Abrégé

The invention relates to a method for producing liquid hydrocarbon, the method comprising: providing a feed material, pressurizing the feed material to a predetermined process pressure, heating the pressurized feed material to a predetermined process temperature, reacting the pressurized and heated feed material for a predetermined period of time, cooling the reacted feed material and mechanically separating a high viscosity fraction from the converted feed material before conveying the remaining converted feed mass through a pressure reduction system and further through a separation system.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation

Abrégé

The invention relates to a pressure reduction device for use in processing equipment handling high pressure and high temperature fluids with a content of abrasive components, where the pressure reduction device comprises a number of pipes with a length and internal cross section adapted to reduce the pressure, where the length, the cross sectional area and the number of pipes are chosen to have an average flow velocity within each pipe of less than 30 m/s.

Classes IPC  ?

• G05D 16/20 - Commande de la pression d'un fluide caractérisée par l'utilisation de moyens électriques
• G05D 16/04 - Commande de la pression d'un fluide sans source d'énergie auxiliaire
• F16L 55/027 - Étranglements

Abrégé

The invention relates to a feed mixture for use in a process for producing hydrocarbons under increased pressure and temperature conditions, where the feed mixture comprisess one or more carbonaceous feedstocks and water, where further a texturing agent has been added to the feed mixture, the texturing agent being adapted to stabilize the feed mixture to prevent separation and further to maintain the feed mixture as a homogenous mixture during a pressurization. Further the invention relates to processes for manufacturing such feed mixture.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive

Abrégé

The invention relates to a feed mixture for use in a process for producing hydrocarbons under increased pressure and temperature conditions, where the feed mixture comprisess one or more carbonaceous feedstocks and water, where further a texturing agent has been added to the feed mixture, the texturing agent being adapted to stabilize the feed mixture to prevent separation and further to maintain the feed mixture as a homogenous mixture during a pressurization. Further the invention relates to processes for manufacturing such feed mixture.

Classes IPC  ?

• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon

Abrégé

The invention relates to a continuous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water, the process comprising converting at least part of the carbonaceous material, and further in a state of cleaning the pressure and temperature is set to a predetermined desired level; where prior to the cleaning, the inflow of feed mixture is terminated and the system is filled with a fluid, where the temperature and the pressure are altered to the predetermined level at a predetermined rate and where the pressure is constantly kept at a level above the saturation pressure for the fluid at a given temperature, where the inflow of at least one cleaning fluid is initiated and the at least one cleaning fluid is circulated in the system for a predetermined time; where upon reaching the predetermined time for the cleaning fluid circulation, the temperature and pressure is altered to the operational pressure and temperature at a predetermined rate, where the pressure is constantly kept at a level above the saturation pressure for the fluid at a given temperature; and where upon reaching the operational conditions the inflow of the fluid/cleaning fluid is terminated and the inflow of feed mixture is initiated.

Classes IPC  ?

• B08B 9/08 - Nettoyage de récipients, p. ex. de réservoirs
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to a continuous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water, the process comprising: converting at least part of the carbonaceous material by: pressurizing the feed mixture to an operational pressure in the range 150-400 bar, heating the feed mixture to an operational temperature in the range 300-450° C., and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product; where in a state of discontinued operation the inflow of feed mixture is terminated and the system is filled with a fluid; where the pressure and temperature is set to a predetermined desired level, where the temperature and the pressure are altered to the predetermined lower level at a predetermined rate and where the pressure during the altering is constantly kept at a level above the saturation pressure for the fluid at a given temperature.

Classes IPC  ?

• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• B01J 19/00 - Procédés chimiques, physiques ou physico-chimiques en généralAppareils appropriés
• B01J 19/24 - Réacteurs fixes sans élément interne mobile
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to a process for continuously converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water, the process comprising: converting at least part of the carbonaceous material by pressurising the feed mixture to an operational pressure in the range 150-400 bar, heating the feed mixture to an operational temperature in the range 300-450° C., and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product; where prior to the pressurisation and heating of the feed mixture the system has been brought to an operational state by filling the system with a fluid while the system being at a temperature and a pressure below the operational temperature and pressure, and subsequently heating and pressurizing the fluid to the operational conditions at a predetermined heating and pressurisation rate, where the pressure is constantly kept at a level above the saturation pressure for the fluid at a given temperature; and where upon reaching the operational temperature and pressure the fluid inflow to the pressurisation is terminated and the feed mixture inflow to the pressurisation is initiated.

Classes IPC  ?

• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive

Abrégé

The invention relates to a method for producing liquid hydrocarbon, the method comprising: providing a feed material, pressurizing the feed material to a predetermined process pressure, heating the pressurized feed material to a predetermined process temperature, reacting the pressurized and heated feed material for a predetermined period of time, cooling the reacted feed material and mechanically separating a high viscosity fraction from the converted feed material before conveying the remaining converted feed mass through a pressure reduction system and further through a separation system.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation

Abrégé

The invention relates to a method for producing liquid hydrocarbon, the method comprising: providing a feed material, pressurizing the feed material to a predetermined process pressure, heating the pressurized feed material to a predetermined process temperature, reacting the pressurized and heated feed material for a predetermined period of time, cooling the reacted feed material and mechanically separating a high viscosity fraction from the converted feed material before conveying the remaining converted feed mass through a pressure reduction system and further through a separation system.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation

Abrégé

The invention relates to a pressure reduction device for use in processing equipment handling high pressure and high temperature fluids with a content of abrasive components, where the pressure reduction device comprises a number of pipes with a length and internal cross section adapted to reduce the pressure, where the length, the cross sectional area and the number of pipes are chosen to have an average flow velocity within each pipe of less than 30m/s.

Classes IPC  ?

• F15C 1/00 - Éléments de circuits n'ayant pas de parties en mouvement
• F15C 7/00 - Éléments hybrides, c.-à-d. éléments de circuits ayant des caractéristiques prévues dans les groupes et
• F15D 1/04 - Agencement de déflecteurs de guidage dans les coudes des tuyaux ou les courbes des conduitsStructure des éléments de conduit pour des coudes en relation avec l'écoulement, p. ex. pour réduire les chutes de débit
• F17D 1/08 - Systèmes de canalisation pour liquides ou produits visqueux
• G05D 16/00 - Commande de la pression d'un fluide

Abrégé

The invention relates to a pressure reduction device for use in processing equipment handling high pressure and high temperature fluids with a content of abrasive components, where the pressure reduction device comprises a number of pipes with a length and internal cross section adapted to reduce the pressure, where the length, the cross sectional area and the number of pipes are chosen to have an average flow velocity within each pipe of less than 30m/s.

Classes IPC  ?

• F15D 1/04 - Agencement de déflecteurs de guidage dans les coudes des tuyaux ou les courbes des conduitsStructure des éléments de conduit pour des coudes en relation avec l'écoulement, p. ex. pour réduire les chutes de débit
• F15C 1/00 - Éléments de circuits n'ayant pas de parties en mouvement
• F15C 7/00 - Éléments hybrides, c.-à-d. éléments de circuits ayant des caractéristiques prévues dans les groupes et
• F17D 1/08 - Systèmes de canalisation pour liquides ou produits visqueux
• G05D 16/00 - Commande de la pression d'un fluide

Abrégé

The invention relates to a continuous process for converting carbonaceous material contained in at least two feedstocks into a liquid hydrocarbon product, said feedstocks including at least one feedstock of biomass and at least one feedstock of lignite and/or peat, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurizing the feed mixture to a pressure in the range 50-400 bar, heating the feed mixture to a temperature in the range 250-500° C., and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; and separating a fraction comprising liquid hydrocarbon product and leaving a residual fraction.

Classes IPC  ?

• C10G 1/04 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par extraction
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• C12M 1/00 - Appareillage pour l'enzymologie ou la microbiologie
• C12P 5/02 - Préparation des hydrocarbures acycliques

Abrégé

The invention relates to continuous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurizing the feed mixture to a pressure in the range 50-400 bar; heating the feed mixture to a temperature in the range 250-500° C., maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; at least partly expanding said converted feed mixture in a flash separation step, wherein the converted feed mixture is separated into a gas phase and a liquid phase, and wherein liquid CO2 is recovered from said gas phase, and separating from the liquid phase a fraction comprising liquid hydrocarbon product.

Classes IPC  ?

• C10G 1/04 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par extraction
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• C12M 1/00 - Appareillage pour l'enzymologie ou la microbiologie
• C12P 5/02 - Préparation des hydrocarbures acycliques

Abrégé

The invention relates to a process for improving efficiency of a organic food production plant, the process comprising preparing a feedstock of a raw harvested organic food base product; processing the prepared food base product, including heating; extracting the organic food material from the food base product, and leaving a residual waste product; feeding the waste product into a continuous process for converting carbonaceous material in the waste product into a liquid hydrocarbon product and extracting a liquid hydrocarbon product. The process is related to palm oil production from fresh fruit bunches.

Classes IPC  ?

• C12N 1/12 - Algues unicellulairesLeurs milieux de culture
• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/04 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par extraction
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• C12M 1/00 - Appareillage pour l'enzymologie ou la microbiologie
• C12P 5/02 - Préparation des hydrocarbures acycliques

Abrégé

The invention relates to a continuous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurizing the feed mixture to a pressure in the range 250-400 bar; heating the feed mixture to a temperature in the range 370-450° C., and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product.

Classes IPC  ?

• C10G 1/04 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par extraction
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• C12M 1/00 - Appareillage pour l'enzymologie ou la microbiologie
• C12P 5/02 - Préparation des hydrocarbures acycliques

Abrégé

The invention relates to a continuous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurizing the feed mixture to a pressure in the range 50-400 bar, heating the feed mixture to a temperature in the range 250-500° C., and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200° C. and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; separating a fraction comprising liquid hydrocarbon product, and leaving a residual fraction; feeding said residual fraction into a bioreactor for the production of biomass such as algae and/or bacteria such as cyano bacteria.

Classes IPC  ?

• C12P 5/02 - Préparation des hydrocarbures acycliques
• C10G 1/04 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par extraction
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
• C12M 1/00 - Appareillage pour l'enzymologie ou la microbiologie

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water, the process comprising : converting at least part of the carbonaceous material by: pressurising the feed mixture to an operational pressure in the range 150- 400 bar, heating the feed mixture to an operational temperature in the range 300-450 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product; where in a state of discontinued operation the inflow of feed mixture is terminated and the system is filled with a fluid;where the pressure and temperature is set to a predetermined desired level, where the temperature and the pressure are altered to the predetermined lower level at a predetermined rate and where the pressure during the altering is constantly kept at a level above the saturation pressure for the fluid at a given temparature.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water, the process comprising converting at least part of the carbonaceous material, and further in a state of cleaning the pressure and temperature is set to a predetermined desired level; where prior to the cleaning, the inflow of feed mixture is terminated and the system is filled with a fluid, where the temperature and the pressure are altered to the predetermined level at a predetermined rate and where the pressure is constantly kept at a level above the saturation pressure for the fluid at a given temparature, where the inflow of at least one cleaning fluid is initiated and the at least one cleaning fluid is circulated in the system for a predetermined time; where upon reaching the predetermined time for the cleaning fluid circulation, the temparature and pressure is altered to the operational pressure and temperature at a predetermined rate, where the pressure is constantly kept at a level above the saturation pressure for the fluid at a given temperature; and where upon reaching the operational conditions the inflow of the fluid/cleaning fluid is terminated and the inflow of feed mixture is initiated.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 33/00 - Déshydratation ou désémulsification des huiles d'hydrocarbures

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water, the process comprising converting at least part of the carbonaceous material, and further in a state of cleaning the pressure and temperature is set to a predetermined desired level; where prior to the cleaning, the inflow of feed mixture is terminated and the system is filled with a fluid, where the temperature and the pressure are altered to the predetermined level at a predetermined rate and where the pressure is constantly kept at a level above the saturation pressure for the fluid at a given temparature, where the inflow of at least one cleaning fluid is initiated and the at least one cleaning fluid is circulated in the system for a predetermined time; where upon reaching the predetermined time for the cleaning fluid circulation, the temparature and pressure is altered to the operational pressure and temperature at a predetermined rate, where the pressure is constantly kept at a level above the saturation pressure for the fluid at a given temperature; and where upon reaching the operational conditions the inflow of the fluid/cleaning fluid is terminated and the inflow of feed mixture is initiated.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 33/00 - Déshydratation ou désémulsification des huiles d'hydrocarbures

Abrégé

The invention relates to a process for continuously converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water, the process comprising: converting at least part of the carbonaceous material by pressurising the feed mixture to an operational pressure in the range 150-400 bar, heating the feed mixture to an operational temperature in the range 300-450 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product;where prior to the pressurisation and heating of the feed mixture the system has been brought to an operational state by filling the system with a fluid while the system being at a temperature and a pressure below the operational temperature and pressure, and subsequently heating and pressurizing the fluid to the operational conditions at a predetermined heating and pressurisation rate, where the pressure is constantly kept at a level above the saturation pressure for the fluid at a given temperature; and where upon reaching the operational temperature and pressure the fluid inflow to the pressurisation is terminated and the feed mixture inflow to the pressurisation is initiated.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water, the process comprising : converting at least part of the carbonaceous material by: pressurising the feed mixture to an operational pressure in the range 150- 400 bar, heating the feed mixture to an operational temperature in the range 300-450 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product; where in a state of discontinued operation the inflow of feed mixture is terminated and the system is filled with a fluid;where the pressure and temperature is set to a predetermined desired level, where the temperature and the pressure are altered to the predetermined lower level at a predetermined rate and where the pressure during the altering is constantly kept at a level above the saturation pressure for the fluid at a given temparature.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to a process for continuously converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water, the process comprising: converting at least part of the carbonaceous material by pressurising the feed mixture to an operational pressure in the range 150-400 bar, heating the feed mixture to an operational temperature in the range 300-450 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product;where prior to the pressurisation and heating of the feed mixture the system has been brought to an operational state by filling the system with a fluid while the system being at a temperature and a pressure below the operational temperature and pressure, and subsequently heating and pressurizing the fluid to the operational conditions at a predetermined heating and pressurisation rate, where the pressure is constantly kept at a level above the saturation pressure for the fluid at a given temperature; and where upon reaching the operational temperature and pressure the fluid inflow to the pressurisation is terminated and the feed mixture inflow to the pressurisation is initiated.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 250-400 bar; heating the feed mixture to a temperature in the range 370-450 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in at least two feedstocks into a liquid hydrocarbon product, said feedstocks including at least one feedstock of biomass and at least one feedstock of lignite and/or peat, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 50-400 bar, heating the feed mixture to a temperature in the range 250-500 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; and separating a fraction comprising liquid hydrocarbon product and leaving a residual fraction.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc

Abrégé

The invention relates to continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 50-400 bar; heating the feed mixture to a temperature in the range 250- 500 °C, maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; at least partly expanding said converted feed mixture in a flash separation step, wherein the converted feed mixture is separated into a gas phase and a liquid phase, and wherein liquid C02 is recovered from said gas phase, and separating from the liquid phase a fraction comprising liquid hydrocarbon product.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 250-400 bar; heating the feed mixture to a temperature in the range 370-450 .degree.C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 .degree.C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 50-400 bar, heating the feed mixture to a temperature in the range 250- 500 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; separating a fraction comprising liquid hydrocarbon product, and leaving a residual fraction; feeding said residual fraction into a bioreactor for the production of biomass such as algae and/or bacteria such as cyano bacteria.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 50-400 bar, heating the feed mixture to a temperature in the range 250- 500 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; separating a fraction comprising liquid hydrocarbon product, and leaving a residual fraction; feeding said residual fraction into a bioreactor for the production of biomass such as algae and/or bacteria such as cyano bacteria.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc

Abrégé

The invention relates to a process for improving efficiency of a organic food production plant, the process comprising preparing a feedstock of a raw harvested organic food base product; processing the prepared food base product, including heating; extracting the organic food material from the food base product, and leaving a residual waste product; feeding the waste product into a continous process for converting carbonaceous material in the waste product into a liquid hydrocarbon product and extracting a liquid hydrocarbon product. The process is related to palm oil production from fresh fruit bunches.

Classes IPC  ?

• C10G 1/00 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon
• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in at least two feedstocks into a liquid hydrocarbon product, said feedstocks including at least one feedstock of biomass and at least one feedstock of lignite and/or peat, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 50-400 bar, heating the feed mixture to a temperature in the range 250-500 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; and separating a fraction comprising liquid hydrocarbon product and leaving a residual fraction.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 50-400 bar, heating the feed mixture to a temperature in the range 250- 500 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; separating a fraction comprising liquid hydrocarbon product; heating the liquid hydrocarbon product from said separation to a temperature in the range 350 to 600 °C, at a pressure in the range 0.5 to 30 bar, thereby producing at least one liquid hydrocarbon fraction and/or at least one solid residue fraction and/or at least one gas fraction and/or at least one aqueous fraction.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc

Abrégé

The invention relates to continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 50-400 bar; heating the feed mixture to a temperature in the range 250- 500 °C, maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product; at least partly expanding said converted feed mixture in a flash separation step, wherein the converted feed mixture is separated into a gas phase and a liquid phase, and wherein liquid C02 is recovered from said gas phase, and separating from the liquid phase a fraction comprising liquid hydrocarbon product.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc

Abrégé

The invention relates to a continous process for converting carbonaceous material contained in one or more feedstocks into a liquid hydrocarbon product, said feedstocks including the carbonaceous material being in a feed mixture including one or more fluids, said fluids including water and further liquid organic compounds at least partly produced by the process in a concentration of at least 1% by weight, where the process comprises converting at least part of the carbonaceous material by pressurising the feed mixture to a pressure in the range 250-400 bar; heating the feed mixture to a temperature in the range 370-450 °C, and maintaining said pressurized and heated feed mixture in the desired pressure and temperature ranges in a reaction zone for a predefined time; cooling the feed mixture to a temperature in the range 25-200 °C and expanding the feed mixture to a pressure in the range of 1-70 bar, thereby causing the carbonaceous material to be converted to a liquid hydrocarbon product and separating from the converted feed mixture a fraction comprising liquid hydrocarbon product.

Classes IPC  ?

• C10G 1/02 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par distillation
• C10G 1/06 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon par hydrogénation destructive
• C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc