A process and system for continuously converting anhydrous LiOH into Li2S by reacting with a sulfur containing gas such as H2S using a fluidized bed reactor with one or more internals. The process may include a solids recovery system to recycle fines and excess sulfur containing gas to the reactor. The process may include a side stripper to strip Li2S product of excess sulfur containing gas and moisture that can be recycled to the fluidized bed reactor.
A process and system for continuously converting anhydrous LiOH into Li2S by reacting with a sulfur containing gas such as H2S using a fluidized bed reactor with one or more internals. The process may include a solids recovery system to recycle fines and excess sulfur containing gas to the reactor. The process may include a side stripper to strip Li2S product of excess sulfur containing gas and moisture that can be recycled to the fluidized bed reactor.
C01B 17/22 - Alkali metal sulfides or polysulfides
B01J 8/00 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles
B01J 8/34 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with stationary packing material in the fluidised bed, e.g. bricks, wire rings, baffles
3.
SYSTEM AND METHOD FOR STABILIZING THE OPERATION OF FACILITIES USING HYDROGEN PRODUCED BY LOW CARBON SOURCES
A system and a method for stabilizing hydrogen flow to a downstream process in a facility determining a hydrogen density and pressure profiles in the hydrogen storage unit for different target net hydrogen flows at different time intervals of a time horizon of a renewable power availability profile, determining an operating target net hydrogen flow of a hydrogen feed to the downstream process, determining a target direct hydrogen flow of a hydrogen feed and a target stored hydrogen flow of a hydrogen feed to the downstream process, and controlling the operation of the downstream process based on the operating target hydrogen flows.
A system and a method for stabilizing hydrogen flow to a downstream process in a facility determining a hydrogen density and pressure profiles in the hydrogen storage unit for different target net hydrogen flows at different time intervals of a time horizon of a renewable power availability profile, determining an operating target net hydrogen flow of a hydrogen feed to the downstream process, determining a target direct hydrogen flow of a hydrogen feed and a target stored hydrogen flow of a hydrogen feed to the downstream process, and controlling the operation of the downstream process based on the operating target hydrogen flows.
42 - Scientific, technological and industrial services, research and design
Goods & Services
Consulting services in the field of design and development of engineering processes; Research and development in the field of carbon capture and storage; Engineering design services; Engineering services in the field of hydrogen production
6.
ADVANCED CONTROL AND RELATED METHODS FOR A LOW CARBON METHANOL FACILITY
Advanced control and related methods for a low carbon methanol facility having an methanol synthesis plant that includes systems to supply energy to the facility, wherein at least a portion of the supplied energy is from a low carbon energy source, receiving a forecasted energy profile for the low carbon energy source over a time period, predicting, using an advanced regulatory controller (ARC), the operating conditions of the facility based on the forecasted energy profile for the low carbon energy source, generating, by the ARC, one or more set points to control the facility; controlling the generating of the hydrogen feed using the ARC; and producing methanol by feeding the generated hydrogen feed to the methanol synthesis plant in accordance with one or more set points generated by the ARC.
C07C 1/04 - Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of carbon from carbon monoxide with hydrogen
B01J 12/00 - Chemical processes in general for reacting gaseous media with gaseous mediaApparatus specially adapted therefor
C01B 3/02 - Production of hydrogen or of gaseous mixtures containing hydrogen
C10G 2/00 - Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
G05B 13/04 - Adaptive control systems, i.e. systems automatically adjusting themselves to have a performance which is optimum according to some preassigned criterion electric involving the use of models or simulators
7.
ADVANCED CONTROL AND RELATED METHODS FOR A LOW CARBON METHANOL FACILITY
Advanced control and related methods for a low carbon methanol facility having an methanol synthesis plant that includes systems to supply energy to the facility, wherein at least a portion of the supplied energy is from a low carbon energy source, receiving a forecasted energy profile for the low carbon energy source over a time period, predicting, using an advanced regulatory controller (ARC), the operating conditions of the facility based on the forecasted energy profile for the low carbon energy source, generating, by the ARC, one or more set points to control the facility; controlling the generating of the hydrogen feed using the ARC; and producing methanol by feeding the generated hydrogen feed to the methanol synthesis plant in accordance with one or more set points generated by the ARC.
C07C 29/152 - Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the reactor used
8.
FLOATING SUPPORT GRID SYSTEM FOR HORIZONTAL AMMONIA CONVERTER BASKET CATALYST BED
A floating support grid system including a plurality of support beams and a plurality of profile wire screen panels wherein the support beams are connected to the profile wire screen panels via one or more first floating connections, wherein the support beams are configured to connect to a horizontal ammonia converter basket via one or more second floating connections, and wherein at least some the profile wire screen panels are configured to connect to a horizontal ammonia converter basket via one or more third floating connections, wherein each of the first, second, and third floating connections independently defines one or more gaps to accommodate movement caused by thermal expansion.
B01J 8/02 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds
B01J 19/32 - Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
A floating support grid system including a plurality of support beams and a plurality of profile wire screen panels wherein the support beams are connected to the profile wire screen panels via one or more first floating connections, wherein the support beams are configured to connect to a horizontal ammonia converter basket via one or more second floating connections, and wherein at least some the profile wire screen panels are configured to connect to a horizontal ammonia converter basket via one or more third floating connections, wherein each of the first, second, and third floating connections independently defines one or more gaps to accommodate movement caused by thermal expansion.
B01J 8/04 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
A method for purifying cumene may include splitting an alkylation reaction product into a first portion and a second portion; feeding the first portion as mostly a liquid into a benzene column; at least partially vaporizing the second portion in a heater; feeding the at least partially vaporized second portion into the benzene column. A method for purifying cumene may also include the steps of providing a benzene column and a cumene column; directing a liquid side draw from the benzene column to the cumene column, the liquid side draw being a liquid substantially free of DIPB; returning a benzene enriched vapor from the cumene column to the benzene column using an overhead line, the benzene enriched vapor having a higher concentration of benzene than the liquid side draw; and drawing purified cumene from the cumene column.
37 - Construction and mining; installation and repair services
40 - Treatment of materials; recycling, air and water treatment,
42 - Scientific, technological and industrial services, research and design
Goods & Services
Procurement, namely, purchasing of equipment, machinery,
process units, supplies and associated equipment for
utility, industrial, commercial, governmental, public works,
public accommodation, and infrastructure facilities,
structures, and plants for others; business management
services, namely, contract administration and project
management services. Construction, installation, repair, renovation, and
replacement services for public and private accommodations
and infrastructure facilities, building structures, plants,
equipment; maintenance services, namely, building
maintenance services in the public and private sectors,
namely, utility, industrial, and commercial companies and
governments; inspection and supervisory services in
connection with the forgoing in the public and private
sectors, namely, utility, industrial, and commercial
companies and government; construction, maintenance, and/or
repair services for buildings, plants, structures, operating
and processing facilities, and equipment for the aviation,
biofuel, carbon capture and storage, chemical,
gas-to-liquids, liquified natural gas, manufacturing, mining
and minerals, oil and gas, petrochemical, pipeline, power
generation and transmission, pulp and paper, refining,
renewable energy, transportation, water supply, and
wastewater handling industries; construction, maintenance,
and/or repair services for buildings, plants, structures,
operating and processing facilities, and equipment for the
aviation, biofuel, carbon capture and storage, chemical,
gas-to-liquids, liquified natural gas, manufacturing, mining
and minerals, oil and gas, petrochemical, pipeline, power
generation and transmission, pulp and paper, refining,
renewable energy, transportation, water supply, and
wastewater handling industries. Biomass gasification services, treatment of waste water;
waste to energy generation services. Architectural and engineering services for the design of
buildings, plants, structures, operating and processing
facilities, and equipment for the aviation, biofuel, carbon
capture and storage, chemical, gas-to-liquids, liquified
natural gas, manufacturing, mining and minerals, oil and
gas, petrochemical, pipeline, power generation and
transmission, pulp and paper, refining, renewable energy,
transportation, water supply, and wastewater handling
industries; engineering services in the field of reducing
carbon dioxide emissions; engineering services in the field
of reducing nitrogen oxide emissions; engineering in the
public and private sectors, namely, utility, industrial, and
commercial companies and governments; design services,
namely, architectural design in the public and private
sectors, namely, utility, industrial, and commercial
companies and governments; information technology
consultation services, namely, enterprise IT consolidation,
help desk and network management, telecommunications
sustainment and modernization, information assurance and
computer network defense; engineering services and computer
engineering services in the field of cybersecurity;
developing computer software for others; and scientific
research services in the field of aerospace development,
national defense, and commercial nuclear power; research,
engineering, and testing in the fields of aerospace
development, national defense, and commercial nuclear power
provided to firms in those industries; engineering services
for computer security purposes, namely, protecting data and
information from unauthorized access.
13.
Method for Treating Hydrocarbon Effluent from Hydrothermal Liquification of Plastic Waste
A method for treating effluent from hydrothermal liquification of feedstock that contains plastic oil, pyrolysis oil, synthetic oil or hydrocarbons distillates in a plastic recycle process using supercritical water as a reaction medium into a finished liquid hydrocarbon fuel by removing impurities such as i.e. silicon, chlorides, metals, heteroatoms, etc., in a pre-treatment zone and may be passed into a feed drum or a continuous mixed settler vessel. The feed is introduced into a hydrogen atmosphere reactor. The reactor effluent is passed to a separator for extracting product mixture by addition of make-up or recycled hydrogen to the separator. The overhead product mixture is water washed to remove sour water or salt. The separator effluent is passed to a distillation section for extracting a liquid fuel product stream. A portion of the hydro processing product stream may be recycled to the feed drum or the continuous mixed settler vessel, which reduces concentration of diolefins.
C10G 1/10 - Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
C10G 1/00 - Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
C10G 1/02 - Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation
C10G 1/04 - Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction
14.
A METHOD FOR TREATING HYDROCARBON EFFLUENT FROM HYDROTHERMAL LIQUIFICATION OF PLASTIC WASTE
A method for treating effluent from hydrothermal liquification of feedstock that contains plastic oil, pyrolysis oil, synthetic oil or hydrocarbons distillates in a plastic recycle process using supercritical water as a reaction medium into a finished liquid hydrocarbon fuel by removing impurities such as i.e. silicon, chlorides, metals, heteroatoms, etc., in a pre-treatment zone and may be passed into a feed drum or a continuous mixed settler vessel. The feed is introduced into a hydrogen atmosphere reactor. The reactor effluent is passed to a separator for extracting product mixture by addition of make-up or recycled hydrogen to the separator. The overhead product mixture is water washed to remove sour water or salt. The separator effluent is passed to a distillation section for extracting a liquid fuel product stream. A portion of the hydro processing product stream may be recycled to the feed drum or the continuous mixed settler vessel, which reduces concentration of diolefins.
C10G 45/32 - Selective hydrogenation of the diolefin or acetylene compounds
C10G 65/06 - Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a selective hydrogenation of the diolefins
C08J 11/04 - Recovery or working-up of waste materials of polymers
C10G 31/06 - Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by heating, cooling, or pressure treatment
01 - Chemical and biological materials for industrial, scientific and agricultural use
04 - Industrial oils and greases; lubricants; fuels
17 - Rubber and plastic; packing and insulating materials
19 - Non-metallic building materials
40 - Treatment of materials; recycling, air and water treatment,
42 - Scientific, technological and industrial services, research and design
Goods & Services
Chemicals for use in industry, science and photography, as
well as in agriculture, horticulture and forestry;
unprocessed artificial resins, unprocessed plastics; fire
extinguishing and fire prevention compositions; tempering
and soldering preparations; substances for tanning animal
skins and hides; adhesives for use in industry; putties and
other paste fillers; compost, manures, fertilizers;
biological preparations for use in industry and science;
accelerators for organic chemical reactions; accelerators
for speeding up chemical reactions; chemicals in the nature
of activators; chemical additives; chemicals in the nature
of buffers; chemical absorbents; chemical adjuvants;
chemical agents; chemical coatings; chemical compositions;
chemical compounds; chemical diagnostic reagents; chemical
emulsifiers; chemical extenders; chemical preparations;
chemical products for biotechnological purposes; chemical
products for laboratory use other than for medical or
veterinary use; chemical products for scientific purposes;
chemical products for research purposes; purification
chemicals; chemicals in the nature of sealing preparations. Industrial oils and greases, wax; lubricants; dust
absorbing, wetting and binding compositions; fuels and
illuminants; biofuel; additives for oil, fuel, lubricants,
greases, petroleum products; alcohol fuel; biodiesel fuel;
biomass fuels; emulsions of oil for use as a fuel; emulsions
of bitumen for use as fuel; fuel mixtures. Unprocessed and semi-processed rubber, gutta-percha, gum,
asbestos, mica and substitutes for all these materials;
plastics and resins in extruded form for use in manufacture;
packing, stopping and insulating materials; recycled
plastic; recycled rubber; semi-finished chemical resins. Materials, not of metal, for building and construction;
asphalt, pitch, tar and bitumen; composite bitumen; mixtures
of bitumen and plastics for building purposes; mixtures of
bitumen and plastics for making roads; bitumen binding
material; bituminous coatings and coverings; bituminous
materials other than paint; bituminous preparations other
than paint; bituminous products other than paint; acrylic
coatings other than paint; coating preparations other than
paints or oils; coating materials. Treatment of materials; recycling; recycling of waste and
trash; recycling of plastic; recycling of materials;
recycling plants; air purification and treatment of water;
catalytic conversion of chemical compounds; chemical
processing of liquids; chemical treatment of waste products;
chemical treatment of plastics; chemical recycling;
treatment of chemicals in the nature of recycling; treatment
of waste in the nature of recycling; upcycling; carbon
offsetting services in the nature of recycling. Scientific and technological services and research and
design relating thereto; industrial analysis, industrial
research and industrial design services; quality control and
authentication services; testing of chemicals; chemistry
services; measurement services; providing information,
including online, about industrial analysis and research
services; material testing; services for assessing the
efficiency of chemicals; services for monitoring industrial
processes; technical data analysis services; technical
diagnostic testing services; technological analysis
services; technological consultation services; chemical
analysis; chemical information; chemical technological
research; preparation of reports relating to chemical
research; research relating to chemicals; research relating
to chemistry; scientific research relating to chemical
products; scientific research relating to chemistry; testing
of chemicals; biotechnological research; biotechnology
research; biotechnology testing; research relating to
biotechnology.
A steam cracking unit including one or more electric resistance heating tubes electrically connected to a current source to generate heat via electrical resistance heating. Each resistance heating tube may include two or more tube sections. Each tube section may be independently supplied with a current. A controller may be configured to adjust the application of the current to one or more tube sections to control the electrical resistance heating of the one or more resistance heating tubes. In examples, the one or more electric heating tubes may be used as preheating tubes, cracking tubes, or both.
C10G 9/36 - Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
B01J 19/24 - Stationary reactors without moving elements inside
A steam cracking unit including one or more electric resistance heating tubes electrically connected to a current source to generate heat via electrical resistance heating. Each resistance heating tube may include two or more tube sections. Each tube section may be independently supplied with a current. A controller may be configured to adjust the application of the current to one or more tube sections to control the electrical resistance heating of the one or more resistance heating tubes. In examples, the one or more electric heating tubes may be used as preheating tubes, cracking tubes, or both.
A first stream containing 1,3-butadiene, C4 acetylenes, and optionally C3 hydrocarbons, is mixed with a portion of the liquid recycle stream from a C4 acetylene hydrogenation reactor containing hydrogenated C4 acetylenes and a molecular hydrogen-containing stream, the resulting mixed stream is then fed to a C4 acetylene hydrogenation reactor to selectively hydrogenate the C4 acetylenes in the crude butadiene stream without appreciable 1,3-butadiene conversion.
C07C 7/167 - Purification, separation or stabilisation of hydrocarbonsUse of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation for removal of compounds containing a triple carbon-to-carbon bond
B01J 19/00 - Chemical, physical or physico-chemical processes in generalTheir relevant apparatus
C07C 5/09 - Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of carbon-to-carbon triple bonds to carbon-to-carbon double bonds
A syngas reforming exchanger reactor design is described. The reforming exchanger has a head, a shell, and a tubesheet secured a tube bundle. The tubesheet is bolted to the shell, after which the head is bolted to the shell. A seal is configured between the tubesheet and components of the shell. Another seal is configured between components of the head and the tubesheet. In the reformer exchanger design, those seals are maintained under bolted pressure via the bolting of both the tubesheet and the head to the shell. This design improves the integrity of sealing, thereby preventing escape of hot reformed gases from the reformer exchanger reactor during operation.
F28D 7/16 - Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
B01J 19/00 - Chemical, physical or physico-chemical processes in generalTheir relevant apparatus
B01J 19/24 - Stationary reactors without moving elements inside
C01B 3/34 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
F28F 9/00 - CasingsHeader boxesAuxiliary supports for elementsAuxiliary members within casings
20.
REFORMING EXCHANGER TUBESHEET AND SHELL FLANGE DESIGN
A syngas reforming exchanger reactor design is described. The reforming exchanger has a head, a shell, and a tubesheet secured a tube bundle. The tubesheet is bolted to the shell, after which the head is bolted to the shell. A seal is configured between the tubesheet and components of the shell. Another seal is configured between components of the head and the tubesheet. In the reformer exchanger design, those seals are maintained under bolted pressure via the bolting of both the tubesheet and the head to the shell. This design improves the integrity of sealing, thereby preventing escape of hot reformed gases from the reformer exchanger reactor during operation.
B01J 8/06 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds in tube reactorsChemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds the solid particles being arranged in tubes
F28F 9/013 - Auxiliary supports for elements for tubes or tube-assemblies
21.
REACTOR SYSTEM FOR SATURATED C3-C6 HYDROCARBON DEHYDROGENATION
A reactor system and method for catalytic dehydrogenation of saturated C3-C6 hydrocarbons within a reactor placed within a reactor disengager, where the reactor is open at the bottom thereof and open to the disengager, and the exit riser from the reactor is not hard coupled to at least one downstream cyclone. This configuration permits controlling the amount of catalyst within the reactor by varying the level of catalyst in the reactor disengager outside the reactor and permits controlling total catalyst hold-up and/or weight hourly space velocity (WHSV) independently from catalyst flow from the catalyst regenerator.
B01J 8/00 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
22.
USED MOTOR OIL DISTILLATION RESIDUE PROCESSING THROUGH SUPERCRITICAL SOLVENT DEASPHALTING FOR LUBE OIL PRODUCTION
A process and system to deasphalt used motor oil distillate residue including VTAE the process including feeding the used motor oil distillate residue and a supercritical solvent to an asphaltene separator that outputs an overhead having deasphalted oil and a bottoms that includes pitch.
C10G 21/00 - Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
C10G 67/02 - Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
C10G 67/04 - Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including solvent extraction as the refining step in the absence of hydrogen
23.
USED MOTOR OIL DISTILLATION RESIDUE PROCESSING THROUGH SUPERCRITICAL SOLVENT DEASPHALTING FOR LUBE OIL PRODUCTION
A process and system to deasphalt used motor oil distillate residue including VTAE the process including feeding the used motor oil distillate residue and a supercritical solvent to an asphaltene separator that outputs an overhead having deasphalted oil and a bottoms that includes pitch.
A system for controlling a steam cracking furnace may include a controller configured to control an electric heater to pre-heat a combustion air feed to a radiation section of the cracking furnace, and one or more sensors configured to sense properties of a recovered pure hydrogen stream fed to the radiation section of the cracking furnace as fuel. The controller can be configured to receive the sensed properties from the one or more sensors and control the electric heater based on the one or more sensed properties.
A process and system for integrating a steam cracking unit with a blue hydrogen unit in which a methane-rich gas stream, a hydrogen-rich gas stream, or both from the steam cracking unit are fed to the blue hydrogen unit and a high purity hydrogen gas stream from the blue hydrogen unit is directed to the steam cracking unit.
C07C 4/02 - Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
C10G 69/02 - Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
C10G 69/06 - Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of thermal cracking in the absence of hydrogen
26.
INTEGRATION OF STEAM CRACKER AND BLUE AMMONIA UNITS TO REDUCE CO2 EMISSION
A process and system to integrate a steam cracking unit with a blue ammonia unit such that a methane-rich gas stream and/or a hydrogen-rich gas stream is directed from the steam cracking unit to the blue ammonia unit while a hydrogen gas containing stream is directed from the blue ammonia unit to the steam cracking unit.
C01B 3/04 - Production of hydrogen or of gaseous mixtures containing hydrogen by decomposition of inorganic compounds, e.g. ammonia
C01B 3/56 - Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with solidsRegeneration of used solids
C01B 3/52 - Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with liquidsRegeneration of used liquids
B01D 3/32 - Other features of fractionating columns
27.
INTEGRATION OF STEAM CRACKER AND BLUE HYDROGEN UNITS TO REDUCE CO2 EMISSION
A process and system for integrating a steam cracking unit with a blue hydrogen unit in which a methane-rich gas stream, a hydrogen-rich gas stream, or both from the steam cracking unit are fed to the blue hydrogen unit and a high purity hydrogen gas stream from the blue hydrogen unit is directed to the steam cracking unit.
C01B 3/36 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
C01B 3/50 - Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
C10G 9/36 - Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
C10G 70/04 - Working-up undefined normally gaseous mixtures obtained by processes covered by groups , , , , by physical processes
28.
INTEGRATION OF STEAM CRACKER AND BLUE AMMONIA UNITS TO REDUCE CO2 EMISSION
A process and system to integrate a steam cracking unit with a blue ammonia unit such that a methane-rich gas stream and/or a hydrogen-rich gas stream is directed from the steam cracking unit to the blue ammonia unit while a hydrogen gas containing stream is directed from the blue ammonia unit to the steam cracking unit.
C10G 9/36 - Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
C01B 3/04 - Production of hydrogen or of gaseous mixtures containing hydrogen by decomposition of inorganic compounds, e.g. ammonia
A method and apparatus for high-purity hydrogen fired liquid hydrocarbon cracking. In one embodiment, the method may include preheating a liquid hydrocarbon feedstock in a first heat exchanger that is external to a furnace, adding steam to the preheated liquid hydrocarbon feedstock to create a fully or substantially fully vaporized stream, heating the fully or substantially fully vaporized stream in a second heat exchanger that is external to the furnace, and cracking the heated fully or substantially fully vaporized stream after it is preheated in the furnace to create a cracked gas stream comprising ethylene and hydrogen.
A method and apparatus for high-purity hydrogen fired liquid hydrocarbon cracking. In one embodiment, the method may include preheating a liquid hydrocarbon feedstock in a first heat exchanger that is external to a furnace, adding steam to the preheated liquid hydrocarbon feedstock to create a fully or substantially fully vaporized stream, heating the fully or substantially fully vaporized stream in a second heat exchanger that is external to the furnace, and cracking the heated fully or substantially fully vaporized stream after it is preheated in the furnace to create a cracked gas stream comprising ethylene and hydrogen.
C07C 4/02 - Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
C10G 9/36 - Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
31.
NET ZERO ETHANE CRACKER WITH NO EXTERNAL HYDROGEN IMPORT
A system for controlling a steam cracking furnace may include a controller configured to control an electric heater to pre-heat a combustion air feed to a radiation section of the cracking furnace, and one or more sensors configured to sense properties of a recovered pure hydrogen stream fed to the radiation section of the cracking furnace as fuel. The controller can be configured to receive the sensed properties from the one or more sensors and control the electric heater based on the one or more sensed properties.
01 - Chemical and biological materials for industrial, scientific and agricultural use
04 - Industrial oils and greases; lubricants; fuels
17 - Rubber and plastic; packing and insulating materials
19 - Non-metallic building materials
40 - Treatment of materials; recycling, air and water treatment,
42 - Scientific, technological and industrial services, research and design
Goods & Services
(1) Chemicals for use in industry, science and photography, as well as in agriculture, horticulture and forestry; unprocessed artificial resins, unprocessed plastics; fire extinguishing and fire prevention compositions; tempering and soldering preparations; substances for tanning animal skins and hides; adhesives for use in industry; putties and other paste fillers; compost, manures, fertilizers; biological preparations for use in industry and science; accelerators for organic chemical reactions; accelerators for speeding up chemical reactions; chemicals in the nature of activators; chemical additives; chemicals in the nature of buffers; chemical absorbents; chemical adjuvants; chemical agents; chemical coatings; chemical compositions; chemical compounds; chemical diagnostic reagents; chemical emulsifiers; chemical extenders; chemical preparations; chemical products for biotechnological purposes; chemical products for laboratory use other than for medical or veterinary use; chemical products for scientific purposes; chemical products for research purposes; purification chemicals; chemicals in the nature of sealing preparations.
(2) Industrial oils and greases, wax; lubricants; dust absorbing, wetting and binding compositions; fuels and illuminants; biofuel; additives for oil, fuel, lubricants, greases, petroleum products; alcohol fuel; biodiesel fuel; biomass fuels; emulsions of oil for use as a fuel; emulsions of bitumen for use as fuel; fuel mixtures.
(3) Unprocessed and semi-processed rubber, gutta-percha, gum, asbestos, mica and substitutes for all these materials; plastics and resins in extruded form for use in manufacture; packing, stopping and insulating materials; recycled plastic; recycled rubber; semi-finished chemical resins.
(4) Materials, not of metal, for building and construction; asphalt, pitch, tar and bitumen; composite bitumen; mixtures of bitumen and plastics for building purposes; mixtures of bitumen and plastics for making roads; bitumen binding material; bituminous coatings and coverings; bituminous materials other than paint; bituminous preparations other than paint; bituminous products other than paint; acrylic coatings other than paint; coating preparations other than paints or oils; coating materials. (1) Treatment of materials; recycling; recycling of waste and trash; recycling of plastic; recycling of materials; recycling plants; air purification and treatment of water; catalytic conversion of chemical compounds; chemical processing of liquids; chemical treatment of waste products; chemical treatment of plastics; chemical recycling; treatment of chemicals in the nature of recycling; treatment of waste in the nature of recycling; upcycling; carbon offsetting services in the nature of recycling.
(2) Scientific and technological services and research and design relating thereto; industrial analysis, industrial research and industrial design services; quality control and authentication services; testing of chemicals; chemistry services; measurement services; providing information, including online, about industrial analysis and research services; material testing; services for assessing the efficiency of chemicals; services for monitoring industrial processes; technical data analysis services; technical diagnostic testing services; technological analysis services; technological consultation services; chemical analysis; chemical information; chemical technological research; preparation of reports relating to chemical research; research relating to chemicals; research relating to chemistry; scientific research relating to chemical products; scientific research relating to chemistry; testing of chemicals; biotechnological research; biotechnology research; biotechnology testing; research relating to biotechnology.
A separation process and system to separate highly pure polymer grade propylene product from a liquefied petroleum gas stream combined. In examples, the system and method as combine the functions of a deethanizer and of a depropanizer, with a C3 splitter system to separate highly pure polymer grade propylene product from a liquefied petroleum gas stream, thus eliminating the need for separate dethanizer, depropanizer, and C3-splitter.
In a Fluid Catalytic Cracker (FCC) unit being operated in petrochemical mode that has an increased dry gas and LPG production that creates a bottleneck in product flow, a method for full or partial separation of light gas components from a wet gas compressor suction stream and routing it directly to an untreated fuel gas header using a parallel system to an existing wet gas compressor, which parallel system includes an auxiliary compressor and a membrane separation system.
C10G 70/04 - Working-up undefined normally gaseous mixtures obtained by processes covered by groups , , , , by physical processes
C10G 55/08 - Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural parallel stages only
36.
METHODS AND SYSTEMS FOR ALKYLATE PRODUCTION INVOLVING A MULTI-ZONE ALKYLATION REACTOR
Methods and systems for alkylate production involving a multi-zone alkylation reactor. The multi-zone alkylation reactor includes a plurality of alkylation zones spaced vertically in a series configuration and a partition splitting the plurality of alkylation zones into at least two mechanically separated catalytic volumes.
B01J 8/04 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
C07C 2/76 - Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
Methods and systems are provided for delimiting a gas plant during fluid catalytic cracking unit (FCCU) revamp as part of the olefin production system. These methods and system include a chiller unit in the gas concentration unit downstream of the FCCU. Other measures also include installing a stripper unit downstream of the regenerator of the FCCU or installing a quench line in a reactor of a FCCU to reduce the contact time of the hydrocarbon feedstock with the catalyst. These methods and systems may also lead to an increase in the propylene yield of the olefin production system
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
C10G 70/04 - Working-up undefined normally gaseous mixtures obtained by processes covered by groups , , , , by physical processes
C10G 35/24 - Controlling or regulating of reforming operations
F28F 19/00 - Preventing the formation of deposits or corrosion, e.g. by using filters
F28D 7/16 - Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
Methods and systems are provided for delimiting a gas plant during fluid catalytic cracking unit (FCCU) revamp as part of the olefin production system. These methods and system include a chiller unit in the gas concentration unit downstream of the FCCU. Other measures also include installing a stripper unit downstream of the regenerator of the FCCU or installing a quench line in a reactor of a FCCU to reduce the contact time of the hydrocarbon feedstock with the catalyst. These methods and systems may also lead to an increase in the propylene yield of the olefin production system.
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles
B01D 5/00 - Condensation of vapoursRecovering volatile solvents by condensation
B01J 8/24 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique
39.
PROCESS FOR DEBOTTLENECKING FCC WET GAS COMPRESSOR AND GAS PLANT
In a Fluid Catalytic Cracker (FCC) unit being operated in petrochemical mode that has an increased dry gas and LPG production that creates a bottleneck in product flow, a method for full or partial separation of light gas components from a wet gas compressor suction stream and routing it directly to an untreated fuel gas header using a parallel system to an existing wet gas compressor, which parallel system includes an auxiliary compressor and a membrane separation system.
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
C10G 11/02 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
C10G 55/06 - Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only including at least one catalytic cracking step
B01J 8/26 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
A multi-tier integrated power-to-ammonia system includes a converter for generating ammonia and heat through a reaction involving a compressed mixture of hydrogen and nitrogen gases. The system includes a steam generator that can generate steam using the heat from the reaction, and a reversible solid-oxide system in fluid communication with the steam generator that can separate the steam into oxygen gas and hydrogen gas.
A multi-tier integrated power-to-ammonia system includes a converter for generating ammonia and heat through a reaction involving a compressed mixture of hydrogen and nitrogen gases. The system includes a steam generator that can generate steam using the heat from the reaction, and a reversible solid-oxide system in fluid communication with the steam generator that can separate the steam into oxygen gas and hydrogen gas.
C25B 1/042 - Hydrogen or oxygen by electrolysis of water by electrolysis of steam
F25J 3/04 - Processes or apparatus for separating the constituents of gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
H01M 8/20 - Indirect fuel cells, e.g. fuel cells with redox couple being irreversible
C01B 3/02 - Production of hydrogen or of gaseous mixtures containing hydrogen
A piping connection system and method to connect a double pipe system such as a double pipe heat changer to a housing, for example a housing of a manifold. In examples, the piping connection system and method may include a transition member configured to bond or connect to the double pipe system and to the housing. In examples, the piping connection system may include a baffle configured to redirect flow from the housing to the double pipe system through an opening and towards the transition member. In examples, the piping connection system and method may be used to manufacture a quench exchanger such as a primary quench exchanger.
F28F 9/18 - Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling by welding
F28D 7/10 - Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
F28F 1/00 - Tubular elementsAssemblies of tubular elements
A piping connection system and method to connect a double pipe system such as a double pipe heat changer to a housing, for example a housing of a manifold. In examples, the piping connection system and method may include a transition member configured to bond or connect to the double pipe system and to the housing. In examples, the piping connection system may include a baffle configured to redirect flow from the housing to the double pipe system through an opening and towards the transition member. In examples, the piping connection system and method may be used to manufacture a quench exchanger such as a primary quench exchanger.
F28D 7/10 - Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
F28D 7/12 - Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically the surrounding tube being closed at one end, i.e. return type
F28D 7/00 - Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
37 - Construction and mining; installation and repair services
42 - Scientific, technological and industrial services, research and design
Goods & Services
Business feasibility studies; Business project management services; Business project management services for construction projects; Business risk management; business services, namely, logistics management in the refinery, crude and refinery product blending, liquid natural gas storage and shipping, and batch processing industries; Procurement, namely, purchasing equipment, machinery, supplies and associated equipment for utility, industrial, transportation, buildings, mining, commercial, governmental, public works, public accommodation and infrastructure facilities, structures and plants for others; Operational business assistance to enterprises Construction, maintenance, and/or repair services for buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, coal gasification, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries; Building construction observation, namely, static inspection, functional verification inspection, performance verification inspection; Construction consultation; Construction project management services; Inspection services in the course of construction of utilities, industrial facilities, transportation systems, buildings, mining facilities, commercial buildings, governmental facilities, public works plants, public accommodations, infrastructure facilities, structures, chemical and industrial plants, and construction equipment; Maintenance and/or repair of utilities, industrial facilities, transportation systems, buildings, mining facilities, commercial buildings, governmental facilities, public works plants, public accommodations, infrastructure facilities, structures, chemical and industrial plants, and construction equipment Architectural and engineering services for the design of buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, coal gasification, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries; engineering services in the field of reducing carbon dioxide emissions; Computer-aided engineering services for others; Computer software development and computer programming development for others; Consulting in the field of information technology; Design, deployment and management of wireless computer networks for others; Engineering design services; Engineering services in the field of reducing nitrogen oxide emissions; Engineering services, namely, engineering for the utility, industrial, transportation, building, mining, commercial, aerospace, power, defense and government industries; Professional computer services, namely, network analysis, LAN/WAN design, wireless engineering, virtualization and computer project management; Scientific research and development; Information technology consulting services
46.
Hydrogenation of acetylenes in a hydrocarbon stream
4 acetylenes contained within a hydrocarbon stream generated in a stream cracker unit where a debutanizer is placed upstream of a depropanizer for more economical processing of the hydrocarbon stream to produce lighter hydrocarbons, where the system requires only one stripper tower downstream of hydrogenation to remove residual hydrogen.
42 - Scientific, technological and industrial services, research and design
Goods & Services
Consulting in the field of engineering; electrical
engineering; engineering design services; engineering
drawing services; engineering services, namely, engineering
for the design and construction of facilities to store
electricity; technology advisory services related to civil
engineering and construction.
42 - Scientific, technological and industrial services, research and design
Goods & Services
Consultancy in the field of artificial intelligence
technology; providing temporary use of on-line
non-downloadable software and applications using artificial
intelligence for engineering and design of processes and
facilities in the utility, industrial, transportation,
building, mining, commercial, aerospace, power, defense and
government industries; research in the field of artificial
intelligence technology; software as a service (SAAS)
services featuring software using artificial intelligence
for engineering and design of processes and facilities in
the ammonia, aviation, biofuel, carbon capture, carbon
storage, chemical, coal gasification, coal monetization,
fertilizer, gas, gas-to-liquids, hydrogen, liquified natural
gas, manufacturing, minerals, mining, oil, olefins, organic
chemical, paper, petrochemical, pipeline, power generation,
power transmission, pulp, refining, renewable energy,
synthesis gas, transportation, water supply and wastewater
handling industries.
01 - Chemical and biological materials for industrial, scientific and agricultural use
04 - Industrial oils and greases; lubricants; fuels
40 - Treatment of materials; recycling, air and water treatment,
17 - Rubber and plastic; packing and insulating materials
19 - Non-metallic building materials
42 - Scientific, technological and industrial services, research and design
Goods & Services
Chemicals for use in industry, science and photography, as well as in agriculture, horticulture and forestry; unprocessed artificial resins, unprocessed plastics; fire extinguishing and fire prevention compositions; tempering and soldering preparations; adhesives for use in industry; putties and other paste fillers, namely, glaziers' putty, oil cement putty, starch paste adhesives other than for stationery or household purposes; compost, manures, fertilizers; biological preparations for use in industry and science; chemical agents in the nature of accelerators for organic chemical reactions; chemical agents in the nature of accelerators for speeding up chemical reactions; chemicals in the nature of activators; chemical additives for the separation and recycling of plastic material; chemicals in the nature of buffers; chemical absorbents for absorbing waste; chemical adjuvants, other than for medical or veterinary purposes; chemical agents for the separation and recycling of waste plastic; chemical coatings for use in recycling; chemical compositions for use in the recycling process; chemical compounds for use in the recycling process; chemical diagnostic reagents for industrial use; chemical emulsifiers for industrial purposes; chemical extenders in the nature of chemical compositions for recycling plastics; chemical preparations for use in recycling; chemical products for biotechnological purposes for use in recycling; chemical products for laboratory use other than for medical or veterinary use for use in recycling; chemical products for scientific purposes for use in recycling; chemical products for research purposes for use in recycling; purification chemicals, namely, chemicals for use in purifying water; chemicals in the nature of sealing preparations, namely, industrial adhesives for use in coating and sealing. Industrial oils and greases, wax; lubricants, namely, naphtha; dust absorbing, wetting and binding compositions; fuels; biofuel; non-chemical additives for oil, fuel, lubricants, greases, petroleum products; alcohol fuel; biodiesel fuel; biomass fuels; emulsions of oil for use as a fuel; emulsions of bitumen for use as fuel; fuel mixtures featuring primarily fuels Treatment of materials in the nature of plastic, glass, metal and stone; recycling; recycling of waste and trash; recycling of plastic; recycling of materials; recycling plants; air purification and treatment of water; catalytic conversion of chemical compounds in the nature of chemical treatment; chemical processing of liquids; chemical treatment of waste products; chemical treatment of plastics; chemical recycling; treatment of chemicals in the nature of recycling; treatment of waste in the nature of recycling; upcycling in the nature of waste recycling; carbon offsetting services in the nature of recycling Unprocessed and semi-processed rubber, gutta-percha, gum, asbestos, mica and substitutes for all these materials; plastics and resins in extruded form for use in manufacture; packing, stopping and insulating materials; recycled plastic in the form of pellets for use in further manufacturing; recycled rubber in the form of pellets for use in further manufacturing; semi-finished chemical resins; acrylic based sealants and adhesives Materials, not of metal, for building and construction, namely, bitumen-based compositions for building purposes; asphalt, pitch, tar and bitumen; composite bitumen; mixtures of bitumen and plastics for building purposes; mixtures of bitumen and plastics for making roads; bitumen binding material consisting primarily of foamed bitumen; bituminous coatings for roofing; bituminous materials other than paint in the nature of foamed bitumen for building and construction; bituminous preparations other than paint in the nature of foamed bitumen for building and construction; bituminous products other than paint in the nature of foamed bitumen for building and construction; coating preparations other than paints or oils, namely, tar coatings for use on roofs, walls and pavements; coating materials, namely, tar coatings for use on roofs, walls and pavements Scientific and technological services, namely, research and design in the field of petrochemicals; industrial analysis in the nature of chemical analysis, analysis of industrial fluids; industrial research in the nature of chemical research and scientific research and development; industrial design; quality control of goods and services and authentication services in the field of petrochemicals; testing of chemicals; chemistry services in the nature of research and consultancy in the field of chemistry; measurement services in the nature of air flow measurement services; providing information, including online, about industrial analysis and research services; material testing; scientific research services for assessing the efficiency of chemicals; services for monitoring industrial processes, namely, monitoring of equipment in industrial facilities; technical data analysis services in the field of petrochemicals and recycling; technical diagnostic testing services in the field of recycling equipment; scientific and technological analysis services in the field of petrochemicals and recycling; technological consultation services in the field of petrochemicals and recycling; chemical analysis; chemical information, namely, providing information in the field of chemical analysis; chemical technological research; scientific research in the field of chemicals; scientific research in the field of chemistry; scientific research in the field of chemical products; testing of chemicals; biotechnological research; biotechnology research; biotechnology testing; scientific research in the field of biotechnology
37 - Construction and mining; installation and repair services
40 - Treatment of materials; recycling, air and water treatment,
42 - Scientific, technological and industrial services, research and design
Goods & Services
Procurement, namely, purchasing of equipment, machinery, process units, supplies related to engineering and construction equipment, and associated equipment for utility, industrial, commercial, governmental, public works, public accommodation, and infrastructure facilities, structures, and plants for others; business management services, namely, contract administration and project management services Construction, installation, repair, renovation, and replacement services of public and private accommodations and infrastructure facilities, building structures, plants, equipment; maintenance services, namely, building maintenance services in the public and private sectors, namely, utility, industrial, and commercial companies and governments; inspection and supervisory services associated therewith in the course of construction, installation, repair, renovation and replacement of the forgoing in the public and private sectors, namely, utility, industrial, and commercial companies and government; construction, maintenance, and repair services for buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries. Biomass gasification services, treatment of waste water; waste to energy generation services Architectural and engineering services for the design of buildings, plants, structures, operating and processing facilities, and equipment for the aviation, biofuel, carbon capture and storage, chemical, gas-to-liquids, liquified natural gas, manufacturing, mining and minerals, oil and gas, petrochemical, pipeline, power generation and transmission, pulp and paper, refining, renewable energy, transportation, water supply, and wastewater handling industries; engineering services in the field of reducing carbon dioxide emissions; engineering services in the field of reducing nitrogen oxide emissions; Engineering in the public and private sectors, namely, utility, industrial, and commercial companies and governments; design services, namely, architectural design in the public and private sectors, namely, utility, industrial, and commercial companies and governments; Information technology consultation services, namely, enterprise IT consolidation, help desk and network management, telecommunications sustainment and modernization, information assurance and computer network defense; Engineering services and computer engineering services in the field of cybersecurity; Developing computer software for others; and Scientific research services in the field of aerospace development, national defense, and commercial nuclear power; Scientific and technical research, engineering, and testing in the fields of aerospace development, national defense, and commercial nuclear power provided to firms in those industries; Engineering services for computer security purposes, namely, protecting data and information from unauthorized access
A system for reactivating a catalyst having a predetermined heat content includes a reactor, a regenerator, and an electrically energized heater. The reactor is configured to generate a spent catalyst. The regenerator is configured to receive the spent catalyst from the reactor. The electrically energized heater has a plurality of energy emitting members at least partially immersed in the spent catalyst. The heater is configured to provide a supplemental heat content to obtain the predetermined heat content.
B01J 8/26 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles
04 - Industrial oils and greases; lubricants; fuels
35 - Advertising and business services
40 - Treatment of materials; recycling, air and water treatment,
42 - Scientific, technological and industrial services, research and design
Goods & Services
Fuels; aviation fuel; hydrocarbon fuels; non-chemical
additives for fuels. Providing fuel business management services in the field of
aviation. Fuel treatment services; processing of fuel materials;
production, treatment and refinement of fuel, diesel fuel,
biofuel and biodiesel fuel for others. Engineering services in the field of reducing fuel
consumption; technology consultation services in the field
of alternative energy, namely, gasifying and combusting
alternative fuels.
55.
ELECTRIFICATION OF HEAT SUPPLY TO FLUIDIZED REGENERATION SYSTEM
A system for reactivating a catalyst having a predetermined heat content includes a reactor, a regenerator, and an electrically energized heater. The reactor is configured to generate a spent catalyst. The regenerator is configured to receive the spent catalyst from the reactor. The electrically energized heater has a plurality of energy emitting members at least partially immersed in the spent catalyst. The heater is configured to provide a supplemental heat content to obtain the predetermined heat content.
B01J 8/26 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
A method of evaluating one or more aspects of a low carbon ammonia production facility uses a digital twin implemented on a computer system. The digital twin includes a low carbon energy source component and one or more of: a hydrogen source component, a nitrogen source component, and an ammonia synthesis loop component.
G06Q 10/04 - Forecasting or optimisation specially adapted for administrative or management purposes, e.g. linear programming or "cutting stock problem"
A method of evaluating one or more aspects of a low carbon ammonia production facility uses a digital twin implemented on a computer system. The digital twin includes a low carbon energy source component and one or more of: a hydrogen source component, a nitrogen source component, and an ammonia synthesis loop component.
G06Q 10/04 - Forecasting or optimisation specially adapted for administrative or management purposes, e.g. linear programming or "cutting stock problem"
G05B 15/02 - Systems controlled by a computer electric
A system for processing a selected feedstock using a catalyst includes a reactor, a catalyst recovery system, and a conduit. The reactor receives the catalyst and the selected feedstock. A reaction between the selected feedstock and the catalyst generates a spent catalyst. The catalyst recovery system processes the spent catalyst. The conduit connects the reactor to the catalyst recovery system and has a lateral section. The spent catalyst flows from the reactor through a flow space defined by an inner wall of the lateral section to the catalyst recovery system. The system also includes a fluidizer positioned at the lateral section. The fluidizer includes at least one nozzle. The at least one nozzle is completely inside the flow space. The at least one nozzle forms and directs a jet of a fluidizing agent into the spent catalyst in the lateral section.
B01J 8/26 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
B01J 4/00 - Feed devicesFeed or outlet control devices
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
60.
FLUIDIZATION OF CATALYST IN LATERAL SECTIONS OF A SYSTEM
A system for processing a selected feedstock using a catalyst includes a reactor, a catalyst recovery system, and a conduit. The reactor receives the catalyst and the selected feedstock. A reaction between the selected feedstock and the catalyst generates a spent catalyst. The catalyst recovery system processes the spent catalyst. The conduit connects the reactor to the catalyst recovery system and has a lateral section. The spent catalyst flows from the reactor through a flow space defined by an inner wall of the lateral section to the catalyst recovery system. The system also includes a fluidizer positioned at the lateral section. The fluidizer includes at least one nozzle. The at least one nozzle is completely inside the flow space. The at least one nozzle forms and directs a jet of a fluidizing agent into the spent catalyst in the lateral section.
7 aromatic rich hydrocarbons that is recycled and mixed with quench water going to the quench water separator drum to assist in removing tar molecules out of the quench water.
C10G 53/04 - Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only including at least one extraction step
62.
ADVANCED CONTROL AND RELATED METHODS FOR A LOW CARBON AMMONIA FACILITY
Advanced control and related methods for a low carbon ammonia facility having an ammonia synthesis loop that includes systems to carry out the steps of supplying energy to the facility, wherein at least a portion of the supplied energy is from a low carbon energy source, receiving a forecasted energy profile for the low carbon energy source over a time period, predicting, using an advanced regulatory controller (ARC), the operating conditions of the facility based on the forecasted energy profile for the low carbon energy source, generating, by the ARC, one or more set points to control the facility; controlling the generating of the hydrogen feed using the ARC; and producing ammonia by feeding the generated hydrogen feed to the ammonia synthesis loop in accordance with one or more set points generated by the ARC.
Advanced control and related methods for a low carbon ammonia facility having an ammonia synthesis loop that includes systems to carry out the steps of supplying energy to the facility, wherein at least a portion of the supplied energy is from a low carbon energy source, receiving a forecasted energy profile for the low carbon energy source over a time period, predicting, using an advanced regulatory controller (ARC), the operating conditions of the facility based on the forecasted energy profile for the low carbon energy source, generating, by the ARC, one or more set points to control the facility; controlling the generating of the hydrogen feed using the ARC; and producing ammonia by feeding the generated hydrogen feed to the ammonia synthesis loop in accordance with one or more set points generated by the ARC.
37 - Construction and mining; installation and repair services
42 - Scientific, technological and industrial services, research and design
Goods & Services
Construction project management services; construction
project management services in the field of pipelines,
offshore platforms, buildings and infrastructure, oil and
gas processing plants and petrochemical plants and
associated utilities; construction project management
services in the field of reducing carbon dioxide emissions. Consulting services for others in the field of design,
planning, and implementation project management of
pipelines, offshore platforms, buildings and infrastructure,
oil and gas processing plants and petrochemical plants and
associated utilities; engineering services in the field of
reducing carbon dioxide emissions; measurement and
verification of carbon dioxide and other greenhouse gas
emission offsets; research in the reduction of carbon
emissions.
65.
Methods and systems for alkylate production involving a multi-zone alkylation reactor
Methods and systems for alkylate production involving a multi-zone alkylation reactor. The multi-zone alkylation reactor includes a plurality of alkylation zones spaced vertically in a series configuration and a partition splitting the plurality of alkylation zones into at least two mechanically separated catalytic volumes.
B01J 8/04 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
C07C 2/54 - Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition of unsaturated hydrocarbons to saturated hydrocarbons, or to hydrocarbons containing a six-membered aromatic ring with no unsaturation outside the aromatic ring
C07C 2/76 - Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
66.
Dimerization of cyclopentadiene from side stream from debutanizer
7 rich bottoms stream are directed to a dimerizer where the CPD is thermally dimerized to dicyclopentadiene (DCPD). DCPD is more stable than CPD and thus safer to handle.
C07C 2/38 - Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of dienes or alkynes
B01J 19/00 - Chemical, physical or physico-chemical processes in generalTheir relevant apparatus
C07C 7/04 - Purification, separation or stabilisation of hydrocarbonsUse of additives by distillation
C07C 13/61 - Bridged indenes, e.g. dicyclopentadiene
67.
SYSTEMS AND RELATED METHODS FOR THE CALCULATION OF EMBODIED AND OPERATIONAL LIFECYCLE CARBON EMISSIONS FOR INFRASTRUCTURE PROJECTS
A method of estimating a carbon emission lifecycle footprint of an infrastructure project includes compiling a rules set that include carbon emission rules and engineering rules, wherein each carbon emission rule and each engineering rule represent a predetermined decision; encoding the rules set in a database; obtaining non-project specific information from suppliers and manufacturers; storing non-project specific information in the database; obtaining project specific information for the energy project; conveying the project specific information via a user interface to the database; generating deliverables using at least the rules set, the non-project specific information, and the project specific information; using the deliverables to estimate the carbon emission lifecycle footprint of the project; and using the workshop and interactive engineering facility to deliver a lower overall carbon emission footprint of the infrastructure project.
37 - Construction and mining; installation and repair services
42 - Scientific, technological and industrial services, research and design
Goods & Services
(1) Construction project management services; construction project management services in the field of pipelines, offshore platforms, buildings and infrastructure, oil and gas processing plants and petrochemical plants and associated utilities; construction project management services in the field of reducing carbon dioxide emissions.
(2) Consulting services for others in the field of design, planning, and implementation project management of pipelines, offshore platforms, buildings and infrastructure, oil and gas processing plants and petrochemical plants and associated utilities; engineering services in the field of reducing carbon dioxide emissions; measurement and verification of carbon dioxide and other greenhouse gas emission offsets; research in the reduction of carbon emissions.
Low carbon dioxide-emitting processes and systems for steam cracking hydrocarbons to produce products such as ethylene are described. The processes and systems involve cracking the feed in a furnace that is configured to burn a hydrogen-rich fuel, which produces less carbon dioxide than methane, which is typically used as fuel for such furnaces. The hydrogen-rich stream can be isolated and recycled from the cracker tail gas.
Low carbon dioxide-emitting processes and systems for steam cracking hydrocarbons to produce products such as ethylene are described. The processes and systems involve cracking the feed in a furnace that is configured to burn a hydrogen-rich fuel, which produces less carbon dioxide than methane, which is typically used as fuel for such furnaces. The hydrogen-rich stream can be isolated and recycled from the cracker tail gas.
42 - Scientific, technological and industrial services, research and design
Goods & Services
Consulting services in the field of design and development
of engineering processes; engineering design services;
engineering services in the field of energy efficiency;
engineering services in the field of hydrogen production.
04 - Industrial oils and greases; lubricants; fuels
35 - Advertising and business services
40 - Treatment of materials; recycling, air and water treatment,
42 - Scientific, technological and industrial services, research and design
Goods & Services
(1) Fuels; aviation fuel; hydrocarbon fuels; non-chemical additives for fuels. (1) Providing fuel business management services in the field of aviation.
(2) Fuel treatment services; processing of fuel materials; production, treatment and refinement of fuel, diesel fuel, biofuel and biodiesel fuel for others.
(3) Engineering services in the field of reducing fuel consumption; technology consultation services in the field of alternative energy, namely, gasifying and combusting alternative fuels.
A process of dissociating ammonia into a dissociated hydrogen/nitrogen stream in catalyst tubes within a radiant tube furnace and an adiabatic or isothermal unit containing catalyst, along with downstream purification process units to purify the dissociated hydrogen/nitrogen stream into high purity hydrogen product.
C01B 3/04 - Production of hydrogen or of gaseous mixtures containing hydrogen by decomposition of inorganic compounds, e.g. ammonia
B01J 19/24 - Stationary reactors without moving elements inside
B01J 15/00 - Chemical processes in general for reacting gaseous media with non-particulate solids, e.g. sheet materialApparatus specially adapted therefor
B01J 19/00 - Chemical, physical or physico-chemical processes in generalTheir relevant apparatus
B01D 3/32 - Other features of fractionating columns
B01D 3/00 - Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
B01D 53/14 - Separation of gases or vapoursRecovering vapours of volatile solvents from gasesChemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases or aerosols by absorption
Processes and systems for fluid catalytic cracking (FCC) of hydrocarbon feeds using a multiple riser FCC reactor are described. The conditions in each riser can be tailored for handling a different feed. For example, one riser may be configured to crack heavy hydrocarbons, such as vacuum gas oil (VGO) to yield medium and light products. Other risers may be configured to crack low and/or medium hydrocarbons to yield light olefins. Embodiments of the disclosed processes and systems may be used to provide a product spectrum that has greater amounts of light olefins.
C10G 11/05 - Crystalline alumino-silicates, e.g. molecular sieves
C10G 51/04 - Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only including only thermal and catalytic cracking steps
76.
Converting Motor Fuels Range Distillates to Light Olefins in a Multiple Riser Fluid Catalytic Cracking (FCC) Unit
Processes and systems for fluid catalytic cracking (FCC) of hydrocarbon feeds using a multiple riser FCC reactor are described. The conditions in each riser can be tailored for handling a different feed. For example, one riser may be configured to crack heavy hydrocarbons, such as vacuum gas oil (VGO) to yield medium and light products. Other risers may be configured to crack low and/or medium hydrocarbons to yield light olefins. Embodiments of the disclosed processes and systems may be used to provide a product spectrum that has greater amounts of light olefins.
A process of dissociating ammonia into a dissociated hydrogen/nitrogen stream in catalyst tubes within a radiant tube furnace and an adiabatic or isothermal unit containing catalyst, along with downstream purification process units to purify the dissociated hydrogen/nitrogen stream into high purity hydrogen product.
42 - Scientific, technological and industrial services, research and design
Goods & Services
Engineering services, namely, engineering for the design of
steam cracking-based ethylene production processes combining
a furnace and recovery section process; engineering services
in the field of reducing emissions in ethylene production.
42 - Scientific, technological and industrial services, research and design
Goods & Services
(1) Consulting services in the field of design and development of engineering processes, namely, consulting services in the field of energy efficiency, hydrogen production; engineering design services, namely, design and engineering in the field of energy efficiency, hydrogen production; engineering services in the field of energy efficiency; engineering services in the field of hydrogen production.
81.
Reactor system for saturated C3-C6 hydrocarbon dehydrogenation
A reactor system and method for catalytic dehydrogenation of saturated C3-C6 hydrocarbons within a reactor placed within a reactor disengager, where the reactor is open at the bottom thereof and open to the disengager, and the exit riser from the reactor is not hard coupled to at least one downstream cyclone. This configuration permits controlling the amount of catalyst within the reactor by varying the level of catalyst in the reactor disengager outside the reactor and permits controlling total catalyst hold-up and/or weight hourly space velocity (WHSV) independently from catalyst flow from the catalyst regenerator.
B01J 8/00 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
82.
Recovery of light olefins from dry hydrocarbon gas from refinery and petrochemical production processes for production of alkylate
Methods and systems for treating an olefin-containing stream are disclosed. The disclosed methods and systems are particularly suitable for treating an off-gas stream in a refining or petrochemical process, such as from a fluid catalytic cracker (FCC), coker, steam cracker, and the like. The stream is treated in an absorber column to reject lighter stream components and to absorb ethylene and/or propylene into a solvent. The solvent is typically isobutane. The enriched solvent stream from the absorber column is fed to an alkylation reactor, which reacts the dissolved olefin with the isobutane solvent to produce an alkylate product.
C07C 7/11 - Purification, separation or stabilisation of hydrocarbonsUse of additives by absorption, i.e. purification or separation of gaseous hydrocarbons with the aid of liquids
B01D 53/14 - Separation of gases or vapoursRecovering vapours of volatile solvents from gasesChemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases or aerosols by absorption
B01J 8/02 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with stationary particles, e.g. in fixed beds
C07C 2/12 - Catalytic processes with crystalline alumino-silicates, e.g. molecular sieves
C07C 7/00 - Purification, separation or stabilisation of hydrocarbonsUse of additives
C07C 7/09 - Purification, separation or stabilisation of hydrocarbonsUse of additives by fractional condensation
83.
REACTOR SYSTEM FOR SATURATED C3-C6 HYDROCARBON DEHYDROGENATION
A reactor system and method for catalytic dehydrogenation of saturated C3-C6 hydrocarbons within a reactor placed within a reactor disengager, where the reactor is open at the bottom thereof and open to the disengager, and the exit riser from the reactor is not hard coupled to at least one downstream cyclone. This configuration permits controlling the amount of catalyst within the reactor by varying the level of catalyst in the reactor disengager outside the reactor and permits controlling total catalyst hold-up and/or weight hourly space velocity (WHSV) independently from catalyst flow from the catalyst regenerator.
B01J 8/26 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
B01J 38/04 - Gas or vapour treatingTreating by using liquids vaporisable upon contacting spent catalyst
C07C 5/327 - Formation of non-aromatic carbon-to-carbon double bonds only
B01J 8/24 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique
84.
INTEGRATED CARBON CAPTURE AND OLEFINS PRODUCTION PROCESS
Carbon capture of carbon dioxide (CO2) gives an extracted CO2 stream that is reacted with hydrogen to produce methanol (MeOH), which can in turn be fed to catalytic production of olefins such as ethylene and propylene to give an integrated process.
C01B 3/34 - Production of hydrogen or of gaseous mixtures containing hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
C07C 1/12 - Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of carbon from carbon dioxide with hydrogen
85.
INTEGRATED CARBON CAPTURE AND OLEFINS PRODUCTION PROCESS
222 stream that is reacted with hydrogen to produce methanol (MeOH), which can in turn be fed to catalytic production of olefins such as ethylene and propylene to give an integrated process.
B01D 53/02 - Separation of gases or vapoursRecovering vapours of volatile solvents from gasesChemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases or aerosols by adsorption, e.g. preparative gas chromatography
B01D 53/34 - Chemical or biological purification of waste gases
B01D 53/73 - After-treatment of removed components
42 - Scientific, technological and industrial services, research and design
Goods & Services
Consulting in the field of engineering; Electrical engineering; Engineering design services; Engineering drawing services; Engineering services, namely, engineering for the design and construction of facilities to store electricity; Technology advisory services related to civil engineering and construction
42 - Scientific, technological and industrial services, research and design
Goods & Services
Consultancy in the field of artificial intelligence technology; Providing temporary use of on-line non-downloadable software and applications using artificial intelligence for engineering and design of processes and facilities in the utility, industrial, transportation, building, mining, commercial, aerospace, power, defense and government industries; Research in the field of artificial intelligence technology; Software as a service (SAAS) services featuring software using artificial intelligence for engineering and design of processes and facilities in the ammonia, aviation, biofuel, carbon capture, carbon storage, chemical, coal gasification, coal monetization, fertilizer, gas, gas-to-liquids, hydrogen, liquified natural gas, manufacturing, minerals, mining, oil, olefins, organic chemical, paper, petrochemical, pipeline, power generation, power transmission, pulp, refining, renewable energy, synthesis gas, transportation, water supply and wastewater handling industries
88.
PROCESSES FOR CATALYTIC PARAFFIN DEHYDROGENATION AND CATALYST RECOVERY
A paraffin having 2-8 carbon atoms may be dehydrogenated by contacting the paraffin with metal oxide catalyst(s) to produce light olefins, such as propylene, under certain reaction conditions in a riser, fluidized bed, or fixed-bed swing reactor. The resulting metal oxide catalyst fines contained in the reactor effluent stream formed by the dehydrogenation reaction may be recovered by contacting the reactor effluent stream with a wash fluid to form a catalyst effluent stream that is subsequently slurried and filtered to capture the catalyst fines for potential reuse.
C07C 5/32 - Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
C07C 5/327 - Formation of non-aromatic carbon-to-carbon double bonds only
B01J 23/54 - Catalysts comprising metals or metal oxides or hydroxides, not provided for in group of noble metals combined with metals, oxides or hydroxides provided for in groups
A method of designing a plastic recycling facility at a selected site includes representing each selected component of the plastic recycling facility a module defined by information relating to at least one of a carbon emission or a cost. The method also includes storing the information represented each module in a database accessible by a processor; programming the processor with a set of engineering rules, wherein each engineering rule is configured to represent a predetermined design decision relating to at least a design of the plastic recycling facility; and generating deliverables using at least the set of engineering rules and the modules. The deliverables may include at least: a cost estimate for the plastic recycling facility, and a carbon emission estimate for the plastic recycling facility.
A method of designing a plastic recycling facility at a selected site includes representing each selected component of the plastic recycling facility a module defined by information relating to at least one of a carbon emission or a cost. The method also includes storing the information represented each module in a database accessible by a processor; programming the processor with a set of engineering rules, wherein each engineering rule is configured to represent a predetermined design decision relating to at least a design of the plastic recycling facility; and generating deliverables using at least the set of engineering rules and the modules. The deliverables may include at least: a cost estimate for the plastic recycling facility, and a carbon emission estimate for the plastic recycling facility.
37 - Construction and mining; installation and repair services
42 - Scientific, technological and industrial services, research and design
Goods & Services
Construction project management services; Construction project management services in the field of pipelines, offshore platforms, buildings and infrastructure, oil and gas processing plants and petrochemical plants and associated utilities; Construction project management services in the field of reducing carbon dioxide emissions Consulting services for others in the field of design, planning, and implementation project management of pipelines, offshore platforms, buildings and infrastructure, oil and gas processing plants and petrochemical plants and associated utilities; Engineering services in the field of reducing carbon dioxide emissions; Measurement and verification of carbon dioxide and other greenhouse gas emission offsets; Research in the reduction of carbon emissions
42 - Scientific, technological and industrial services, research and design
Goods & Services
Consulting services in the field of design and development of engineering processes; Engineering design services; Engineering services in the field of energy efficiency; Engineering services in the field of hydrogen production
The present invention relates to debottleneck solution for delayed Coker unit. More particularly, this invention relates to bottoms of vacuum residuum routed to Coker unit through de-asphalting unit to avoid revamp of existing Coker for the processing of heavier feed stock when there is a change in crude slate. Another object of the invention, in particular, relates to improved delayed coking products, a process used in petroleum refineries to crack petroleum residue, thus converting it into gaseous and liquid product streams and leaving behind solid, carbonaceous petroleum coke.
C10G 21/00 - Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
C10G 55/04 - Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only including at least one thermal cracking step
40 - Treatment of materials; recycling, air and water treatment,
35 - Advertising and business services
42 - Scientific, technological and industrial services, research and design
Goods & Services
Fuel treatment services; Processing of fuel materials; Production, treatment and refinement of fuel, diesel fuel, biofuel and biodiesel fuel for others Providing fuel management services in the field of aviation Engineering services in the field of reducing fuel consumption; Technology consultation services in the field of alternative energy, namely, gasifying and combusting alternative fuels
A system for processing a hydrocarbon feed has a final stage reactor and internal separator with cyclone that forms a substantially gas stream and a substantially non-gas stream. The substantially gas stream is sent directly from the final stage reactor and separator to further downstream processing.
C10G 1/10 - Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
B01J 8/00 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes
B01J 8/26 - Chemical or physical processes in general, conducted in the presence of fluids and solid particlesApparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
C10G 1/00 - Production of liquid hydrocarbon mixtures from oil shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
96.
THERMALLY COUPLED DISTILLATION SCHEME FOR PURIFICATION OF CUMENE
A method for purifying cumene may include splitting an alkylation reaction product into a first portion and a second portion; feeding the first portion as mostly a liquid into a benzene column; at least partially vaporizing the second portion in a heater; feeding the at least partially vaporized second portion into the benzene column. A method for purifying cumene may also include the steps of providing a benzene column and a cumene column; directing a liquid side draw from the benzene column to the cumene column, the liquid side draw being a liquid substantially free of DIPB; returning a benzene enriched vapor from the cumene column to the benzene column using an overhead line, the benzene enriched vapor having a higher concentration of benzene than the liquid side draw; and drawing purified cumene from the cumene column.
C07C 6/12 - Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
97.
Thermally coupled distillation scheme for purification of cumene
A method for purifying cumene may include splitting an alkylation reaction product into a first portion and a second portion; feeding the first portion as mostly a liquid into a benzene column; at least partially vaporizing the second portion in a heater; feeding the at least partially vaporized second portion into the benzene column. A method for purifying cumene may also include the steps of providing a benzene column and a cumene column; directing a liquid side draw from the benzene column to the cumene column, the liquid side draw being a liquid substantially free of DIPB; returning a benzene enriched vapor from the cumene column to the benzene column using an overhead line, the benzene enriched vapor having a higher concentration of benzene than the liquid side draw; and drawing purified cumene from the cumene column.
41 - Education, entertainment, sporting and cultural services
Goods & Services
Providing educational mentoring services and programs in the
field of sustainability and environmental protection;
Providing science educational mentoring services and
programs.
42 - Scientific, technological and industrial services, research and design
Goods & Services
Engineering services, namely, engineering for the design of steam cracking-based ethylene production processes combining a furnace and recovery section process; Engineering services in the field of reducing emissions in ethylene production
42 - Scientific, technological and industrial services, research and design
Goods & Services
Chemical engineering, namely, design and production of methane carboxylic acid (acetic acid) from methanol and carbon monoxide; Engineering design services for the production of methane carboxylic acid (acetic acid) from methanol and carbon monoxide
