The invention provides a method capable of producing a monocyclic aromatic hydrocarbon such as benzene or xylene effective as a base raw material, with a naphtha raw material containing renewable naphtha. The method for producing at least one monocyclic aromatic hydrocarbon of benzene or xylene with a naphtha raw material containing renewable naphtha includes step (A-1) of pyrolyzing the naphtha raw material in the presence of water vapor, to produce and separate toluene, and step (A-2) of subjecting toluene to disproportionation reaction or transalkylation reaction, to produce and separate at least one monocyclic aromatic hydrocarbon of benzene or xylene.
C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds
C07C 6/12 - Préparation d'hydrocarbures à partir d'hydrocarbures contenant un nombre différent d'atomes de carbone par des réactions de redistribution par conversion d'une liaison carbone-carbone saturée exclusivement dans les hydrocarbures contenant un cycle aromatique à six chaînons
C07C 7/04 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par distillation
C07C 7/10 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par extraction, c.-à-d. purification ou séparation d'hydrocarbures liquides à l'aide de liquides
C07C 7/12 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par adsorption, c.-à-d. purification ou séparation d'hydrocarbures à l'aide de solides, p. ex. à l'aide d'échangeurs d'ions
C07C 7/14 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par cristallisationPurification ou séparation des cristaux
C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène
A cooling liquid for an immersion cooling system is provided, which is contained in a liquid immersion tank of an immersion cooling system as a cooling liquid, the cooling liquid containing a hydrocarbon oil and one or more antioxidants selected from the group consisting of an amine-based antioxidant and a phenol-based antioxidant, in which the hydrocarbon oil is contained in an amount of 50% by mass or more with respect to the total amount of the cooling liquid for an immersion cooling system, a 5% distillation temperature of the cooling liquid for an immersion cooling system is 320° C. or higher, a % CN is 30.0 or less, and a kinematic viscosity at 40° C. is 11.5 mm2/s or more.
A lubricating oil additive composition including: (i) a Broensted acid salt of at least one first amide compound, the Broensted acid salt being a salt of the first amide compound and a Broensted acid, the first amide compound being a monoamide of at least one fatty acid (a1), and at least one amine compound (a2), the amine compound (a2) being an oligomer of at least one alkanolamine (a3) represented by the general formula (1):
A lubricating oil additive composition including: (i) a Broensted acid salt of at least one first amide compound, the Broensted acid salt being a salt of the first amide compound and a Broensted acid, the first amide compound being a monoamide of at least one fatty acid (a1), and at least one amine compound (a2), the amine compound (a2) being an oligomer of at least one alkanolamine (a3) represented by the general formula (1):
A lubricating oil additive composition including: (i) a Broensted acid salt of at least one first amide compound, the Broensted acid salt being a salt of the first amide compound and a Broensted acid, the first amide compound being a monoamide of at least one fatty acid (a1), and at least one amine compound (a2), the amine compound (a2) being an oligomer of at least one alkanolamine (a3) represented by the general formula (1):
in the formula, n is 1 or 2; R1 is C1-4 linear chain alkylene or C3-10 branched chain alkylene, the C3-10 branched chain alkylene having a main chain, the main chain having a carbon number of 2; and when n is 2, a plurality of R1's may be the same, and may be different from each other.
C10M 139/00 - Compositions lubrifiantes caractérisées en ce que l'additif est un composé organique non macromoléculaire contenant des atomes d'éléments non prévus dans l'un des groupes
C10M 177/00 - Méthodes particulières de préparation des compositions lubrifiantesModification chimique par post-traitement des constituants ou de la composition lubrifiante elle-même, non couverte par d'autres classes
A diagnosis method according to the present disclosure is a diagnosis method for diagnosing deterioration of lubricating oil. The lubricating oil contains a phenolic antioxidant. The diagnosis method comprises: detecting the color of the lubricating oil with a color sensor, and thus acquiring RGB data from the color sensor; and diagnosing deterioration of the lubricating oil on the basis of B data of the RGB data.
A device according includes at least one memory, and at least one processor. The at least one processor is configured to: generate a score by using a neural network; calculate a derivative value of the score by applying back propagation to the neural network; set a search condition for an optimal solution of the score by using an index indicating an uncertainty of the score, the derivative value of the score, and the score; and determine the optimal solution of the score by a gradient method using the search condition.
This device for producing an organic hydride includes: an electrolytic cell comprising an electrolyte membrane, an anode provided on one side of the electrolyte membrane, and a cathode provided on the other side of the electrolyte membrane; and a cleaning part for cleaning the anode with pure water so as to result in a pH of 5 or higher.
C25B 9/00 - Cellules ou assemblages de cellulesÉléments de structure des cellulesAssemblages d'éléments de structure, p. ex. assemblages d'électrode-diaphragmeCaractéristiques des cellules relatives aux procédés
C25B 9/23 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes comprenant des membranes échangeuses d'ions dans ou sur lesquelles est incrusté du matériau pour électrode
An organic hydride production device according to the present invention is used in producing an organic hydride in an electrolytic cell having an electrolyte membrane, an anode electrode installed on one side of the electrolyte membrane, and a cathode electrode installed on the other side of the electrolyte membrane. The organic hydride production device comprises a control unit for controlling the output of a power source unit that supplies electrical power to the electrolytic cell. The control unit performs an output change process for increasing or decreasing the current flowing between the anode electrode and the cathode electrode when the Faraday efficiency has become equal to or less than a threshold value.
C25B 9/00 - Cellules ou assemblages de cellulesÉléments de structure des cellulesAssemblages d'éléments de structure, p. ex. assemblages d'électrode-diaphragmeCaractéristiques des cellules relatives aux procédés
C25B 9/23 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes comprenant des membranes échangeuses d'ions dans ou sur lesquelles est incrusté du matériau pour électrode
C25B 15/023 - Mesure, analyse ou test pendant la production électrolytique
Provided is a technique by which it becomes possible to produce a high-purity bioethanol raw material from waste paper that contains a metal or an organic material layer other than paper. The bioethanol raw material is derived from waste paper that contains at least one of a metal and an organic material layer other than paper, wherein the total content ratio of cellulose and hemicellulose in solid content is in the range of 90.0 to 99.5 mass%, the content ratio of organic materials excluding the cellulose, the hemicellulose and lignin in the solid content is in the range of 0.25 to 5.0 mass%, and the ash content ratio in the solid content is in the range of 0.25 to 5.0 mass%.
C12P 19/04 - Polysaccharides, c.-à-d. composés contenant plus de cinq radicaux saccharide reliés entre eux par des liaisons glucosidiques
B09B 3/30 - Destruction de déchets solides ou transformation de déchets solides en quelque chose d'utile ou d'inoffensif impliquant un traitement mécanique
A lubricating oil additive composition including: (i) at least one first amide compound, and/or a salt thereof, the at least one first amide compound being a monoamide of at least one fatty acid (a1), and at least one amine compound (a2), the amine compound (a2) being an oligomer of at least one alkanolamine (a3) represented by the general formula (1); and (ii) at least one second amide compound having a structure such that an amino group and at least one hydroxy group of the alkanolamine (a3) are acylated with the fatty acid (a1):
A lubricating oil additive composition including: (i) at least one first amide compound, and/or a salt thereof, the at least one first amide compound being a monoamide of at least one fatty acid (a1), and at least one amine compound (a2), the amine compound (a2) being an oligomer of at least one alkanolamine (a3) represented by the general formula (1); and (ii) at least one second amide compound having a structure such that an amino group and at least one hydroxy group of the alkanolamine (a3) are acylated with the fatty acid (a1):
A lubricating oil additive composition including: (i) at least one first amide compound, and/or a salt thereof, the at least one first amide compound being a monoamide of at least one fatty acid (a1), and at least one amine compound (a2), the amine compound (a2) being an oligomer of at least one alkanolamine (a3) represented by the general formula (1); and (ii) at least one second amide compound having a structure such that an amino group and at least one hydroxy group of the alkanolamine (a3) are acylated with the fatty acid (a1):
in the formula, n is 1 or 2; R1 is C1-4 linear chain alkylene or C3-10 branched chain alkylene having a main chain, the main chain having a carbon number of 2; and when n is 2, a plurality of R1's may be the same, and may be different from each other.
C10M 171/00 - Compositions lubrifiantes caractérisées par des critères purement physiques, p. ex. contenant comme matériau de base, épaississant ou additif des ingrédients exclusivement caractérisés par des valeurs numériques particulières de leurs propriétés physiques, c.-à-d. contenant des ingrédients physiquement bien définis mais dont la nature chimique n'est pas précisée ou n'est que très vaguement indiquée
C09K 5/04 - Substances qui subissent un changement d'état physique lors de leur utilisation le changement d'état se faisant par passage de l'état liquide à l'état vapeur ou vice versa
F25B 1/00 - Machines, installations ou systèmes à compression à cycle irréversible
C10N 20/00 - Propriétés physiques particulières des constituants des compositions lubrifiantes
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
C10N 40/30 - Lubrifiants pour machines frigorifiques
11.
DEVICE FOR PRODUCING ORGANIC HYDRIDE, SYSTEM FOR PRODUCING ORGANIC HYDRIDE, AND METHOD FOR REUSING MIGRATION WATER
A device for producing an organic hydride according to the present invention produces the organic hydride in an electrolytic cell comprising an electrolyte membrane, an anode disposed on one side of the electrolyte membrane, and a cathode disposed on the other side of the electrolyte membrane, said device being equipped with: an anolyte supply part for supplying an anolyte to the anode; and an aeration part in which a gas including at least one of oxygen and nitrogen is supplied as an aeration gas to migration water separated from a catholyte and organic matter dissolved in the migration water is separated therefrom, and from which the migration water having a reduced concentration of dissolved organic matter is supplied to the anolyte supply part.
C25B 9/00 - Cellules ou assemblages de cellulesÉléments de structure des cellulesAssemblages d'éléments de structure, p. ex. assemblages d'électrode-diaphragmeCaractéristiques des cellules relatives aux procédés
C25B 9/19 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes
12.
PYROLYSIS OIL, ELASTOMER, RUBBER PRODUCT, AND RESIN PRODUCT
The present invention addresses the problem of providing a pyrolysis oil which is easy to use as a raw material for chemical products. This pyrolysis oil is obtained by pyrolyzing a waste material including used tires, and is characterized by having a 90% distillation temperature of 400°C or lower and an olefin content, as determined by GC×GC-MS, of 10 vol% or higher.
C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
C08F 301/00 - Composés macromoléculaires non prévus dans les groupes
C08J 11/12 - Récupération ou traitement des résidus des polymères par coupure des chaînes moléculaires des polymères ou rupture des liaisons de réticulation par voie chimique, p. ex. dévulcanisation uniquement par traitement à la chaleur sèche
13.
PYROLYSIS OIL, ELASTOMER, RUBBER PRODUCT, AND RESIN PRODUCT
The present invention addresses the problem of providing a pyrolysis oil that is easy to use as a raw material for a chemical product. The problem is solved by a pyrolysis oil obtained by thermally decomposing a waste material containing used tires, the pyrolysis oil being characterized by having an aromatic content of at most 80 vol% as measured by GC×GC-MS and a 90% distillation temperature of at most 400 °C.
C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
C08F 301/00 - Composés macromoléculaires non prévus dans les groupes
C08J 11/12 - Récupération ou traitement des résidus des polymères par coupure des chaînes moléculaires des polymères ou rupture des liaisons de réticulation par voie chimique, p. ex. dévulcanisation uniquement par traitement à la chaleur sèche
14.
ORGANIC HYDRIDE PRODUCTION DEVICE, ORGANIC HYDRIDE PRODUCTION SYSTEM, AND ORGANIC HYDRIDE PRODUCTION METHOD
An organic hydride production device provided with an electrolytic cell that has an electrolyte membrane, an anode chamber disposed on one side of the electrolyte membrane and accommodating an anode solution and an anode, and a cathode chamber disposed on the other side of the electrolytic membrane and accommodating a cathode, wherein the liquid level of the anode solution in the anode chamber is equal to or higher than the height of the upper end surface of the cathode.
C25B 9/00 - Cellules ou assemblages de cellulesÉléments de structure des cellulesAssemblages d'éléments de structure, p. ex. assemblages d'électrode-diaphragmeCaractéristiques des cellules relatives aux procédés
C25B 9/23 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes comprenant des membranes échangeuses d'ions dans ou sur lesquelles est incrusté du matériau pour électrode
C25B 13/02 - DiaphragmesÉléments d'espacement caractérisés par la configuration ou la forme
15.
METHOD FOR PRODUCING PYROLYSIS OIL, METHOD FOR PRODUCING ELASTOMER, METHOD FOR PRODUCING RUBBER PRODUCT, AND METHOD FOR PRODUCING RESIN PRODUCT
The present invention addresses the problem of providing a method for producing a pyrolysis oil which is a light oil and is rich in olefins. This method for producing a pyrolysis oil is characterized by comprising a step in which a waste material including used tires is pyrolyzed in a pyrolysis furnace to obtain a pyrolysis gas and a solid including a carbide, and a step in which the pyrolysis gas is cooled to obtain a pyrolysis oil, wherein the pyrolysis temperature is 300-500°C and the pyrolysis reaction time is 0.6 minutes or longer.
C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
C08J 11/12 - Récupération ou traitement des résidus des polymères par coupure des chaînes moléculaires des polymères ou rupture des liaisons de réticulation par voie chimique, p. ex. dévulcanisation uniquement par traitement à la chaleur sèche
C10B 53/07 - Distillation destructive spécialement conçue pour des matières premières solides particulières ou sous forme spéciale de matières polymères synthétiques, p. ex. pneumatiques
16.
PYROLYSIS OIL, ELASTOMER, RUBBER PRODUCT, AND RESIN PRODUCT
C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
C08F 301/00 - Composés macromoléculaires non prévus dans les groupes
C08J 11/12 - Récupération ou traitement des résidus des polymères par coupure des chaînes moléculaires des polymères ou rupture des liaisons de réticulation par voie chimique, p. ex. dévulcanisation uniquement par traitement à la chaleur sèche
17.
HYDROGEN GAS INVENTORY ACQUISITION METHOD, HYDROGEN GAS INVENTORY ACQUISITION DEVICE, HYDROGEN GAS INVENTORY ACQUISITION SYSTEM, AND HYDROGEN GAS INVENTORY MANAGEMENT SYSTEM
A management apparatus for managing an inventory amount of a hydrogen gas in a plurality of hydrogen tanks that store hydrogen gas, the management apparatus including a log data receiving circuit configured to receive log data including a plurality of parameter data measured by a plurality of instruments arranged each on hydrogen tank and identification information of each hydrogen tank, and an inventory amount calculation circuit configured to calculate an inventory amount of the hydrogen gas at an individual calculation timing that is individually set for each hydrogen tank based on the log data.
F17C 13/02 - Adaptations spéciales des dispositifs indicateurs, de mesure ou de contrôle
F17C 5/06 - Procédés ou appareils pour remplir des récipients sous pression de gaz liquéfiés, solidifiés ou comprimés pour le remplissage avec des gaz comprimés
A pressure swing adsorption (PSA) device includes an adsorption tower configured to introduce hydrogen gas and adsorb impurity components in the hydrogen gas by using a pressure swing adsorption (PSA) method, an adsorbent of one layer made of activated carbon or an adsorbent of two layers in which activated carbon and zeolite are stacked being disposed in the adsorption tower, the hydrogen gas containing carbon monoxide (CO) of 0.5 vol % or more and 6.0 vol % or less and methane (CH4) of 0.4 vol % or more and 10 vol % or less as the impurity components; and a densitometer configured to detect a concentration of CO in the hydrogen gas discharged from the adsorption tower, wherein the impurity components are adsorbed and removed to cause the CO concentration measured by the densitometer to fall below a threshold.
B01J 20/20 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant du carbone libreCompositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant du carbone obtenu par des procédés de carbonisation
B01J 20/28 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation caractérisées par leur forme ou leurs propriétés physiques
C01B 3/56 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification par contact avec des solidesRégénération des solides usés
37 - Services de construction; extraction minière; installation et réparation
Produits et services
Drilling of oil or gas wells; sealing of oil or gas wells;
workover or maintenance of oil and gas wells; drilling of
CO2 injection wells; sealing of CO2 injection wells;
workover or maintenance of CO2 injection wells; drilling of
wells; sealing of wells; workover or maintenance of wells;
consultancy, information and advisory services relating to
drilling of oil and gas wells; consultancy, information and
advisory services relating to sealing of oil and gas wells;
consultancy, information and advisory services relating to
workover or maintenance of oil and gas wells; consultancy,
information and advisory services relating to drilling of
CO2 injection wells; consultancy, information and advisory
services relating to sealing of CO2 injection wells;
consultancy, information and advisory services relating to
workover or maintenance of CO2 injection wells; consultancy,
information and advisory services relating to drilling of
wells; consultancy, information and advisory services
relating to sealing of wells; consultancy, information and
advisory services relating to workover or maintenance of
wells; construction; construction consultancy; operation and
maintenance of building equipment; shipbuilding; repair or
maintenance of vessels; repair or maintenance of
telecommunication machines and apparatus; repair or
maintenance of construction machines and apparatus; repair
or maintenance of mining machines and apparatus.
A lubricating oil composition including: (A) a lubricant base oil; (B1) a first amide compound, and/or a salt thereof, the first amide compound being a monoamide of a fatty acid (a1), and an amine compound (a2), the compound (a2) being an oligomer of an alkanolamine (a3) of the general formula (1); and (B2) a second amide compound having a structure such that an amino group and at least one hydroxy group of the alkanolamine (a3) are acylated with the fatty acid (a1), wherein the inequation (eq1) is satisfied:
A lubricating oil composition including: (A) a lubricant base oil; (B1) a first amide compound, and/or a salt thereof, the first amide compound being a monoamide of a fatty acid (a1), and an amine compound (a2), the compound (a2) being an oligomer of an alkanolamine (a3) of the general formula (1); and (B2) a second amide compound having a structure such that an amino group and at least one hydroxy group of the alkanolamine (a3) are acylated with the fatty acid (a1), wherein the inequation (eq1) is satisfied:
M
B
2
≥
0
.
5
0
×
M
B
1
(
eq
1
)
A lubricating oil composition including: (A) a lubricant base oil; (B1) a first amide compound, and/or a salt thereof, the first amide compound being a monoamide of a fatty acid (a1), and an amine compound (a2), the compound (a2) being an oligomer of an alkanolamine (a3) of the general formula (1); and (B2) a second amide compound having a structure such that an amino group and at least one hydroxy group of the alkanolamine (a3) are acylated with the fatty acid (a1), wherein the inequation (eq1) is satisfied:
M
B
2
≥
0
.
5
0
×
M
B
1
(
eq
1
)
in the inequation, MB1 and MB2 are a content of the first amide compound, and a content of the (B2) component (mass %), respectively,
A lubricating oil composition including: (A) a lubricant base oil; (B1) a first amide compound, and/or a salt thereof, the first amide compound being a monoamide of a fatty acid (a1), and an amine compound (a2), the compound (a2) being an oligomer of an alkanolamine (a3) of the general formula (1); and (B2) a second amide compound having a structure such that an amino group and at least one hydroxy group of the alkanolamine (a3) are acylated with the fatty acid (a1), wherein the inequation (eq1) is satisfied:
M
B
2
≥
0
.
5
0
×
M
B
1
(
eq
1
)
in the inequation, MB1 and MB2 are a content of the first amide compound, and a content of the (B2) component (mass %), respectively,
A lubricating oil composition including: (A) a lubricant base oil; (B1) a first amide compound, and/or a salt thereof, the first amide compound being a monoamide of a fatty acid (a1), and an amine compound (a2), the compound (a2) being an oligomer of an alkanolamine (a3) of the general formula (1); and (B2) a second amide compound having a structure such that an amino group and at least one hydroxy group of the alkanolamine (a3) are acylated with the fatty acid (a1), wherein the inequation (eq1) is satisfied:
M
B
2
≥
0
.
5
0
×
M
B
1
(
eq
1
)
in the inequation, MB1 and MB2 are a content of the first amide compound, and a content of the (B2) component (mass %), respectively,
in the formula, n is 1 or 2; R1 is C1-4 linear chain alkylene or C3-10 branched chain alkylene having a C2 main chain; and a plurality of R1's may be same, and may be different from each other.
A fuel cell comprising: a cathode catalyst layer containing a cathode-side proton-conductive ionomer; an anode catalyst layer; and an electrolyte layer disposed between the cathode catalyst layer and the anode catalyst layer and containing a proton conductor, wherein the cathode-side proton-conductive ionomer contains a Group 16 element-oxygen-acid compound, and the proton conductor contains a Group 15 element-oxygen-acid compound.
A method for producing a hydrocarbon according to the present disclosure includes a step of subjecting a feedstock to fluid catalytic cracking by using a fluid catalytic cracking unit including a reactor and a regenerator, in which the feedstock includes FT synthetic oil, and a feed temperature x (unit: ° C.) of the feedstock, a feed rate y1 (unit: ton/h) of the feedstock, a feed rate y2 (unit: ton/h) of a fuel oil to be fed into the regenerator, and a circulation rate z1 (unit: ton/h) of a catalyst circulating the reactor and the regenerator satisfy a specific inequality expression.
C10G 11/18 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures avec catalyseurs solides mobiles préchauffés selon la technique du "lit fluidisé"
23.
CONTROL DEVICE FOR WATER ELECTROLYSIS CELL, WATER ELECTROLYSIS SYSTEM, AND CONTROL METHOD FOR WATER ELECTROLYSIS CELL
A water electrolysis cell has: an oxygen generating electrode containing an oxygen generating catalyst; a hydrogen generating electrode containing a hydrogen generating catalyst; and a membrane that separates the oxygen generating electrode and the hydrogen generating electrode, and electrolyzes water to generate oxygen on the oxygen generating electrode and generate hydrogen on the hydrogen generating electrode. A control device controls electric current supply to the water electrolysis cell so that a potential of the oxygen generating electrode is higher than a reduction potential of the oxygen generating catalyst and lower than an oxygen generating potential, and a potential of the hydrogen generating electrode is lower than an oxidation potential of the hydrogen generating catalyst, during an operation stop.
A base oil for refrigerating machine oil containing an α-olefin and a hydrocarbon oil other than the α-olefin. A refrigerating machine oil containing the base oil. A working fluid composition containing the refrigerating machine oil and a refrigerant.
C10M 111/02 - Compositions lubrifiantes caractérisées en ce que le matériau de base est un mélange d'au moins deux composés couverts par plus d'un des groupes principaux , chacun de ces composés étant un composé essentiel l'un d'eux, au moins, étant un composé organique non macromoléculaire
C09K 5/04 - Substances qui subissent un changement d'état physique lors de leur utilisation le changement d'état se faisant par passage de l'état liquide à l'état vapeur ou vice versa
A server device (2) derives a ship distribution plan for transporting, by a plurality of ships, raw materials from a plurality of loading ports to an unloading port, the server device (2) comprising: an acquisition unit (21) that acquires information relating to a plurality of loading port groups into which the loading ports are grouped; a setting unit (22) that sets an index corresponding to each of the loading port groups and including a parameter pertaining to the ship distribution plan as a variable, with the index indicating the total number of stopping ports for the ships in each loading port group, and when one ship stops at a plurality of loading ports belonging to the same loading port group, the number of stopping ports for said ship being counted as a fewer number than the number of loading ports; and a calculation unit (23) that derives each parameter pertaining to the ship distribution plan such that the value of the objective function, set based on the sum of the terms related to the indices corresponding to the respective loading port groups, decreases.
The present invention provides a method for producing a catalyst for Fischer-Tropsch synthesis, with which the activity of the catalyst for Fischer-Tropsch synthesis does not deteriorate or is suppressed from deteriorating. More specifically, provided is a method for producing a catalyst for Fischer-Tropsch synthesis, the method comprising: a step for producing a catalyst precursor by causing a carrier to support a cobalt compound; a step for producing an unreduced catalyst containing a cobalt oxide by drying and firing the catalyst precursor; and a step for reducing the unreduced catalyst to obtain a catalyst that is for FT synthesis and that includes a reduced product of the unreduced catalyst. The unreduced catalyst reduction step includes subjecting the unreduced catalyst to a reduction treatment in a reducing gas and at a first temperature, and thereafter, lowering the temperature to a second temperature, followed by substitution with nitrogen. The first temperature is 300-400°C, and the second temperature is 60-210°C.
A control device of an organic compound producing system including an electrolytic bath and a catholyte supply device, wherein the electrolytic bath has a cathode chamber for accommodating a cathode electrode for reducing a raw material of an organic compound in a catholyte by electrolysis to generate the organic compound, wherein the catholyte supply device is capable of supplying any catholyte selected from a plurality of the catholytes having different concentrations of the raw material to the cathode chamber, and wherein the control device determines a specific concentration of the raw material according to a magnitude of a current flowing in the electrolytic bath and controls the catholyte supply device so as to supply to the cathode chamber the catholyte having the specific concentration of the raw material as determined.
A server device (2) for deriving a ship allocation plan for transporting a raw material from a loading point to an unloading point by a ship comprises: an acquisition unit (21) that acquires condition information set by a user; a first setting unit (28) that sets, by using the condition information, a first index including a first parameter related to the ship allocation plan as a variable and indicating costs required for transportation; a second setting unit (29) that sets, by using the condition information, a second index including a second parameter related to the ship allocation plan as a variable and indicating a difference between a raw material scheduled to be transported to the unloading point and a raw material required at the unloading point; and a calculation unit (23) that derives said parameters related to the ship allocation plan so that the value of an objective function including the sum of a term pertaining to the first index and a term pertaining to the second index becomes smaller.
G06Q 10/04 - Prévision ou optimisation spécialement adaptées à des fins administratives ou de gestion, p. ex. programmation linéaire ou "problème d’optimisation des stocks"
G06Q 10/08 - Logistique, p. ex. entreposage, chargement ou distributionGestion d’inventaires ou de stocks
G06Q 50/40 - Procédés d’affaires s’appliquant à l’industrie du transport
This electrochemical cell comprises an anode part, a cathode part, and an electrolyte membrane. The anode part comprises a first flow field forming a space through which a first fluid containing water flows so as to come into contact with a first surface of the electrolyte membrane. The cathode part comprises a second flow field forming a space through which a second fluid containing a hydrogen storage material flows so as to come into contact with a second surface of the electrolyte membrane. At least one of the first flow field and the second flow field includes: a first flow path having a structure in which a first outlet end portion is less conducive to fluid flow than a first inlet end portion; and a second flow path having a structure in which a second inlet end portion is less conducive to fluid flow than a second outlet end portion. The at least one flow field has a region in which a portion of the first flow path and a portion of the second flow path are arranged in parallel.
C25B 9/00 - Cellules ou assemblages de cellulesÉléments de structure des cellulesAssemblages d'éléments de structure, p. ex. assemblages d'électrode-diaphragmeCaractéristiques des cellules relatives aux procédés
C25B 9/23 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes comprenant des membranes échangeuses d'ions dans ou sur lesquelles est incrusté du matériau pour électrode
C25B 9/65 - Dispositifs pour l'alimentation en courantConnexions d'électrodesConnexions électriques intercellulaires
This electrochemical cell comprises an anode part, a cathode part, and an electrolyte membrane. The anode part is provided with a first flow field that forms a space in which a first fluid containing water flows so as to come into contact with a first surface of the electrolyte membrane. The cathode part includes a second flow field that forms a space in which a second fluid containing a hydrogenation target substance flows so as to come into contact with a second surface of the electrolyte membrane. The electrochemical cell further comprises an insulating member disposed in at least one flow field among the first flow field and the second flow field.
C25B 9/00 - Cellules ou assemblages de cellulesÉléments de structure des cellulesAssemblages d'éléments de structure, p. ex. assemblages d'électrode-diaphragmeCaractéristiques des cellules relatives aux procédés
C25B 9/23 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes comprenant des membranes échangeuses d'ions dans ou sur lesquelles est incrusté du matériau pour électrode
C25B 9/65 - Dispositifs pour l'alimentation en courantConnexions d'électrodesConnexions électriques intercellulaires
C25B 13/08 - DiaphragmesÉléments d'espacement caractérisés par le matériau à base de matériaux organiques
An electrochemical cell according to the present invention comprises an anode part, a cathode part, and an electrolyte membrane. The anode part has a first flow field that forms a space through which a first fluid including water flows so as to contact a first surface of the electrolyte membrane. The cathode part has a second flow field that forms a space through which a second fluid including a hydrogenated substance flows so as to contact a second surface of the electrolyte membrane. The second flow field comprises a porous layer formed of a conductive material, and the compressive strain of the porous layer in the cathode part is 0.3-0.8.
C25B 9/00 - Cellules ou assemblages de cellulesÉléments de structure des cellulesAssemblages d'éléments de structure, p. ex. assemblages d'électrode-diaphragmeCaractéristiques des cellules relatives aux procédés
C25B 9/23 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes comprenant des membranes échangeuses d'ions dans ou sur lesquelles est incrusté du matériau pour électrode
C25B 15/08 - Alimentation ou vidange des réactifs ou des électrolytesRégénération des électrolytes
A working fluid filled in a refrigerant circulation system comprising a compressor, a condenser, an expansion mechanism, an evaporator, and an accumulator, the working fluid comprising: a refrigerant; and a refrigerating machine oil, wherein the refrigerant comprises a hydrocarbon refrigerant having 2 to 4 carbon atoms, the refrigerating machine oil has a mixed aniline point of 20° C. or higher and 50° C. or lower and a viscosity index of 110 or more, an amount of the refrigerant dissolved in the working fluid is 40% by mass or less under conditions of a temperature of 80° C. and an absolute pressure of 2.8 MPa, and the refrigerating machine oil has a kinematic viscosity at −10° C. of 200 mm2/s or more and 3000 mm2/s or less.
C10M 105/46 - Esters complexes, c.-à-d. composés contenant au moins 3 groupes carboxyle estérifiés et dérivés de la combinaison d'au moins trois types différents des cinq types de composés suivants: composés monohydroxylés, composés polyhydroxylés, acides monocarboxyliques, acides polycarboxyliques et acides hydroxycarboxyliques dérivés uniquement de la combinaison de composés monohydroxylés, de composés dihydroxylés et d'acides dicarboxyliques et ne comportant pas de groupes hydroxyle ou carboxyle libres
C09K 5/04 - Substances qui subissent un changement d'état physique lors de leur utilisation le changement d'état se faisant par passage de l'état liquide à l'état vapeur ou vice versa
C10M 105/40 - Esters contenant des groupes hydroxyle ou carboxyle libres
C10N 30/02 - Point d'écoulementIndice de viscosité
C10N 30/06 - OnctuositéRésistance du filmAnti-usureRésistance aux pressions extrêmes
C10N 40/30 - Lubrifiants pour machines frigorifiques
F25B 1/00 - Machines, installations ou systèmes à compression à cycle irréversible
F25B 43/02 - Dispositions pour la séparation ou la purification des gaz ou des liquidesDispositions pour la vaporisation des résidus de fluides frigorigènes, p. ex. par la chaleur pour la séparation des lubrifiants du frigorigène
A method for producing a hydrocarbon according to the present disclosure includes a step of treating a feedstock using a fluid catalytic cracking unit, the feedstock includes FT synthetic oil, and the feedstock has a % CA of 6 to 23.
C10G 11/18 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures avec catalyseurs solides mobiles préchauffés selon la technique du "lit fluidisé"
34.
REFRIGERATOR OIL AND WORKING FLUID COMPOSITION FOR REFRIGERATOR
C10M 169/04 - Mélanges de matériaux de base et d'additifs
C09K 5/04 - Substances qui subissent un changement d'état physique lors de leur utilisation le changement d'état se faisant par passage de l'état liquide à l'état vapeur ou vice versa
A refrigerating machine oil according to the present invention contains a compound represented by formula (1) as a base oil, the surface tension of the compound represented by formula (1) at 25°C being at least 31 mN/m. (In the formula, R1and R2are each independently a hydrogen atom or an alkyl group, R3 is an ethylene group or a propylene group, and m is an integer that is equal to or greater than 2.)
C10M 137/00 - Compositions lubrifiantes caractérisées en ce que l'additif est un composé organique non macromoléculaire contenant du phosphore
C10N 20/00 - Propriétés physiques particulières des constituants des compositions lubrifiantes
C10N 30/06 - OnctuositéRésistance du filmAnti-usureRésistance aux pressions extrêmes
C10N 40/30 - Lubrifiants pour machines frigorifiques
36.
FOAMING SUPPRESSANT FOR REFRIGERATOR OIL, METHOD FOR SUPPRESSING FOAMING IN REFRIGERATOR OIL, USE FOR SUPPRESSING FOAMING IN REFRIGERATOR OIL, REFRIGERATOR OIL, AND WORKING FLUID COMPOSITION
This foaming suppressant for a refrigerator oil contains a compound represented by a formula (1) [in the formula, R1and R2are each independently a hydrogen atom or an alkyl group, R3 is an ethylene group or a propylene group, and m is an integer of 2 or more]. In the compound represented by formula (1), the hydrogen atom/alkyl group molar ratio is 40/60-60/40 and the ethylene group/propylene group molar ratio is 10/90 or less.
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
A refrigerator comprising a refrigerant circulation system that has a compressor, a condenser, an expansion mechanism, and an evaporator, wherein: the refrigerant circulation system has a member which contains at least one selected from the group consisting of ethylene propylene diene rubbers and hydrogenated nitrile butadiene rubbers; the refrigerant circulation system is filled with a refrigerant containing a hydrocarbon and a refrigerator oil containing a compound represented by formula (1) [in the formula, R1and R2are each independently a hydrogen atom or an alkyl group, R3 is an ethylene group or a propylene group, and m is an integer of not less than 2]; and the molar ratio of ethylene group/propylene group in the compound represented by formula (1) is not less than 25/75.
C09K 5/04 - Substances qui subissent un changement d'état physique lors de leur utilisation le changement d'état se faisant par passage de l'état liquide à l'état vapeur ou vice versa
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
C10N 40/30 - Lubrifiants pour machines frigorifiques
This refrigerator oil contains a compound represented by formula (I) as a base oil. [In the formula, R1and R2are each independently a hydrogen atom or an alkyl group, R3 is an ethylene group or a propylene group, and m is an integer of 2 or greater.] The compound represented by formula (1) has an ethylene group/propylene group molar ratio of 5/95 to 65/35.
Provided is a refrigerator equipped with a refrigerant circulation system having a compressor, a condenser, an expansion mechanism, and an evaporator, wherein the refrigerant circulation system has a member containing at least one selected from the group consisting of ethylene propylene diene rubber and hydrogenated nitrile butadiene rubber, the refrigerant circulation system is filled with a refrigerant containing a hydrocarbon and a refrigerator oil containing a compound represented by formula (1) [in the formula, R1and R2each independently are a hydrogen atom or an alkyl group, R3 is an ethylene group or a propylene group, and m is an integer of 2 or more.], and the molar ratio of ethylene groups/propylene groups in the compound represented by formula (1) is 85/15 or less.
C09K 5/04 - Substances qui subissent un changement d'état physique lors de leur utilisation le changement d'état se faisant par passage de l'état liquide à l'état vapeur ou vice versa
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
C10N 40/30 - Lubrifiants pour machines frigorifiques
40.
MANUFACTURING PLAN GENERATION SYSTEM, MANUFACTURING PLAN GENERATION METHOD, AND MANUFACTURING SYSTEM
A production cost of fuel provided to a vehicle is reduced.
A production cost of fuel provided to a vehicle is reduced.
A production plan generation system 10 generates a production plan for fuel or a vehicle and includes a condition information acquisition unit 11 acquiring condition information including information indicating an amount of fuel suppliable to a vehicle to which a produced fuel can be supplied and a production plan generation unit 12 generating the production plan including a production time of the fuel and an amount of fuel produced on the basis of the condition information acquired by the condition information acquisition unit 11.
A seafarer safety device (500) includes an evaluator (510a) and an inboard outputter (510k). The evaluator (510a) executes an evaluation process of evaluating whether a crew in emergency circumstances, on the basis of the intensities of notification radio waves indicating the existence of the crew on a craft and transmitted from a wearable transmitting device that repetitively transmits the notification radio waves, and on the basis of the strengths of rocking motions of the craft detected by a craft rocking-motion sensor that detects the strengths of rocking motions. The inboard outputter (510k) outputs, to an alarm unit, an emergency evaluation signal indicating a result of evaluation, when the evaluator (510a) evaluates that the crew is in emergency circumstances.
G08B 21/08 - Alarmes pour assurer la sécurité des personnes réagissant à la présence de personnes dans une masse d'eau, p. ex. dans une piscineAlarmes pour assurer la sécurité des personnes réagissant à un état anormal d'une masse d'eau
G08B 25/00 - Systèmes d'alarme dans lesquels l'emplacement du lieu où existe la condition déclenchant l'alarme est signalé à une station centrale, p. ex. systèmes télégraphiques d'incendie ou de police
A refrigerating machine oil that can ensure the residual amount of an anti-wear agent. The refrigerating machine oil comprises an ester of a polyhydric alcohol and a fatty acid having 14 to 20 carbon atoms as a base oil, and an anti-wear agent. The fatty acid having 14 to 20 carbon atoms comprises an unsaturated fatty acid, which includes an unsaturated fatty acid having one carbon-carbon unsaturated bond and an unsaturated fatty acid having two or more carbon-carbon unsaturated bonds. The proportion of the unsaturated fatty acid having two or more carbon-carbon unsaturated bonds is 20% by mole or less based on the total amount of the unsaturated fatty acid.
C09K 5/04 - Substances qui subissent un changement d'état physique lors de leur utilisation le changement d'état se faisant par passage de l'état liquide à l'état vapeur ou vice versa
C10M 169/04 - Mélanges de matériaux de base et d'additifs
C10M 171/00 - Compositions lubrifiantes caractérisées par des critères purement physiques, p. ex. contenant comme matériau de base, épaississant ou additif des ingrédients exclusivement caractérisés par des valeurs numériques particulières de leurs propriétés physiques, c.-à-d. contenant des ingrédients physiquement bien définis mais dont la nature chimique n'est pas précisée ou n'est que très vaguement indiquée
C10N 20/00 - Propriétés physiques particulières des constituants des compositions lubrifiantes
C10N 30/02 - Point d'écoulementIndice de viscosité
C10N 30/06 - OnctuositéRésistance du filmAnti-usureRésistance aux pressions extrêmes
C10N 30/10 - Inhibition de l'oxydation, p. ex. anti-oxydants
C10N 40/30 - Lubrifiants pour machines frigorifiques
43.
ORGANIC HYDRIDE GENERATION SYSTEM, CONTROL DEVICE FOR ORGANIC HYDRIDE GENERATION SYSTEM, AND CONTROL METHOD FOR ORGANIC HYDRIDE GENERATION SYSTEM
A control device includes a controller that controls a first power supplier structured to supply power to an electrolytic bath for generating an organic compound and a second power supplier different from the first power supplier and structured to supply power to the electrolytic bath. The controller controls the second power supplier based on a change in a voltage between a cathode electrode and an anode electrode provided in the electrolytic bath to a specified voltage, a change in a potential of the cathode electrode to a specified potential ECA1, or a change in a potential of the anode electrode to a specified potential EAN1.
A lubricating oil composition for an internal combustion engine includes: (A) a lubricating base oil including at least one mineral oil-based base oil and having a kinematic viscosity at 100° C. of from 2.0 mm2/s or more and 4.3 mm2/s or less, and (B) a calcium borate-containing metallic detergent in an mount of 500 mass ppm or more and less than 1500 mass ppm in terms of calcium, based on a total amount of the composition. The composition has an evaporation loss by NOACK method (250° C., 1 h) of from 10 mass % or more and 40 mass % or less, and the composition has a viscosity index of from 140 or more and 350 or less. The lubricating oil composition is provided, wherein even in the case of using a highly evaporative base oil to make the viscosity low, the friction characteristic of the lubricating oil composition can be kept low.
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
C10N 30/02 - Point d'écoulementIndice de viscosité
C10N 30/04 - Propriétés détergentes ou dispersantes
Provided is a cooling oil composition. The cooling oil composition contains: a base oil containing a compound represented by formula (1); and an antioxidant containing an amine-based antioxidant. [In formula (1), m represents an integer between 2 and 8. R1represents a hydrogen atom or a C1-8 alkyl group. R2represents a C1-6 alkylene group. The plurality of R2moieties that are present may be the same as or different from each other. R3 represents a hydrogen atom or a C1-8 alkyl group.]
C10M 133/12 - Amines, p. ex. polyalkylènepolyaminesAmines quaternaires comportant des groupes amine liés à un atome de carbone d'un cycle aromatique à six chaînons
C10M 135/00 - Compositions lubrifiantes caractérisées en ce que l'additif est un composé organique non macromoléculaire contenant du soufre, du sélénium ou du tellure
C10N 30/10 - Inhibition de l'oxydation, p. ex. anti-oxydants
C10N 40/00 - Utilisation ou application particulière de la composition lubrifiante
46.
MANAGEMENT DEVICE, ENERGY SUPPLY SYSTEM, AND MANAGEMENT METHOD
This management device comprises a plan creation unit that creates a supply plan for supplying hydrogen carriers to two or more energy generation devices whose throughputs for generating hydrogen energy by using hydrogen carriers as a starting material differ.
The present invention provides a method for producing a nitrogenated heterocyclic ring-containing compound using a nickel-based catalyst, the method making it possible to efficiently synthesize the nitrogenated heterocyclic ring-containing compound in a short time. More specifically, provided is a method for producing a nitrogenated heterocyclic ring-containing compound represented by formula (1), the method including a reaction step in which a first starting compound represented by formula (10) is reacted with a second starting compound represented by formula (11) in the presence of an aprotic polar solvent having a boiling point of 90°C or higher and a nickel-based catalyst represented by formula (12) to synthesize the nitrogenated heterocyclic ring-containing compound represented by formula (1).
MITSUBISHI HEAVY INDUSTRIES THERMAL SYSTEMS, LTD. (Japon)
ENEOS CORPORATION (Japon)
Inventeur(s)
Yuki, Hiroyuki
Horaguchi, Norihisa
Wajima, Kazuki
Suemitsu, Ryosuke
Shono, Yohei
Abrégé
Provided are a heat source machine and an operation method of the same that employ predetermined solutions by using a predetermined refrigerating machine oil that can suppress deterioration of the refrigerating machine oil and viscosity reduction when a refrigerant is dissolved in the refrigerating machine oil. In the heat source machine (10) of the present disclosure, a compressor (11), a condenser (12), an expansion valve (13), and an evaporator (14) are connected to each other via main pipes (L1 to L8) to form a refrigerant circulation circuit configured to circulate a refrigerant, and the refrigerant circulation circuit is filled with HFO-1336mzz (Z) as a refrigerant. The heat source machine includes a refrigerating machine oil supply unit (15) configured to supply a refrigerating machine oil to the compressor (11), the refrigerating machine oil supply unit (15) includes a storage unit (15a) storing the refrigerating machine oil, the refrigerating machine oil includes an ester-based base oil having a dynamic viscosity of 100 mm2/s to 180 mm2/s at 40° C. and an epoxy-based acid scavenger at a mass of 0.1% by mass to 6% by mass with respect to a total mass of the refrigerating machine oil, and the machine design temperature is 130° C. or higher and 225° C. or lower.
C10M 169/04 - Mélanges de matériaux de base et d'additifs
C09K 5/04 - Substances qui subissent un changement d'état physique lors de leur utilisation le changement d'état se faisant par passage de l'état liquide à l'état vapeur ou vice versa
A method for producing 1,3-butanediol, the method comprising: a step for bringing a raw material liquid containing acetaldehyde into contact with a solid base catalyst and a hydrogenation catalyst to obtain a reaction liquid containing 1,3-butanediol, wherein the solid base catalyst includes at least one among metal elements having an atomic number of 12-20, and the hydrogenation catalyst includes Ni.
C07C 29/141 - Préparation de composés comportant des groupes hydroxyle ou O-métal liés à un atome de carbone ne faisant pas partie d'un cycle aromatique à six chaînons par réduction d'un groupe fonctionnel contenant de l'oxygène de groupes contenant C=O, p. ex. —COOH d'un groupe —CHO avec de l'hydrogène ou des gaz contenant de l'hydrogène
A water electrolysis cell has: an oxygen generating electrode; a hydrogen generating electrode; and a membrane, and electrolyzes water to generate oxygen on the oxygen generating electrode and generate hydrogen on the hydrogen generating electrode. A control device includes: a potential-maintaining mode where the water electrolysis cell is supplied with electric current; and a complete stop mode where the water electrolysis cell is shut out from electric current supply, each of the modes is optionally implemented during an operation stop, wherein which of the modes is implemented is determined based on a duration time of the operation stop, a first deterioration rate of the water electrolysis cell when the complete stop mode is implemented, and a second deterioration rate of the water electrolysis cell when the potential-maintaining mode is implemented.
An organic hydride production apparatus includes an electrolysis tank having an anode electrode for oxidizing water in an anolyte La to generate protons, a cathode electrode for hydrating a substance α to be hydrated in the cathode liquid Lc with protons to generate an organic hydride β, and a diaphragm positioned between the anode electrode and the cathode electrode, the diaphragm moving protons together with produced water W from the anode electrode side to the cathode electrode side; an anolyte supply part for supplying the anolyte La to the anode electrode; a water separation unit for separating the produced water W from a catholyte Lc sent from the cathode electrode; and a water return unit for sending the produced water W separated by the water separation unit to the anolyte supply part.
C25B 9/23 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes comprenant des membranes échangeuses d'ions dans ou sur lesquelles est incrusté du matériau pour électrode
An organic hydride production apparatus includes: a membrane electrode assembly in which an anode electrode and a cathode electrode are laminated with a membrane interposed therebetween; a supply flow path which extends in a vertical direction, and in which a catholyte flows from a lower side to an upper side; and a collection flow path which extends in the vertical direction, and in which the catholyte flows from a lower side to an upper side. A flow resistance R1 of the catholyte flowing through the cathode electrode, a flow resistance R2 of the catholyte flowing through the collection flow path, and a flow resistance R3 of the catholyte flowing through the supply flow path satisfy a relation of R1>R2>R3.
C25B 9/23 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes comprenant des membranes échangeuses d'ions dans ou sur lesquelles est incrusté du matériau pour électrode
An organic hydride production apparatus includes: a membrane electrode assembly in which an anode electrode and a cathode electrode are laminated with a membrane interposed therebetween; a cathode flow path that overlaps the membrane electrode assembly when viewed from a lamination direction of the cathode electrode, the membrane, and the anode electrode, and feeds and discharges a catholyte to and from the cathode electrode; and a support member that supports the membrane electrode assembly so as to suppress fitting of the membrane electrode assembly into the cathode flow path.
C25B 9/23 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes comprenant des membranes échangeuses d'ions dans ou sur lesquelles est incrusté du matériau pour électrode
C10M 169/06 - Mélanges d'épaississants et d'additifs
C10M 107/02 - Polymères d'hydrocarburesPolymères d'hydrocarbures modifiés par oxydation
C10M 115/08 - Compositions lubrifiantes caractérisées en ce que l'épaississant est un composé organique non macromoléculaire, autre qu'un acide carboxylique ou ses sels contenant de l'azote
C10M 133/06 - Amines, p. ex. polyalkylènepolyaminesAmines quaternaires comportant des groupes amine liés à des atomes de carbone acycliques ou cycloaliphatiques
C10N 30/06 - OnctuositéRésistance du filmAnti-usureRésistance aux pressions extrêmes
C10N 40/04 - Bains d'huileBoîtes de vitessesTransmissions automatiquesMécanismes de traction
C10N 50/10 - Forme sous laquelle est appliqué le lubrifiant au matériau à lubrifier semi-solideForme sous laquelle est appliqué le lubrifiant au matériau à lubrifier huileuse
55.
METHOD FOR CONTROLLING HYDROGEN GENERATION SYSTEM, AND HYDROGEN GENERATION SYSTEM
A method for controlling a hydrogen generation system includes controlling the potentials of an electrode for oxygen generation and an electrode for hydrogen generation included in an electrolyzer so that the potential change is smaller in the electrode for oxygen generation or the electrode for hydrogen generation having a larger deterioration rate than in the electrode having a smaller deterioration rate.
A method for controlling an organic hydride generation system includes controlling potentials in an anode electrode and a cathode electrode such that a potential change in an electrode having a higher deterioration rate among the anode electrode and the cathode electrode included in an electrolytic bath is smaller than a potential change in an electrode having a lower deterioration rate.
A fuel production apparatus includes: a synthesis gas production unit that produces a synthesis gas containing carbon monoxide and hydrogen by using carbon dioxide and hydrogen; a hydrocarbon production unit that produces a hydrocarbon by using the synthesis gas; a first distillation separator that separates at least a first fraction and a second fraction lighter than the first fraction from an effluent from the hydrocarbon production unit; a hydrocracking unit that performs a hydrocracking treatment on a portion of the first fraction; and a catalytic cracking unit that performs a catalytic cracking treatment on another portion of the first fraction.
C10G 69/04 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage catalytique en l'absence d'hydrogène
B01J 8/24 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé"
C01B 3/02 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène
58.
LUBRICANT ADDITIVE, LUBRICANT COMPOSITION, AND WORKING FLUID COMPOSITION
An additive for a lubricating oil containing a phosphorus compound P represented by the following formula (1):
An additive for a lubricating oil containing a phosphorus compound P represented by the following formula (1):
An additive for a lubricating oil containing a phosphorus compound P represented by the following formula (1):
wherein R1 and R2 each independently represent an alkyl group having 1 to 3 carbon atoms, and n represents an integer of 0 to 3, wherein the phosphorus compound P contains a phosphorus compound PO wherein n is 0, a phosphorus compound P1 wherein n is 1, a phosphorus compound P2 where n is 2, and a phosphorus compound P3 wherein n is 3, and a total proportion of the phosphorus compound PO and the phosphorus 10 compound P1 in the phosphorus compound P is 60% by mole or more.
C10M 131/02 - Compositions lubrifiantes caractérisées en ce que l'additif est un composé organique non macromoléculaire contenant des halogènes contenant uniquement du carbone, de l'hydrogène et des halogènes
C10M 169/04 - Mélanges de matériaux de base et d'additifs
C10N 40/30 - Lubrifiants pour machines frigorifiques
59.
HYDROGEN GAS SUPPLY APPARATUS AND HYDROGEN GAS SUPPLY METHOD
A control apparatus for controlling a gas purification apparatus includes a circuit configured to control to depressurize a pressure inside a compressor configured to compress a gas. The gas purification apparatus includes the compressor, a first adsorption part configured to include a first adsorbent which adsorbs impurities mixed in the gas, a second adsorption part configured to include a second adsorbent which adsorbs the impurities, and a valve provided on a pipe connecting the compressor, the first adsorption part, and the second adsorption part. The circuit is further configured to control the valve so that the second adsorbent adsorbs the impurities desorbed from the first adsorbent in a case that a pressure inside the compressor is depressurized, to regenerate the first adsorption part.
B01D 53/04 - Séparation de gaz ou de vapeursRécupération de vapeurs de solvants volatils dans les gazÉpuration chimique ou biologique des gaz résiduaires, p. ex. gaz d'échappement des moteurs à combustion, fumées, vapeurs, gaz de combustion ou aérosols par adsorption, p. ex. chromatographie préparatoire en phase gazeuse avec adsorbants fixes
B01J 20/28 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation caractérisées par leur forme ou leurs propriétés physiques
C01B 3/56 - Séparation de l'hydrogène ou des gaz contenant de l'hydrogène à partir de mélanges gazeux, p. ex. purification par contact avec des solidesRégénération des solides usés
F17C 5/06 - Procédés ou appareils pour remplir des récipients sous pression de gaz liquéfiés, solidifiés ou comprimés pour le remplissage avec des gaz comprimés
60.
GEAR-TYPE TRANSMISSION FOR ELECTROMOTIVE MOBILITY, LUBRICATING OIL COMPOSITION FOR GEAR-TYPE TRANSMISSION FOR ELECTROMOTIVE MOBILITY, AND METHOD FOR LUBRICATING GEAR-TYPE TRANSMISSION FOR ELECTROMOTIVE MOBILITY USING SAME
This gear-type transmission for electromotive mobility comprises: a lubricating oil composition for lubricating sliding portions; and a joining part in which a form-in-place gasket containing silicone is used in at least a portion thereof as a sealing member for the lubricating oil composition. The lubricating oil composition contains specific components (A)-(F) and satisfies all specific conditions (i)-(vi).
C10M 137/02 - Compositions lubrifiantes caractérisées en ce que l'additif est un composé organique non macromoléculaire contenant du phosphore ne comportant pas de liaison carbone-phosphore
C10M 139/00 - Compositions lubrifiantes caractérisées en ce que l'additif est un composé organique non macromoléculaire contenant des atomes d'éléments non prévus dans l'un des groupes
C10M 159/22 - Mélanges réactionnels comportant un excès de base neutralisante, p. ex. produits appelés superbasiques ou hautement basiques contenant des radicaux phénol
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
C10N 30/02 - Point d'écoulementIndice de viscosité
C10N 30/04 - Propriétés détergentes ou dispersantes
C10N 30/06 - OnctuositéRésistance du filmAnti-usureRésistance aux pressions extrêmes
A refrigerating machine oil containing: a lubricating base oil; and a polymer additive, wherein a carbon residue of 10% residual oil is 0.05% by mass or more.
Provided is a method for producing chemical products, including: a pyrolysis step of obtaining a first gas fraction, a pyrolysis oil, and a residual fraction by pyrolysis of a crushed material of a waste material including waste tires; a hydrogenolysis step of obtaining a second gas fraction, a light fraction with a boiling point of 350° C. or lower, and a heavy fraction with a boiling point higher than 350° C. by hydrogenolysis of a raw material oil containing at least a part of the pyrolysis oil; and a steam-cracking step of obtaining a chemical product by steam cracking of a steam-cracking raw material oil containing at least a part of the light fraction.
C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène
C10B 53/07 - Distillation destructive spécialement conçue pour des matières premières solides particulières ou sous forme spéciale de matières polymères synthétiques, p. ex. pneumatiques
63.
INFORMATION PROCESSING APPARATUS, HYDROGEN PRODUCTION SYSTEM, POWER SUPPLY SYSTEM, OPERATION PLAN CREATION METHOD, AND COMPUTER PROGRAM
NATIONAL INSTITUTE OF ADVANCED INDUSTRIAL SCIENCE AND TECHNOLOGY (Japon)
Inventeur(s)
Harada, Kosuke
Takami, Hirofumi
Okumo, Ichiro
Uehara, Kazuki
Kojima, Hirokazu
Kikusato, Hiroshi
Oozeki, Takashi
Furutani, Hirohide
Abrégé
A hydrogen production system includes a hydrogen production facility and a management server. The management server includes an operation plan creation unit and an operation plan output unit. The operation plan creation unit creates an operation plan for the hydrogen production facility. The operation plan output unit outputs data including the operation plan created by the operation plan creation unit. The operation plan creation unit creates an operation plan for the hydrogen production facility based on an amount of energy consumed by the hydrogen production facility and a degradation loss of the hydrogen production facility.
This prediction device comprises: a verification prediction unit that predicts electricity prices in a predetermined verification period, on the basis of each of a plurality of trained prediction models; a model selection unit that selects a prediction model having high accuracy for predicting electricity prices among the prediction models; and a target prediction unit that predicts electricity prices in a prediction target period, on the basis of the selected prediction model.
H02J 3/00 - Circuits pour réseaux principaux ou de distribution, à courant alternatif
65.
COMPLEX ESTER FOR REFRIGERATING MACHINE OILS AND METHOD FOR PRODUCING SAME, REFRIGERATING MACHINE OIL, WORKING FLUID COMPOSITION, AND METHOD FOR IMPROVING STABILITY OF COMPLEX ESTER
Provided is a complex ester for refrigerating machine oils, which is a complex ester of neopentyl glycol, a divalent aliphatic alcohol other than neopentyl glycol, a divalent aliphatic carboxylic acid, and a monovalent aliphatic alcohol. The complex ester has an ester bond in which a hydroxy group of neopentyl glycol is esterified and an unreacted hydroxy group in which a hydroxy group is not esterified, and the proportion of the unreacted hydroxy group in the total of the ester bond and the unreacted hydroxy group is 6% by mole or less.
C10M 105/42 - Esters complexes, c.-à-d. composés contenant au moins 3 groupes carboxyle estérifiés et dérivés de la combinaison d'au moins trois types différents des cinq types de composés suivants: composés monohydroxylés, composés polyhydroxylés, acides monocarboxyliques, acides polycarboxyliques et acides hydroxycarboxyliques
C07C 67/08 - Préparation d'esters d'acides carboxyliques par réaction d'acides carboxyliques ou d'anhydrides symétriques avec le groupe hydroxyle ou O-métal de composés organiques
A chemical looping system includes repeating: a generation process of reacting a reduced form of a material for the chemical looping system, which contains a first element selected from the group consisting of Co and Ni and a second element selected from the group consisting of In and Ga, with carbon dioxide so as to generate an oxidized form of the material for the chemical looping system, in which the second element is oxidized by the reaction, and carbon monoxide, and a reduction treatment of reacting the oxidized form with a reducing agent and thus reducing the second element having been oxidized in the generation process so as to thereby convert the oxidized form back into the reduced form.
B01J 8/26 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées selon la technique du "lit fluidisé" comportant au moins deux lits fluidisés, p. ex. installations de réaction et de régénération
B01J 8/18 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées
Provided is a gas compressor oil composition comprising a base oil (A), wherein the base oil (A) contains a hydrocarbon base oil (A1) which includes biomass-derived carbon, and the biomass-derived carbon content as measured in accordance with ASTM D6866 is not less than 20 mass% with respect to the total carbon contained in the gas compressor oil composition.
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
Provided is a gas compressor oil composition containing a base oil (A) and a degradation product dissolving agent (B), wherein the base oil (A) contains a hydrocarbon base oil (A1) having biomass-derived carbon, and the content of biomass-derived carbon as measured by ASTM D6866 is 20 mass% or more in terms of the total carbon in the gas compressor oil composition.
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
C10N 30/06 - OnctuositéRésistance du filmAnti-usureRésistance aux pressions extrêmes
Provided is a method for producing chemical products and carbides, including: a pyrolysis step of obtaining a first gas fraction, a pyrolysis oil, and a residual fraction by pyrolysis of a crushed material of waste tires; a carbide recovery step of recovering a carbide from the residual fraction; a hydrogenolysis step of obtaining a second gas fraction, a light fraction, and a heavy fraction by hydrogenolysis of a raw material oil containing at least a part of the pyrolysis oil; and a steam-cracking step of obtaining a chemical product and a raw material for producing a carbide by steam cracking of a steam-cracking raw material oil containing at least a part of the light fraction.
C10B 53/07 - Distillation destructive spécialement conçue pour des matières premières solides particulières ou sous forme spéciale de matières polymères synthétiques, p. ex. pneumatiques
C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène
This oil/seal lubrication system comprises a seal member, and a slide member that moves relative to the seal member and comes into contact with the seal member via lubricating oil. The seal member contains an inorganic filler, and at least one of the seal member and the lubricating oil contains an ashless friction modifier.
F16J 15/10 - Joints d'étanchéité entre surfaces immobiles entre elles avec garniture solide comprimée entre les surfaces à joindre par garniture non métallique
C10M 169/04 - Mélanges de matériaux de base et d'additifs
This lubricating oil composition comprises a base oil and at least one friction modifier selected from the group consisting of a fatty acid ester-based compound, an amine-based compound, an amide-based compound, an imide-based compound, a phosphorus-based compound, a sulfur-based compound, and a phosphorus-sulfur-based compound, and is used together with an oil seal including an inorganic filler.
A control circuit controls fillings speeds of hydrogen gas filling a fuel tank. The control circuit a) receives values of a characteristic of the tank during a process of filling the tank with the hydrogen gas, b) calculates at different times during the filling process the differences between a preset threshold of the characteristic of the tank and the values of the characteristic of the tank received at the different times during the filling process, c) calculates plural filling speeds of the hydrogen gas filling the tank during the filling process, each of the filling speeds depending on one of the plurality of differences between the preset threshold and the values of the characteristic of the tank received at the different times during the filling process, and d) controls an operation of a dispenser for filling the tank with the hydrogen gas at the calculated filling speeds.
F17C 5/00 - Procédés ou appareils pour remplir des récipients sous pression de gaz liquéfiés, solidifiés ou comprimés
B67D 7/04 - Appareils ou dispositifs pour transférer des liquides à partir de récipients ou de réservoirs de stockage en vrac vers des véhicules ou des récipients portables, p. ex. pour la vente au détail pour transférer des carburants, des lubrifiants ou leurs mélanges
B67D 7/32 - Aménagements des dispositifs de sécurité ou d'alarmeMoyens pour empêcher un débit non autorisé du liquide
F17C 5/06 - Procédés ou appareils pour remplir des récipients sous pression de gaz liquéfiés, solidifiés ou comprimés pour le remplissage avec des gaz comprimés
F17C 13/02 - Adaptations spéciales des dispositifs indicateurs, de mesure ou de contrôle
G01K 3/08 - Thermomètres donnant une indication autre que la valeur instantanée de la température fournissant des différences de valeursThermomètres donnant une indication autre que la valeur instantanée de la température fournissant des valeurs différenciées
G01L 19/00 - Détails ou accessoires des appareils pour la mesure de la pression permanente ou quasi permanente d'un milieu fluent dans la mesure où ces détails ou accessoires ne sont pas particuliers à des types particuliers de manomètres
74.
METHOD FOR DIAGNOSING FAILURE IN PRESSURE GAUGE OF HYDROGEN FILLING SYSTEM, AND METHOD FOR CALIBRATING PRESSURE GAUGE OF HYDROGEN FILLING SYSTEM
According to one aspect of the present invention, a method for diagnosing failure in a pressure gauge of a hydrogen filling system includes filling a fuel cell vehicle powered by hydrogen fuel with the hydrogen fuel from an accumulator, in which the hydrogen fuel is accumulated, via a dispenser; and acquiring pressure values measured by a plurality of pressure gauges disposed at different positions in a flow passage of the hydrogen fuel between the accumulator and an outlet of the dispenser at timing when a flow rate of the hydrogen fuel to be filled at a stage close to an end of the filling becomes a threshold value or less, determining whether or not a deviation between the pressure values is within a threshold value on the basis of acquired pressure values, and outputting a determination result.
F17C 5/06 - Procédés ou appareils pour remplir des récipients sous pression de gaz liquéfiés, solidifiés ou comprimés pour le remplissage avec des gaz comprimés
F17C 13/02 - Adaptations spéciales des dispositifs indicateurs, de mesure ou de contrôle
H01M 8/04082 - Dispositions pour la commande des paramètres des réactifs, p. ex. de la pression ou de la concentration
A diagnosis system (100) according to the present disclosure is provided with: a storage unit (40) that stores a detection result of a sensor (11) indicating a deterioration state of oil; and a control unit (30) that diagnoses a change time of the oil on the basis of the detection result stored in the storage unit (40) and notifies a notification destination associated with the sensor (11) of change information indicating the diagnosed change time.
G01M 99/00 - Matière non prévue dans les autres groupes de la présente sous-classe
F16N 29/00 - Dispositifs particuliers dans les installations ou les systèmes de lubrification indiquant ou détectant des conditions indésirablesUtilisation des dispositifs sensibles à ces conditions dans les installations ou les systèmes de lubrification
G01N 21/27 - CouleurPropriétés spectrales, c.-à-d. comparaison de l'effet du matériau sur la lumière pour plusieurs longueurs d'ondes ou plusieurs bandes de longueurs d'ondes différentes en utilisant la détection photo-électrique
A measuring device (1) according to the present disclosure is provided with: a level gauge (12) that is provided outside a tank (11) and indicates the amount of oil inside the tank (11); and a color sensor (21) that detects the color of oil inside the level gauge (12).
G01M 99/00 - Matière non prévue dans les autres groupes de la présente sous-classe
G01N 21/27 - CouleurPropriétés spectrales, c.-à-d. comparaison de l'effet du matériau sur la lumière pour plusieurs longueurs d'ondes ou plusieurs bandes de longueurs d'ondes différentes en utilisant la détection photo-électrique
77.
CHEMICAL PRODUCT PRODUCTION METHOD AND METHOD FOR MANAGING SAME
[Problem] To provide a method that, by improving each step in a series of processes, can efficiently produce chemical products from waste tire-containing waste materials. [Solution] The chemical product production method comprises: a pyrolysis step for obtaining a first gas fraction, a pyrolysis oil, and a residue by pyrolyzing a pulverized material from a waste tire-containing waste material; a low-temperature hydrogenation step for obtaining a low-temperature hydrogenated oil by subjecting a starting oil containing at least a portion of the pyrolysis oil to a low-temperature hydrogenation treatment at 180°C to 350°C; a hydrocracking step for subjecting a starting oil containing at least a portion of the low-temperature hydrogenated oil to a hydrocracking treatment at a temperature higher than that of the low-temperature hydrogenation treatment, to obtain a second gas fraction, a light fraction having a boiling point of not more than 350°C, and a heavy fraction having a boiling point above 350°C; and a steam cracking step for subjecting a steam cracking starting oil containing at least a portion of the light fraction to a steam cracking treatment to obtain a chemical product, wherein the amount of the pyrolysis oil in the pyrolysis step is at least 40 mass% with reference to the total amount of the first gas fraction, pyrolysis oil, and residue.
C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène
C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds
C10G 45/32 - Hydrogénation sélective des composés dioléfiniques ou acétyléniques
C10G 47/00 - Craquage des huiles d'hydrocarbures, en présence d'hydrogène ou de composés donneurs d'hydrogène, pour obtenir des fractions à point d'ébullition inférieur
78.
METHOD FOR PRODUCING CHEMICAL PRODUCT AND METHOD FOR MANAGING SAME
[Problem] To provide a method for efficiently producing a chemical product from a waste material containing waste tires by improving each step in a series of processes to realize long-term operation of the processes. [Solution] This method for producing a chemical product involves a pyrolysis step for obtaining, through pyrolysis of a crushed product of a waste material including waste tires, a first gas component, a pyrolysis oil, and a residual component, a low-temperature hydrogenation step for subjecting a raw material oil containing at least part of the pyrolysis oil to a low-temperature hydrogenation treatment at a temperature of 180°C-350°C to obtain a low-temperature hydrogenated oil, a high-temperature hydrogenation step for subjecting a raw material oil containing at least part of the low-temperature hydrogenated oil to a hydrogenation treatment at a temperature higher than that of the low-temperature hydrogenation treatment to obtain a second gas component and a high-temperature hydrogenated oil, a separation step for separating a naphtha fraction from other fractions through atmospheric distillation of an atmospheric distillation raw material oil containing crude oil and at least part of the high-temperature hydrogenated oil, and a steam cracking step for subjecting a steam cracking raw material oil containing at least part of the naphtha fraction and/or other fractions to a steam cracking treatment to obtain a chemical product, wherein the amount of the pyrolysis oil with respect to the total amount of the first gas component, the pyrolysis oil, and the residual component in the pyrolysis step is 40% by mass or more.
C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène
C08J 11/12 - Récupération ou traitement des résidus des polymères par coupure des chaînes moléculaires des polymères ou rupture des liaisons de réticulation par voie chimique, p. ex. dévulcanisation uniquement par traitement à la chaleur sèche
C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds
C10G 45/06 - Raffinage des huiles d'hydrocarbures au moyen d'hydrogène ou de composés donneurs d'hydrogène pour éliminer des hétéro-atomes sans modifier le squelette de l'hydrocarbure mis en œuvre et sans craquage en hydrocarbures à point d'ébullition inférieurHydrofinissage caractérisé par le catalyseur utilisé contenant du nickel ou du cobalt, ou leurs composés
C10G 45/32 - Hydrogénation sélective des composés dioléfiniques ou acétyléniques
79.
METHOD FOR PRODUCING CHEMICAL PRODUCT AND CARBIDE, AND METHOD FOR MANAGING CHEMICAL PRODUCT
[Problem] To provide a method for efficiently producing a chemical product from waste tires by improving steps in a series of processes and also efficiently obtaining a carbide. [Solution] Provided is a method for producing a chemical product and a carbide, the method comprising: a thermal decomposition step for obtaining a first gas, a thermal decomposition oil and a residue through thermal decomposition of fragmented waste tires; a carbide recovery step for recovering a carbide from the residue; a low temperature hydrogenation step for subjecting a raw material oil containing at least a portion of the thermal decomposition oil to a low temperature hydrogenation treatment at a temperature of 180-350ºC to obtain a low temperature hydrogenated oil; a hydrocracking step for subjecting a raw material oil that contains at least a portion of the low temperature hydrogenated oil to a hydrocracking treatment at a temperature higher than that in the low temperature hydrogenation treatment so as to obtain a second gas, a light fraction having a boiling point of 350°C or lower and a heavy fraction having a boiling point of higher than 350°C; and a steam cracking step for steam cracking a steam cracking raw material oil that contains at least a portion of the light fraction so as to obtain a chemical product and a raw material for carbide production, which comprises a heavy fraction having a 10% distillation temperature of 190°C or higher. The thermal decomposition temperature in the thermal decomposition is 350-750ºC.
C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène
C10B 53/07 - Distillation destructive spécialement conçue pour des matières premières solides particulières ou sous forme spéciale de matières polymères synthétiques, p. ex. pneumatiques
C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds
C10G 45/32 - Hydrogénation sélective des composés dioléfiniques ou acétyléniques
C10G 47/00 - Craquage des huiles d'hydrocarbures, en présence d'hydrogène ou de composés donneurs d'hydrogène, pour obtenir des fractions à point d'ébullition inférieur
80.
METHOD FOR PRODUCING CHEMICAL PRODUCT AND METHOD FOR MANAGING SAME
[Problem] To provide a method for efficiently producing a chemical product from a waste material including waste tires by improving each step in a series of processes to realize long-term operation of the processes. [Solution] This method for producing a chemical product involves a pyrolysis step for obtaining a first gas component, a pyrolysis oil, and a residual component through pyrolysis of a pulverized product of a waste material including waste tires, a low-temperature hydrogenation step for subjecting a raw material oil containing at least part of the pyrolysis oil to a low-temperature hydrogenation treatment at 180°C-350°C to obtain a low-temperature hydrogenated oil, a separation step for subjecting, to atmospheric distillation, a raw material oil for atmospheric distillation containing crude oil and at least part of the low-temperature hydrogenated oil to separate a naphtha fraction from other fractions, and a steam cracking step for subjecting, to steam cracking, a steam cracking raw material oil containing at least part of the naphtha fraction to obtain a chemical product, wherein the amount of the pyrolysis oil with respect to the total amount of the first gas component, the pyrolysis oil, and the residual component is 40% by mass or more in the pyrolysis step.
C10G 69/06 - Traitement des huiles d'hydrocarbures par au moins un procédé d'hydrotraitement et au moins un autre procédé de conversion uniquement par plusieurs étapes en série comprenant au moins une étape de craquage thermique en l'absence d'hydrogène
C08J 11/12 - Récupération ou traitement des résidus des polymères par coupure des chaînes moléculaires des polymères ou rupture des liaisons de réticulation par voie chimique, p. ex. dévulcanisation uniquement par traitement à la chaleur sèche
C10G 1/10 - Production de mélanges liquides d'hydrocarbures à partir de schiste bitumineux, de sable pétrolifère ou de matières carbonées solides non fusibles ou similaires, p. ex. bois, charbon à partir de caoutchouc ou de déchets de caoutchouc
C10G 9/36 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures par contact direct avec des fluides inertes préchauffés, p. ex. avec des métaux ou sels fondus avec des gaz ou vapeurs chauds
C10G 45/32 - Hydrogénation sélective des composés dioléfiniques ou acétyléniques
81.
METHOD FOR PRODUCING 2,5-DIMETHYL-2,4-HEXADIENE AND METHOD FOR PRODUCING P-XYLENE
This method for producing 2,5-dimethyl-2,4-hexadiene comprises a condensation reaction step for reacting isobutyraldehyde and at least one type of first feedstock selected from the group consisting of isobutene and tert-butyl alcohol in the presence of a catalyst so as to obtain 2,5-dimethyl-2,4-hexadiene, wherein the catalyst is a catalyst obtained by acid-treating a catalyst precursor containing niobium oxide.
C07C 2/86 - Préparation d'hydrocarbures à partir d'hydrocarbures contenant un plus petit nombre d'atomes de carbone par condensation d'un hydrocarbure et d'un non-hydrocarbure
B01J 27/195 - PhosphoreSes composés avec de l'arsenic, de l'antimoine, du bismuth, du vanadium, du niobium, du tantale, du polonium, du chrome, du molybdène, du tungstène, du manganèse, du technétium ou du rhénium avec du vanadium, du niobium ou du tantale
This fuel gas filling device (14) comprises: a filling unit (48) for filling a gas tank (50) of a moving body (16) with a fuel gas; a tank information acquisition unit (140) for acquiring tank information pertaining to the remaining amount of gas in the gas tank before filling the gas tank with the fuel gas by the filling unit is started; a temperature adjustment unit (30) for adjusting the gas temperature (Td) of the fuel gas to fill the gas tank so as to approach an adjustment target temperature (Tc); and a determination unit (152) for determining the adjustment target temperature in accordance with the tank information acquired by the tank information acquisition unit.
F17C 5/06 - Procédés ou appareils pour remplir des récipients sous pression de gaz liquéfiés, solidifiés ou comprimés pour le remplissage avec des gaz comprimés
F17C 13/00 - Détails des récipients ou bien du remplissage ou du vidage des récipients
B60S 5/02 - Alimentation des véhicules en combustibleDisposition générale des installations dans les stations d'approvisionnement
83.
PRODUCTION METHOD FOR CYCLOPENTANONE AND PURIFIED CYCLOPENTANONE
A production method for cyclopentanone according to the present invention includes a transfer hydrogenation step for passing a first fluid that contains furfuryl alcohol, water, and hydrogen through a solid-bed flow reactor packed with a hydrogenation catalyst to obtain a reaction product that includes cyclopentanone and water, an extraction step for extracting the cyclopentanone from the reaction product by means of an extraction solvent to obtain an oil phase that contains the cyclopentanone, and a recovery step for recovering the cyclopentanone from the oil phase.
C07C 45/59 - Préparation de composés comportant des groupes C=O liés uniquement à des atomes de carbone ou d'hydrogènePréparation des chélates de ces composés à partir de composés hétérocycliques avec l'oxygène comme unique hétéro-atome dans des cycles à cinq chaînons
020120020120120 is 0.8-1.3. The volume of pores having a pore diameter of 20-600 Å among the pores in the pseudoboehmite is 0.80-1.20 ml/g. The volume of the pores is measured by the nitrogen adsorption method. The pH that indicates the isoelectric point of the pseudoboehmite in water is 8.8 or more.
C01F 7/141 - Oxyde ou hydroxyde d'aluminium obtenus à partir d'aluminates de métaux alcalins à partir de solutions aqueuses d'aluminate par neutralisation avec un agent acide
B01J 35/60 - Catalyseurs caractérisés par leur forme ou leurs propriétés physiques, en général caractérisés par leurs propriétés de surface ou leur porosité
B01J 37/00 - Procédés de préparation des catalyseurs, en généralProcédés d'activation des catalyseurs, en général
C01F 7/34 - Préparation de l'hydroxyde d'aluminium par précipitation à partir de solutions contenant des sels d'aluminium
[Problem] To provide a method capable of producing paraxylene useful as a basic raw material by using a renewable raw material. [Solution] This method produces paraxylene using a naphtha raw material including renewable naphtha and using at least one renewable raw material of benzene and xylene, the method comprising: a step (A-1) for thermally decomposing the renewable raw material in the presence of water vapor to produce and separate a xylene mixture; and a step (A-2) for separating paraxylene by subjecting the xylene mixture to adsorption separation or crystallization separation.
C07C 7/12 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par adsorption, c.-à-d. purification ou séparation d'hydrocarbures à l'aide de solides, p. ex. à l'aide d'échangeurs d'ions
C07C 5/27 - Réarrangement des atomes de carbone dans le squelette hydrocarboné
C07C 7/04 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par distillation
C07C 7/10 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par extraction, c.-à-d. purification ou séparation d'hydrocarbures liquides à l'aide de liquides
C07C 7/14 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par cristallisationPurification ou séparation des cristaux
C07C 51/265 - Préparation d'acides carboxyliques, de leurs sels, halogénures ou anhydrides par oxydation avec l'oxygène moléculaire de composés contenant des cycles aromatiques à six chaînons sans ouverture du cycle comportant des chaînes latérales alkylées qui sont oxydées en groupes carboxyle
[Problem] Provided is a method capable of producing a monocyclic aromatic hydrocarbon, such as benzene or xylene, which is effective as a basic raw material, by using a naphtha raw material including renewable naphtha. [Solution] This method for producing at least one monocyclic aromatic hydrocarbon among benzene and xylene by using a naphtha raw material including renewable naphtha comprises: a step (A-1) for fractionally distilling the naphtha raw material to be separated into heavy naphtha and light naphtha; and a step (A-2) for generating and separating at least one monocyclic aromatic hydrocarbon among benzene and xylene by a cyclization dehydrogenation reaction of paraffin and/or a dehydrogenation reaction of naphthene, contained in the heavy naphtha obtained in the step (A-1).
C07C 5/27 - Réarrangement des atomes de carbone dans le squelette hydrocarboné
C07C 7/12 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par adsorption, c.-à-d. purification ou séparation d'hydrocarbures à l'aide de solides, p. ex. à l'aide d'échangeurs d'ions
C07C 7/14 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par cristallisationPurification ou séparation des cristaux
C07C 51/265 - Préparation d'acides carboxyliques, de leurs sels, halogénures ou anhydrides par oxydation avec l'oxygène moléculaire de composés contenant des cycles aromatiques à six chaînons sans ouverture du cycle comportant des chaînes latérales alkylées qui sont oxydées en groupes carboxyle
[Problem] To provide a method with which it is possible to produce monocyclic aromatic hydrocarbon such as xylene and benzene effective as a basic material using a crude oil material which contains renewable naphtha and crude oil. [Solution] A method for producing monocyclic aromatic hydrocarbon, which is benzene and/or xylene, using a crude oil material which contains renewable naphtha and crude oil, said method comprising: a step (A-1) for separating a naphtha fraction and other fractions by atmospheric distillation of the crude oil material; a step (A-2) for obtaining a naphtha material by applying desulfurization treatment to the naphtha fraction obtained in the step (A-1); a step (A-3) for separating the naphtha material acquired in the step (A-2) into heavy naphtha and light naphtha by fractional distillation of the naphtha material; and a step (A-4) for generating and separating monocyclic aromatic hydrocarbon, which is benzene and/or xylene, by a cyclization dehydrogenation reaction of paraffin contained in the heavy naphtha obtained in the step (A-3) and/or a dehydrogenation reaction of naphthene contained in the heavy naphtha.
C07C 5/27 - Réarrangement des atomes de carbone dans le squelette hydrocarboné
C07C 7/12 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par adsorption, c.-à-d. purification ou séparation d'hydrocarbures à l'aide de solides, p. ex. à l'aide d'échangeurs d'ions
C07C 7/14 - Purification, séparation ou stabilisation d'hydrocarburesEmploi d'additifs par cristallisationPurification ou séparation des cristaux
C07C 51/265 - Préparation d'acides carboxyliques, de leurs sels, halogénures ou anhydrides par oxydation avec l'oxygène moléculaire de composés contenant des cycles aromatiques à six chaînons sans ouverture du cycle comportant des chaînes latérales alkylées qui sont oxydées en groupes carboxyle
Provided is an asphalt mixture for pavement, the asphalt mixture being obtained by effectively reutilizing discarded electrical wiring and enabling pavement having excellent dynamic stability. The asphalt mixture for pavement comprises aggregate and an asphalt binder. The aggregate contains crosslinked polyethylene recovered from discarded electrical wiring. The asphalt binder contains straight asphalt and a polyolefinic resin.
E01C 5/22 - Revêtements faits d'éléments préfabriqués faits d'éléments composés d'un mélange des matériaux couverts par plusieurs des groupes
C08L 23/04 - Homopolymères ou copolymères de l'éthylène
C08L 23/26 - Compositions contenant des homopolymères ou des copolymères d'hydrocarbures aliphatiques non saturés ne possédant qu'une seule liaison double carbone-carboneCompositions contenant des dérivés de tels polymères modifiées par post-traitement chimique
C08L 95/00 - Compositions contenant des matières bitumeuses, p. ex. asphalte, goudron ou brai
90.
BASE OIL FOR REFRIGERATOR OIL, REFRIGERATOR OIL, AND WORKING FLUID COMPOSITION
Provided is a base oil for a refrigerator oil, the base oil comprising a hexaester of dipentaerythritol with a fatty acid and at least one ester selected from the group consisting of diesters of neopentyl glycol with fatty acids and tetraesters of pentaerythritol with fatty acids including fatty acids having 4-6 carbon atoms.
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
C10N 40/30 - Lubrifiants pour machines frigorifiques
91.
INFORMATION PROCESSING APPARATUS, HYDROGEN PRODUCTION SYSTEM, POWER SUPPLY SYSTEM, OPERATION PLAN CREATION METHOD, AND COMPUTER PROGRAM
NATIONAL INSTITUTE OF ADVANCED INDUSTRIAL SCIENCE AND TECHNOLOGY (Japon)
Inventeur(s)
Harada, Kosuke
Takami, Hirofumi
Okumo, Ichiro
Uehara, Kazuki
Kojima, Hirokazu
Kikusato, Hiroshi
Oozeki, Takashi
Furutani, Hirohide
Abrégé
A hydrogen production system includes a hydrogen production facility and a management server. The management server includes an operation plan creation unit and an operation plan output unit. The operation plan creation unit creates an operation plan for the hydrogen production facility. The operation plan output unit outputs data including the operation plan created by the operation plan creation unit. The operation plan creation unit creates an operation plan for the hydrogen production facility including a demand response possible amount for each unit time based on a demand response consideration for each unit time determined in advance.
C25B 15/02 - Commande ou régulation des opérations
C25B 1/04 - Hydrogène ou oxygène par électrolyse de l'eau
H01M 8/0656 - Combinaison d’éléments à combustible avec des moyens de production de réactifs ou pour le traitement de résidus avec des moyens de production des réactifs gazeux par des moyens électrochimiques
H02J 3/38 - Dispositions pour l’alimentation en parallèle d’un seul réseau, par plusieurs générateurs, convertisseurs ou transformateurs
C10G 65/04 - Traitement des huiles d'hydrocarbures, uniquement par plusieurs procédés d'hydrotraitement uniquement par plusieurs étapes en série ne comprenant que des étapes de raffinage
B01J 35/60 - Catalyseurs caractérisés par leur forme ou leurs propriétés physiques, en général caractérisés par leurs propriétés de surface ou leur porosité
C10G 45/08 - Raffinage des huiles d'hydrocarbures au moyen d'hydrogène ou de composés donneurs d'hydrogène pour éliminer des hétéro-atomes sans modifier le squelette de l'hydrocarbure mis en œuvre et sans craquage en hydrocarbures à point d'ébullition inférieurHydrofinissage caractérisé par le catalyseur utilisé contenant du nickel ou du cobalt, ou leurs composés en combinaison avec du chrome, du molybdène ou du tungstène, ou leurs composés
93.
LUBRICATING OIL COMPOSITION FOR INTERNAL COMBUSTION ENGINES AND METHOD FOR PRODUCING SAME
Provided is a lubricating oil composition for internal combustion engines that contains a lubricating oil base oil, wherein the lubricating oil base oil has a kinematic viscosity at 40°C of 18.0 mm2/s or less, does not contain an olefin copolymer, and has an estimated value X of the change amount per unit time of evaporation loss of the lubricating oil composition, measured by a NOACK evaporation test using conditions of 150°C and 12 hours and determined by a specific calculation formula, of 0.45 mass%/h or less.
C10M 171/00 - Compositions lubrifiantes caractérisées par des critères purement physiques, p. ex. contenant comme matériau de base, épaississant ou additif des ingrédients exclusivement caractérisés par des valeurs numériques particulières de leurs propriétés physiques, c.-à-d. contenant des ingrédients physiquement bien définis mais dont la nature chimique n'est pas précisée ou n'est que très vaguement indiquée
C10M 169/04 - Mélanges de matériaux de base et d'additifs
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
This lubricating oil composition for internal combustion engines contains a lubricant base oil. In the lubricating oil composition: the content of a component having a boiling point of 330°C or lower in the lubricant base oil is 3.2 mass% or less based on the total amount of the lubricant base oil; the lubricant base oil has a kinematic viscosity at 100°C of 2.7 mm2/s to 4.1 mm2/s; the lubricant base oil contains, as a constituent component, at least one base oil component that satisfies specific conditions (I) and (II); and the lubricant base oil contains 15 mass% or more of the base oil component that satisfies the specific conditions (I) and (II) based on the total amount of the lubricant base oil.
C10M 171/00 - Compositions lubrifiantes caractérisées par des critères purement physiques, p. ex. contenant comme matériau de base, épaississant ou additif des ingrédients exclusivement caractérisés par des valeurs numériques particulières de leurs propriétés physiques, c.-à-d. contenant des ingrédients physiquement bien définis mais dont la nature chimique n'est pas précisée ou n'est que très vaguement indiquée
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
The invention provides a novel carbon dioxide adsorbent that can capture carbon dioxide and the like, the carbon dioxide adsorbent being a carbon dioxide adsorbent including a metal-organic framework, the metal-organic framework can capture and desorb carbon dioxide, an isolated voids are formed inside the metal-organic framework by the metal-organic framework's three-dimensional structure, the isolated voids are the space that can capture carbon dioxide and does not have a channel through which carbon dioxide can pass in an ordinary state, and although the three-dimensional structure of the framework changes during the process where carbon dioxide is captured within isolated voids and the process where carbon dioxide is released from isolated voids, the three-dimensional structure of the metal-organic framework when carbon dioxide is captured within the isolated voids is the same as when carbon dioxide is not captured within the isolated voids.
B01J 20/22 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation contenant une substance organique
B01D 53/02 - Séparation de gaz ou de vapeursRécupération de vapeurs de solvants volatils dans les gazÉpuration chimique ou biologique des gaz résiduaires, p. ex. gaz d'échappement des moteurs à combustion, fumées, vapeurs, gaz de combustion ou aérosols par adsorption, p. ex. chromatographie préparatoire en phase gazeuse
B01J 20/28 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtrationAbsorbants ou adsorbants pour la chromatographieProcédés pour leur préparation, régénération ou réactivation caractérisées par leur forme ou leurs propriétés physiques
96.
ORGANIC HYDRIDE PRODUCTION DEVICE AND ORGANIC HYDRIDE PRODUCTION METHOD
This organic hydride production device 2 comprises, as an anode catalyst 11, an anode electrode 10 having a high entropy alloy containing a base metal element, a cathode electrode 8, and an electrolyte membrane 12 positioned between the anode electrode 10 and the cathode electrode 8. The anode electrode 10 oxidizes water or hydroxide ions. The cathode electrode 8 electrochemically reduces a hydride to generate an organic hydride.
C25B 9/23 - Cellules comprenant des électrodes fixes de dimensions stablesAssemblages de leurs éléments de structure avec des diaphragmes comprenant des membranes échangeuses d'ions dans ou sur lesquelles est incrusté du matériau pour électrode
C25B 11/052 - Électrodes comportant un substrat et un ou plusieurs revêtements électro-catalytiques
2/s; (B) 50 mass ppm to 2000 mass ppm of a molybdenum-based friction modifier based on the total amount of the composition as an amount of molybdenum; (C) a nitrogen-containing ashless friction modifier; (D) a succinimide or a derivative thereof as a dispersant; (E) an amine ashless antioxidant as an antioxidant; and (F) 1000 mass ppm to 2200 mass ppm of a metallic detergent based on the total amount of the composition as an amount of metal, wherein the amount of sulfated ash in the composition is 0.9 mass % or less, and a nitrogen management index is 0.60 or less. Provided is a lubricating oil composition for an internal combustion engine having improved fuel efficiency and oxidative stability, while maintaining low amount of sulfated ash.
C10M 129/54 - Acides carboxyliquesLeurs sels comportant des groupes carboxyle liés à un atome de carbone d'un cycle aromatique à six chaînons contenant des groupes hydroxyle
C10M 133/06 - Amines, p. ex. polyalkylènepolyaminesAmines quaternaires comportant des groupes amine liés à des atomes de carbone acycliques ou cycloaliphatiques
C10M 133/08 - Amines, p. ex. polyalkylènepolyaminesAmines quaternaires comportant des groupes amine liés à des atomes de carbone acycliques ou cycloaliphatiques contenant des groupes hydroxyle
C10M 133/12 - Amines, p. ex. polyalkylènepolyaminesAmines quaternaires comportant des groupes amine liés à un atome de carbone d'un cycle aromatique à six chaînons
C10M 141/10 - Compositions lubrifiantes caractérisées en ce que l'additif est un mélange d'au moins deux composés couverts par plus d'un des groupes principaux , chacun de ces composés étant un composé essentiel l'un d'eux, au moins, étant un composé organique contenant du phosphore
C10M 143/00 - Compositions lubrifiantes caractérisées en ce que l'additif est un hydrocarbure macromoléculaire ou un tel hydrocarbure modifié par oxydation
C10M 161/00 - Compositions lubrifiantes caractérisées en ce que l'additif est un mélange d'un composé macromoléculaire et d'un composé non macromoléculaire, chacun de ces composés étant un composé essentiel
C10M 169/04 - Mélanges de matériaux de base et d'additifs
C10N 20/04 - Poids moléculaireRépartition du poids moléculaire
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
C10N 30/04 - Propriétés détergentes ou dispersantes
C10N 30/10 - Inhibition de l'oxydation, p. ex. anti-oxydants
The purpose of the present invention is to provide a viscosity index improver which is suitable for a refrigerator oil, has excellent solubility in a refrigerant and an oxygen atom-containing base oil, and has a high viscosity index-improving effect when used in a refrigerator oil, and with which a refrigerator oil having a low kinematic viscosity at a low temperature can be obtained. The present invention pertains to a viscosity index improver comprising a copolymer (A) that contains, as essential constituent monomers, a fluorine atom-containing monomer (a) represented by general formula (1), a monomer (b) represented by general formula (2), and a silicon atom-containing monomer (c) represented by general formula (3), wherein the solubility parameter of the copolymer (A) is 7.5-9.0 (cal/cm3)1/2.
C09K 5/04 - Substances qui subissent un changement d'état physique lors de leur utilisation le changement d'état se faisant par passage de l'état liquide à l'état vapeur ou vice versa
C10M 169/04 - Mélanges de matériaux de base et d'additifs
C10M 107/24 - Composés macromoléculaires obtenus par des réactions faisant intervenir uniquement des liaisons non saturées carbone-carbone contenant des monomères comportant un radical insaturé lié à un radical alcool, aldéhyde, cétone, éther, cétal ou acétal
C10N 20/00 - Propriétés physiques particulières des constituants des compositions lubrifiantes
C10N 20/04 - Poids moléculaireRépartition du poids moléculaire
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
C10N 30/02 - Point d'écoulementIndice de viscosité
C10N 40/30 - Lubrifiants pour machines frigorifiques
99.
INFORMATION PROCESSING SYSTEM, INFORMATION PROCESSING METHOD, AND PROGRAM
Provided is an information processing system comprising: a first reception unit that receives position information from a terminal; and a display processing unit that, on the basis of the position information, displays on a screen of the terminal at least one hydrogen station and a type of hydrogen which is from among a plurality of types of hydrogen produced via a plurality of methods having differing carbon dioxide emission amounts, and for which filling is possible at said at least one hydrogen station.
This hydraulic oil composition for a shock absorber comprises components (A) and (B), wherein the component (A) is an ester base oil that has a pour point of -45°C or lower and has a 10% distillation temperature of 300°C or higher, the 10% distillation temperature being determined in accordance with the gas chromatographic distillation test method defined in JIS K 2254:1998 and component (B) is a zinc dialkyl dithiophosphate.
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
C10N 30/02 - Point d'écoulementIndice de viscosité
C10N 30/06 - OnctuositéRésistance du filmAnti-usureRésistance aux pressions extrêmes
C10N 40/06 - Instruments ou autres appareils de précision, p. ex. fluides amortisseurs
