A method of manufacturing an organic EL element having a corrugated structure, the organic EL element comprising a transparent supporting substrate, a transparent electrode, an organic layer, and a metal electrode, the method comprises the steps of: laminating on the transparent supporting substrate a curable-resin layer having concavity and convexity formed thereon in a periodic arrangement in a way that a curable resin is applied onto the transparent supporting substrate, the curable resin is then cured with a master block being pressed thereto, and thereafter the master block is detached; and obtaining an organic EL element by laminating on the curable-resin layer the transparent electrode, the organic layer, and the metal electrode individually so that a shape of the concavity and convexity formed on a surface of the curable-resin layer can be maintained.
H01L 21/00 - Procédés ou appareils spécialement adaptés à la fabrication ou au traitement de dispositifs à semi-conducteurs ou de dispositifs à l'état solide, ou bien de leurs parties constitutives
H01L 29/08 - Corps semi-conducteurs caractérisés par les formes, les dimensions relatives, ou les dispositions des régions semi-conductrices avec des régions semi-conductrices connectées à une électrode transportant le courant à redresser, amplifier ou commuter, cette électrode faisant partie d'un dispositif à semi-conducteur qui comporte trois électrodes ou plus
2.
Method of treating biomass, fuel for fuel cell, gasoline, diesel fuel, liquefied petroleum gas, and synthetic resin
Disclosed is a lubricant composition which exhibits excellently low friction and excellent low-temperature storage stability, while having high flash point. Specifically disclosed is a lubricant composition for a sliding guide surface having excellent positioning performance, which is characterized by containing, in a lubricant base oil, (A) an acidic phosphate ester represented by the general formula (1) below in an amount of 0.02-0.1% by mass based on the total amount of the composition and (B) an aliphatic monoamine represented by the general formula (2) below in an amount of 0.005-0.1% by mass based on the total amount of the composition. (R1O)mP(=O)(OH)3-m (1) (In the formula (1), R1 represents a linear alkyl group having 4-8 carbon atoms, and m represents 1 or 2. When m is 2, the R1s may be the same as or different from each other.) R2nNH3-n (2) (In the formula (2), R2 represents a linear alkyl group or linear alkenyl group having 12-18 carbon atoms, and n represents an integer of 1-3. When n is 2 or 3, the R2s may be the same as or different from each other.)
C10M 169/04 - Mélanges de matériaux de base et d'additifs
C10M 133/06 - Amines, p. ex. polyalkylènepolyaminesAmines quaternaires comportant des groupes amine liés à des atomes de carbone acycliques ou cycloaliphatiques
a poly(meth)acrylate based viscosity index improver including a structural unit represented by general formula (1):
2/s at 100° C. and a viscosity index of 140 to 300.
A process for the preparation of norbornene derivatives, characterized by reacting a norbornadiene derivative of general formula (2) [wherein R2, R3, R4, R5 and R6 are each independently a hydrogen atom or the like; l is an integer of 0 or 1; m is an integer of 0 or 1; and n is an integer of 0 or 1] with a halogen compound of general formula (3): [wherein Z is a phenylene group or the like; X is a chlorine atom or the like; and R7 is a hydrogen atom or the like] in the presence of a solvent such as N,N-dimethylformamide, a reducing agent, and a palladium catalyst wherein phosphine ligands of general formula (1) [wherein R1s are each independently a cyclic aliphatic hydrocarbon group] coordinate to a divalent palladium atom, and thereby obtaining a norbornene derivative of general formula (4) [wherein R8, R9, R10, R11, R12, l, m and n are as defined for R2, R3, R4, R5, R6, l, m, n in general formula (2); R13 is as defined for R7 in general formula (3); and Z is as defined for Z in general formula (3)], wherein the substituent Z in general formula (4) is configured in the exo form.
C07C 2/72 - Addition à un atome de carbone non aromatique d'hydrocarbures contenant un cycle aromatique à six chaînons
C07C 13/605 - Hydrocarbures polycycliques ou leurs dérivés hydrocarbonés acycliques à cycles condensés à trois cycles condensés à système cyclique ponté
C07C 43/205 - Éthers une liaison sur l'oxygène de la fonction éther étant sur un atome de carbone d'un cycle aromatique à six chaînons le cycle aromatique n'étant pas condensé
C07C 205/06 - Composés contenant des groupes nitro liés à un squelette carboné ayant des groupes nitro liés à des atomes de carbone de cycles aromatiques à six chaînons
Provided are a liquid delivery system wherein a pump downstream of a desulfurizer can be stably controlled, and a liquid fuel can be efficiently delivered; and a fuel cell system provided with the liquid delivery system. On the upstream side of a pump (105), a liquid fuel passes through a gas-liquid separating portion (103), so that gas bubbles of the liquid fuel which has been cooled by a cooling mechanism (101) and decompressed by a decompression mechanism (102) to reduce the solubility of the liquid fuel, are removed to separate gas from the liquid fuel. Further, the liquid fuel which has passed through the gas-liquid separating portion (103) is stored in a gas-liquid separating tank (104), so that the gas contained in the liquid fuel is moved upwardly in the liquid fuel to collect the gas on the upper side of the gas-liquid separating tank (104), and collect the liquid on the bottom side of the gas-liquid separating tank (104). Thus, the gas and the liquid of the liquid fuel are separated, so that the liquid fuel, the gas of which has been sufficiently removed, can be supplied to the pump (105).
H01M 8/06 - Combinaison d’éléments à combustible avec des moyens de production de réactifs ou pour le traitement de résidus
H01M 8/10 - Éléments à combustible avec électrolytes solides
C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
Provided is a surface combustion burner wherein the possibility of backfire is reduced. A surface combustion burner which burns the mixture of vaporized kerosene and air on the combustion surface has a funnel-like channel, i.e. a channel in the shape of a funnel having the cross-sectional area enlarged toward the combustion surface, which introduces the mixture to the combustion surface.
Provided is a kerosene carburetor which can avoid the necessity of an air pump, a flowmeter and a controller for both the combustion air and the cooling air supplied to a surface combustion burner. A kerosene carburetor which supplies the mixture of vaporized kerosene and air to a surface combustion burner comprises a kerosene vaporization pot equipped with a heater and internally vaporizing kerosene, a kerosene channel, i.e. a channel communicating with the interior of the kerosene vaporization pot, through which kerosene is introduced to the kerosene vaporization pot, a first air channel, i.e. a channel communicating with the interior of the kerosene vaporization pot, through which air is introduced to the kerosene vaporization pot, a mixture channel, i.e. a channel communicating with the interior of the kerosene vaporization pot, through which the mixture of vaporized kerosene and air is discharged from the kerosene vaporization pot, a second air channel, i.e. a channel branched from the first air channel, and an orifice provided in the second air channel.
Provided is a fuel reformer having a multicylindrical structure such that the size of the fuel reformer can be reduced. The reformer is for reforming kerosene to produce reformed gas and comprises a burner for burning kerosene; a combustion cylinder having a cylindrical shape that forms a region through which the combustion gas generated by the burner is allowed to flow; a reforming catalyst layer having a hollow cylindrical shape that is disposed coaxially with the combustion cylinder inside the combustion cylinder; and a primary partition wall, which has a cylindrical shape, is disposed to the inside of the inner peripheral surface of the reforming catalyst layer and is for demarcating the region through which the combustion gas is allowed to flow and the reforming catalyst layer.
C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
Japan Oil, Gas and Metals National Corporation (Japon)
Inpex Corporation (Japon)
Nippon Oil Corporation (Japon)
Japan Petroleum Exploration Co., Ltd. (Japon)
Cosmo Oil Co., Ltd. (Japon)
Inventeur(s)
Onishi, Yasuhiro
Abrégé
There is provided a synthesis reaction system which synthesizes a hydrocarbon compound by a chemical reaction of a synthesis gas including hydrogen and carbon monoxide as main components, and a slurry having solid catalyst particles suspended in liquid and which extracts the hydrocarbon compound from the slurry. The synthesis reaction system includes a reactor main body which accommodates the slurry, a separator which separates the hydrocarbon compound included in the slurry from the slurry, a first flow passage which allows the slurry including the hydrocarbon compound to flow to the separator from the reactor main body, a second flow passage which allows the slurry to flow to the reactor main body from the separator, and a fluid supply nozzle which supplies a fluid toward at least any one of the separator, the first flow passage, and the second flow passage.
B01J 8/20 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées l'agent fluidisant étant un liquide
C07C 27/00 - Procédés impliquant la production simultanée de plusieurs classes de composés contenant de l'oxygène
11.
PROCESS AND DEVICE FOR PRODUCING COMPOSITE CONTAINER
A process for producing a composite container which has a desired shape and strength. A tow prepreg is wound around a liner to form a fibrous layer (S4). The fibrous layer is heated from inside the liner to reduce the viscosity of the resin infiltrated into the fibers wound around the liner to a value lower than the viscosity as measured before the winding around the liner (S5). Thereafter, the fibrous layer is heated from inside the liner to gradually cure the resin of the fibrous layer from the side near the liner surface toward the side apart therefrom (S6). Alternatively, a tow prepreg is wound around a liner to form a fibrous layer, and the fibrous layer is heated from inside the liner. The resin infiltrated into the fibers wound around the liner is thereby gradually cured from the side near the liner surface toward the side apart therefrom and is caused to generate heat as the curing proceeds.
B29C 70/06 - Façonnage de matières composites, c.-à-d. de matières plastiques comprenant des renforcements, des matières de remplissage ou des parties préformées, p. ex. des inserts comprenant uniquement des renforcements, p. ex. matières plastiques auto-renforçantes des renforcements fibreux uniquement
B29C 70/16 - Façonnage de matières composites, c.-à-d. de matières plastiques comprenant des renforcements, des matières de remplissage ou des parties préformées, p. ex. des inserts comprenant uniquement des renforcements, p. ex. matières plastiques auto-renforçantes des renforcements fibreux uniquement caractérisées par la structure des renforcements fibreux utilisant des fibres de grande longueur, ou des fibres continues
F17C 1/06 - Enveloppes protectrices constituées par un enroulement de bandes ou de matériaux filiformes p. ex. fils métalliques
12.
APPARATUS FOR PROCESSING EXHAUST GAS AND METHOD FOR PROCESSING EXHAUST GAS
A gas mixture discharged from a semiconductor manufacturing apparatus (20) is sent to a filter unit (30) by means of a pump (12), and after removing higher silanes in the filter unit (30), the gas mixture is separated into hydrogen and monosilane by means of a separation unit (40) which utilizes low temperature separation. The separated monosilane is removed by a silane gas removal unit (50). Meanwhile, the separated hydrogen is discharged into the atmosphere by a hydrogen gas discharge unit (60).
B01D 53/46 - Élimination des composants de structure définie
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
C23C 16/44 - Revêtement chimique par décomposition de composés gazeux, ne laissant pas de produits de réaction du matériau de la surface dans le revêtement, c.-à-d. procédés de dépôt chimique en phase vapeur [CVD] caractérisé par le procédé de revêtement
F25J 3/08 - Séparation des impuretés gazeuses des gaz ou des mélanges gazeux
H01L 21/205 - Dépôt de matériaux semi-conducteurs sur un substrat, p. ex. croissance épitaxiale en utilisant la réduction ou la décomposition d'un composé gazeux donnant un condensat solide, c.-à-d. un dépôt chimique
Provided is a minimal flow rate liquid pump control device wherein the cost thereof can be reduced, and a minimal flow rate can be controlled with high accuracy. The amount of liquid within a liquid level adjuster (3) is measured to obtain measured values including the amount of reduced liquid, the average amount of reduced liquid, etc. In the range of minimal flow rate, it is difficult to directly measure the flow rate of liquid because the flow rate is infinitesimal. However, the total amount of liquid can be measured after the elapse of a certain period of time. Therefore, the measured value is compared with a value calculated on the basis of an instruction value, so that the difference between the actual amount of the transferred liquid and the calculated amount of the transferred liquid can be obtained. Further, if there is a difference therebetween, the instruction value is corrected to improve the accuracy of control of the flow rate. Further, the liquid level adjuster (3) which stores the liquid of a pump (2) is extremely less expensive than a expensive pump or flow rate measuring device. This prevents the cost for the entire system from increasing.
The production process of the invention comprises a first step of hydrodesulfurizing of catalytically-cracked gasoline so as to result in an olefin hydrogenation rate of no greater than 25 mol % in the catalytically-cracked gasoline, a total sulfur content of no greater than 20 ppm by weight based on the product oil weight, a sulfur content derived from thiophenes and benzothiophenes of no greater than 5 ppm by weight and a sulfur content derived from thiacyclopentanes of no greater than 0.1 ppm by weight, and a second step of further hydrodesulfurizing of the product oil obtained by the first step so as to result in a total of no greater than 30 mol % for the olefin hydrogenation rate in the first step and the olefin hydrogenation rate in the second step, a total sulfur content of no greater than 10 ppm by weight based on the product oil weight, and a sulfur content derived from thiols of no greater than 5 ppm by weight.
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 45/08 - 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
C10G 65/02 - Traitement des huiles d'hydrocarbures, uniquement par plusieurs procédés d'hydrotraitement uniquement par plusieurs étapes en série
A desulfurization device (3) equipped with: a desulfurizer (7) containing therein a desulfurization catalyst (7a) with which sulfur is removed from a liquid fuel to be supplied to a reformer (5) which generates a hydrogen-containing reformed gas; a heater (8) which heats the desulfurization catalyst (7a); a manometer (14) which measures the pressure of the liquid fuel inside the desulfurizer (7); and a control unit (15) which controls the heater (8). The control unit (15) controls, on the basis of the pressure measured by the manometer (14), the heater (8) so that the pressure of the liquid fuel inside the desulfurizer (7) is kept at a given pressure which is the withstand pressure of the desulfurizer (7) or lower. By using this configuration, it is possible to provide the desulfurization device (3) and the fuel cell system in each of which the desulfurizer (7) can be inhibited from decreasing in reliability and durability.
C10G 29/00 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, au moyen d'autres produits chimiques
C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
H01M 8/06 - Combinaison d’éléments à combustible avec des moyens de production de réactifs ou pour le traitement de résidus
H01M 8/10 - Éléments à combustible avec électrolytes solides
16.
UPGRADING METHOD FOR LOW-GRADE COAL, AND PROCESS FOR PRODUCTION OF COKE
An upgrading method for converting a low-grade coal having a low rank of coalification into an equivalent of caking coal, characterized by comprising at least a modification step of heating a powdery low-grade coal having a low rank of coalification to a temperature of 350 to 450°C in the presence of a petroleum- or coal-based modifier to modify the low-grade coal, said low-grade coal being a coal having a reactive maceral content exceeding 50% as determined by coal maceral analysis. Thus provided is an upgrading method for converting a non-caking or slightly caking coal, which is classified as low-grade coal, into an equivalent of caking coal which can be used as a material in producing coke for iron-making or the like.
C10B 57/08 - Traitement préalable non mécanique de la charge
C10B 53/08 - Distillation destructive spécialement conçue pour des matières premières solides particulières ou sous forme spéciale sous forme de briquettes, mottes ou similaires
A method of designing a gas-solid separator that has an inner cylinder having a closed lower end and an opened upper end, and extending in a vertical direction; an outer cylinder that coaxially covers the inner cylinder from the outside and has a gas vent port formed on the upper end side of the inner cylinder and communicating with an exterior; and a plurality of axially extending long holes formed a side surface on the lower end side of the inner cylinder in a circumferential direction, one of long side edge parts of each of the long holes being provided with a guide blade that protrudes outward and is inclined circumferentially so as to cover the long hole.
A hydroisomerization catalyst according to the present invention is obtained by calcining a catalyst composite including an ion-exchanged molecular sieve or a calcined material thereof which is obtained by performing ion exchange of a molecular sieve containing an organic template in a solution containing a cation species and using water as a main solvent and at least one metal which is selected from a group consisting of metals belonging to Groups 8-10 of the Periodic Table of the Elements, molybdenum, and tungsten supported on the ion-exchanged molecular sieve or a calcined material thereof.
The hydrocarbon desulfurizing agent contains a porous inorganic oxide, nickel and/or a nickel oxide, zinc oxide, cobalt and/or a cobalt oxide, and molybdenum and/or a molybdenum oxide. The content of the porous inorganic oxide is 10‑30 mass%, the content of the nickel and/or the nickel oxide is 45‑75 mass%, and the content of the zinc oxide is 3‑40 mass% in terms of oxide, based on the total mass of the desulfurizing agent. According to the invention, it is possible to provide a hydrocarbon desulfurizing agent and a manufacturing method thereof with which sufficient desulfurizing capability can be sustained over a long period of time even when a starting material fuel such as kerosene is desulfurized under low-pressure conditions or in the absence of hydrogen, as well as provide a kerosene desulfurization method which utilizes said desulfurizing agent and a fuel cell system.
C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
C01B 3/48 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants suivie par une réaction de la vapeur d'eau avec l'oxyde de carbone
C10G 25/00 - Raffinage des huiles d'hydrocarbures, en l'absence d'hydrogène, au moyen d'absorbants ou d'adsorbants solides
C10G 29/04 - Métaux ou métaux déposés sur un support
2s], W/D=0.2 to 0.5, u1=5 to 300 [m/s], and u2=5 to 300 [m/s] are satisfied when a mass flow per unit area of a moving bed is Q [kg/nes], the difference between an outer diameter and an inner diameter of the moving bed is W [m], an inner diameter of a reaction tube is D [m], a linear velocity of a horizontal component of the stock oil at a jet orifice of the internal stock oil injection nozzle u1 [m/s], and a linear velocity of a horizontal component of the stock oil at a jet orifice of the external stock oil injection nozzle u2 [m/s].
B01J 8/08 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés avec des particules mobiles
When the production of hydrogen and the recovery of carbon dioxide are simultaneously performed by using as a raw material a carbon-containing fuel, the increase of the system cost is suppressed and the efficiency is improved. Disclosed is a method for producing hydrogen and recovering carbon dioxide which method produces hydrogen from a carbon-containing fuel and recovers carbon dioxide, including: a hydrogen-containing gas producing step of obtaining a hydrogen-containing gas that contains hydrogen and carbon dioxide by reforming a carbon-containing fuel; a PSA step of separating, by using a pressure swing adsorption apparatus, the hydrogen-containing gas into a first hydrogen-enriched gas that is a gas enriched in hydrogen and a PSA offgas that is a gas enriched in the components other than hydrogen; and a step of obtaining, by treating the PSA offgas with a hydrogen separation membrane and a carbon dioxide separation membrane, a second hydrogen-enriched gas that is a gas enriched in hydrogen and a carbon dioxide-enriched gas that is a gas enriched in carbon dioxide. Also disclosed is an apparatus for embodying the method.
C01B 3/02 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène
C01B 3/22 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par décomposition de composés organiques gazeux ou liquides
C01B 3/24 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par décomposition de composés organiques gazeux ou liquides d'hydrocarbures
C01B 3/26 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par décomposition de composés organiques gazeux ou liquides d'hydrocarbures avec des catalyseurs
22.
Fluid catalytic cracking process, and gasoline and liquefied petroleum gas obtained by the process
The fluid catalytic cracking process according to the present invention includes a first step of feeding a feedstock to a first fluid catalytic cracker, and catalytically cracking the feedstock in the first fluid catalytic cracker, so as to produce a fraction (LCO) having a boiling range of 221 to 343° C. and having a total aromatic content of 40 to 80 volume %; and a second step of feeding an oil to be processed containing the fraction to a second fluid catalytic cracker having a reaction zone, a separation zone, a stripping zone, and a regeneration zone, and catalytically cracking the oil in the reaction zone of the second fluid catalytic cracker, in the presence of a cracking catalyst, at an outlet temperature of the reaction zone of 550 to 750° C., a contact time between the oil and the catalyst of 0.1 to 1 second, and a catalyst/oil ratio of 20 to 40 wt/wt.
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"
C10G 51/02 - Traitement des huiles d'hydrocarbures, en l'absence d'hydrogène, uniquement par plusieurs procédés de craquage uniquement par plusieurs étapes en série
C10L 1/06 - Combustibles carbonés liquides à base essentielle de mélanges d'hydrocarbures pour allumage par bougie
Provided is a process for production of a hydrocarbon composition. In the process, urea is brought into contact with a hydrocarbon raw material comprising branched paraffins which each bear an alkyl group branch having five or less carbon atoms, whereby, among the branched paraffins, branched paraffins each having six or more carbon atoms between at least one end and the branch position are separated from the hydrocarbon raw material in the form of urea adducts. Thus, an objective hydrocarbon composition is obtained. The composition exhibits a high viscosity index and excellent low-temperature characteristics and is particularly suitable for use as a lube base oil or a lubricating oil composition.
C10G 73/24 - Obtention des cires de pétrole à partir des huiles d'hydrocarburesDéparaffinage d'huiles d'hydrocarbures par formation de produits d'addition
C10G 29/20 - Composés organiques ne renfermant pas d'atomes métalliques
C10L 1/04 - Combustibles carbonés liquides à base essentielle de mélanges d'hydrocarbures
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
C10N 30/02 - Point d'écoulementIndice de viscosité
2/s, pour point being −15 degree C. or less, aniline point being 100 degree C. or more, paraffinic content in saturates being 40 mass % or more, monocyclic naphthenic content being 25 mass % or less, bicyclic to hexacyclic naphthenic content being 35 mass % or less, iodine number being 2 or less, and ratio of tertiary carbon to the total carbon atoms composing the (A1) being 6.3% or more. The total mass of the composition is: (B) 0.005 to 0.5 mass % of a metallic detergent as metal content; (C1) 0.005 to 0.2 mass % of a boron-containing succinimide ashless dispersant as boron content; and (D) 0.005 to 0.2 mass % of a metal salt of phosphorus-containing acid as phosphorus content.
A process for hydrocarbon oil production which comprises: a first step in which a raw oil comprising oxygenic organic compounds and water-insoluble chlorine compounds is brought into contact with an adsorbent constituted of a porous inorganic oxide and at least one metal selected from the elements in Group IA, Group IIA, and Group IB to adsorb the water-insoluble chlorine compounds onto the adsorbent and thereby obtain a dechlorinated oil; a second step in which the dechlorinated oil is brought into contact with a hydrogenation catalyst constituted of a support comprising a porous inorganic oxide and at least one metal deposited on the support and selected from the elements in Group VIA and Group VIII of the periodic table, in the presence of hydrogen to yield reaction products including a hydrocarbon oil and water through the deoxidizing hydrogenation of the oxygenic organic compounds; and a third step in which the water is separated from the reaction products to obtain a product oil comprising the hydrocarbon oil.
C10G 67/06 - Traitement des huiles d'hydrocarbures, uniquement par au moins un procédé d'hydrotraitement et au moins un procédé de raffinage en l'absence d'hydrogène uniquement par plusieurs étapes en série comprenant un procédé d'absorption ou d'adsorption comme étape de raffinage en l'absence d'hydrogène
C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
C10G 25/05 - Élimination des composés autres que des hydrocarbures, p. ex. des composés soufrés
C10G 45/04 - 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
The cavity of a formwork body (1) wherein the inside of an outer shell (6) provided with a sealable cavity is heated to a designed temperature range higher than the melting point of sulfur is fully packed with a sulfur-containing material. As the sulfur-containing material becomes cold and thus shrinks within the cavity as described above, a lid is put on the top opening (11). Thus, the inside becomes sealable and a definite pressure is applied thereto. At the same time, replenish sulfur-containing material contained in a replenish tank (2), the inside of which has been heated to the designed temperature range as described above, is supplied into the cavity due to the pressure applied to the above-described replenish tank (2).
The refrigerating machine oil of the invention is characterized by comprising an ester of a polyhydric alcohol and fatty acids with a content of a C10-C13 branched fatty acid of 50% by mole or greater. The working fluid composition for a refrigerating machine of the invention is characterized in that the working fluid composition comprises an ester of a polyhydric alcohol and fatty acids with a content of a C10-C13 branched fatty acid of 50% by mole or greater, and a refrigerant.
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
28.
LUBRICANT OIL COMPOSITION IN CONTACT WITH A SILVER-CONTAINING MATERIAL
Disclosed is a lubricant oil composition containing: a lubricant base oil comprised of a mineral base oil and/or a synthetic base oil; (A) a metal system cleaning agent; (B) one type or two types or more of alkenyl succinimide and/or boron-containing alkenyl succinimide, and (C) zinc dialkyl dithiophosphate. With the total amount of the lubricant oil composition as a reference, the lubricant oil composition contains: as the amount of metal, 0.12 mass% - 2.0 mass% of component (A); as the amount of boron, 0 mass% - 0.03 mass%, and as the amount of nitrogen, 0.005 mass% - less than 0.08 mass% of component (B), with the mass ratio (B/N) of the boron amount (B) and the nitrogen amount (N) being 0 – 0.55, and as the amount of phosphorous, 0.005 mass% - 0.10 mass% of component (C). Thus, it is possible to provide a lubricant oil composition that, even though zinc dialkyl dithiophosphate is contained, can inhibit corrosion of a silver-containing material as a lubricant oil in contact with a silver-containing material.
C10M 107/02 - Polymères d'hydrocarburesPolymères d'hydrocarbures modifiés par oxydation
C10M 129/10 - Composés hydroxylés comportant des groupes hydroxyle liés à un atome de carbone d'un cycle aromatique à six chaînons
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 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
The present invention provides a lubricating base oil comprising saturated components of 90% by mass or greater, wherein the proportion of cyclic saturated components among the saturated components is not greater than 40% by mass, and by having a viscosity index of 110 or higher and an iodine value of not greater than 2.5. The lubricating base oil of the invention exhibits excellent viscosity-temperature characteristics and heat and oxidation stability while also allowing additives to exhibit a higher level of function when additives are included. The lubricating base oil of the invention is suitable for use in various lubricating oil fields, and is especially useful for reducing energy loss and achieving energy savings in devices in which the lubricating base oil is applied.
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
31.
Method of minimal quantity lubrication cutting/grinding processing and oil composition used therefor
The present invention provides a method of minimal quantity lubrication cutting and grinding that can improve cutting and grinding properties and extend the life of tools. The minimal quantity lubrication cutting and grinding method of the present invention comprises supplying a compressed fluid containing 0.1 to 15 percent by volume of oxygen together with a cutting and grinding oil (particularly preferably an oil composition comprising an ester) to processing spots of a workpiece.
B26D 7/08 - Moyens de traitement de la pièce ou de l'outil de coupe pour faciliter la coupe
B24B 49/00 - Appareillage de mesure ou de calibrage pour la commande du mouvement d'avance de l'outil de meulage ou de la pièce à meulerAgencements de l'appareillage d'indication ou de mesure, p. ex. pour indiquer le début de l'opération de meulage
A gas-solid separator has: an inner cylinder 10 having a closed lower end 11 and an opened upper end 1, and extending in a vertical direction; and an outer cylinder 2 that coaxially covers the inner cylinder 10 from the outside and has a gas vent port 6 formed on the upper end side and communicating with an exterior, wherein a plurality of axially extending long holes 4 are formed on a side surface on the lower end 11 side of the inner cylinder 10 in a circumferential direction, one of long side edge parts of each of the long holes 4 is provided with a guide blade 5 that protrudes outward and is inclined circumferentially so as to cover the long hole 4, and in a section of the outer cylinder 2 that surrounds the plurality of long holes 4 of the inner cylinder 10, an inner diameter D1 of a lower part is larger than an inner diameter D2 of an upper part.
A hydrocarbon oil is obtained by hydrogenating a raw material oil containing an oxygen-containing hydrocarbon compound derived from an animal/plant oil, and a catalyst containing a porous inorganic oxide containing two or more elements selected from aluminum and the like and one or more metals selected from group 6A and group 8 elements of the periodic table and supported by the porous inorganic oxide, in the presence of hydrogen at a hydrogen pressure of not less than 1 MPa but less than 6 MPa; and then removing hydrogen and the like from the resulting hydrogenated product. The raw material oil contains a recycle oil which is obtained by recyclingly supplying a part of the hydrocarbon oil obtained by the preceding step in an amount of 0.5-5 times the mass of the oxygen-containing hydrocarbon compound, and 1-50 ppm by mass of a sulfur-containing hydrocarbon compound in terms of sulfur atoms with respect to the oxygen-containing hydrocarbon compound.
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
C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
A gas oil base material which consists of a hydrocarbon fraction obtained by hydrotreating a raw material oil in the presence of hydrogen, wherein the raw material oil contains oxygen -containing hydrocarbons resulting from an animal or vegetable oil, aliphatic hydrocarbons, and sulfur-containing hydrocarbons. Further, the gas oil base material is characterized in that the n-paraffin content is 90mass% or above and that the average of (Bn-1/An) values in the range of 10≤n≤20 is 0.30 or above, wherein An is total content (unit: mass%) of paraffins having n carbon atoms in the hydrocarbon fraction; Bn-1 is total content (unit: mass%) of paraffins having (n-1) carbon atoms therein; and (Bn-1/An) is a ratio of Bn-1 to An, with the proviso that n (which represents the number of carbon atoms) is a prescribed even number satisfying the relationship: 10 ≤ n ≤ 20.
The present invention provides a lubricating oil composition with excellent torque capacity and shifting characteristics suitable for use as automatic or continuously variable transmission fluids, which composition comprises a base oil and, on the basis of the total mass of the composition, (A) a sulfonate detergent in an amount of 0.01 to 0.3 percent by mass in terms of metal (MeA); (B) a salicylate detergent in an amount of 0 or more than 0 and 0.1 percent by mass or less, in terms of metal (MeB); and (C) a boron-containing succinimide type ashless dispersant in an amount of 0.001 to 0.1 percent by mass in terms of boron (BoC); (MeB)/(MeA) being 0, or greater than 0 and 1.5 or less, and (MeA)/(BoC) being from 0.001 to 20.
C10M 133/44 - Cycle à cinq chaînons ne contenant que du carbone et de l'azote
C10M 163/00 - Compositions lubrifiantes caractérisées en ce que l'additif est un mélange d'un composé de constitution indéterminée ou incomplètement déterminée et d'un composé non macromoléculaire, chacun de ces composés étant un composé essentiel
37.
Raw coke for electricity storage carbon material and needle coke
The present invention provides a raw coke having such a structure that the graphitized product resulting from graphitization of the raw coke at a temperature of 2800° C. under an inactive gas atmosphere will have ratios of the crystallite size to the lattice constant of 360 or less in the (002) plane and 1500 or less in the (110) plane, as a raw coke providing active carbon produced by alkali-activating the raw coke, which is reduced in remaining alkali content and can simplify washing operation because washing liquid can easily pass through the activated carbon, or as a raw coke for the production of needle coke.
H01G 9/00 - Condensateurs électrolytiques, redresseurs électrolytiques, détecteurs électrolytiques, dispositifs de commutation électrolytiques, dispositifs électrolytiques photosensibles ou sensibles à la températureProcédés pour leur fabrication
C10C 3/00 - Traitement du brai, de l'asphalte, du bitume
C10G 11/00 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures
C10G 9/14 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures dans des tubes ou serpentins avec ou sans dispositifs auxiliaires, p. ex. "digesteurs", chambres de maturation, dispositifs d'expansion
H01B 1/04 - Conducteurs ou corps conducteurs caractérisés par les matériaux conducteurs utilisésEmploi de matériaux spécifiés comme conducteurs composés principalement soit de compositions à base de carbone-silicium, soit de carbone soit de silicium
H01B 1/24 - Matériau conducteur dispersé dans un matériau organique non conducteur le matériau conducteur comportant des compositions à base de carbone-silicium, du carbone ou du silicium
38.
VACUUM INSULATING MATERIAL AND METHOD FOR PRODUCING THE SAME
Disclosed are a vacuum insulating material having excellent heat insulating performance, and a method for producing the vacuum insulating material. A vacuum insulating material (1) has a filler (2) and an outer covering member (3) having a vacuum inside and enclosing the filler (2). The filler (2) is obtained by laminating two or more fiber array layers wherein continuous long fibers composed of a thermoplastic resin are stretched and arrayed generally linearly in one direction. The long fibers in an array layer are arranged in a direction which intersects the direction in which the long fibers in an adjacent array layer are arranged.
A kerosene composition excellent in combustibility, oxidative stability, and life-cycle characteristics is provided. The kerosene composition is obtained by mixing 10-90 vol.% kerosene base and 90-10 vol.% kerosene fraction obtained by the refining of, e.g., crude oil. The kerosene base is produced by hydrotreating, as a raw material, an animal/vegetable fat in which the proportion of constituent fatty acids having an alkyl group with 10-14 carbon atoms is 60 mass% or higher. The hydrotreating is conducted in the presence of hydrogen using a catalyst which comprises a porous inorganic oxide containing two or more elements selected among aluminum, silicon, zirconium, boron, titanium, and magnesium and, deposited on the inorganic oxide, a metal selected among the elements in Group 6A and Group 8 of the periodic table, under the conditions of a hydrogen pressure of 2-13 MPa, liquid hourly space velocity of 0.1-3.0 h-1, hydrogen/oil ratio of 150-1,500 NL/L, and reaction temperature of 150-480°C. The kerosene composition has an initial boiling point of 140°C or higher, final boiling point of 300°C or lower, flash point of 40°C or higher, sulfur content of 10 mass ppm or lower, 15°C density of 740-820 kg/m3, smoke point of 23 mm or more, and peroxide value less than 1 mass ppm.
A lubricating oil composition for wet clutches and/or four-cycle engines for motorcycles which can improve the power transmission performance of a wet clutch and reduce the friction of an engine and which is excellent in fuel consumption reduction, specifically, a lubricating oil composition which comprises a lube base oil, (A) 0.01 to 0.2mass% (in terms of phosphorus) of a metal salt of a prescribed phosphorus compound, (B) 0.005 to 0.5mass% (in terms of metal) of a metallic detergent consisting of a metal salt of an aromatic acid having a branched alkyl group, (C) 0.005 to 0.10mass% (in terms of boron) of a boron-modified succinimide ashless dispersant, and (D) 0.01 to 0.10mass% (in terms of molybdenum) of molybdenum dithiocarbamate.
C10M 129/10 - Composés hydroxylés comportant des groupes hydroxyle liés à un atome de carbone d'un cycle aromatique à six chaînons
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 135/18 - ThioacidesThiocyanatesLeurs dérivés comportant une liaison double carbone-soufre du type thiocarbamique, c.-à-d. contenant les groupes
C10M 135/30 - ThiolsSulfuresPolysulfures contenant des atomes de soufre liés à un atome de carbone d'un cycle aromatique à six chaînons contenant des groupes hydroxyleLeurs dérivés
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
C10M 159/24 - Mélanges réactionnels comportant un excès de base neutralisante, p. ex. produits appelés superbasiques ou hautement basiques contenant des radicaux sulfoniques
Disclosed is a lubricant composition having excellent oxidation stability, which is characterized by containing, as a main component of a base oil, (A) a mineral oil having a composition including 10-50% by mass of a total aromatic content and 0.1-1.0% by mass of a sulfur content, a viscosity index of 85-100 and a pour point of not more than -10˚C. The lubricant composition is also characterized by further containing, based on the total amount of the composition, (B) 0.01-5% by mass of an antioxidant, (C) 0.01-0.1% by mass of an alkylphenoxy carboxylic acid, and (D) 0.005-0.1% by mass of a triazole derivative.
C10M 129/40 - Acides carboxyliquesLeurs sels comportant des groupes carboxyle liés à des atomes de carbone acycliques ou cycloaliphatiques comportant au moins 8 atomes de carbone monocarboxyliques
C10M 133/44 - Cycle à cinq chaînons ne contenant que du carbone et de l'azote
Disclosed is a production method of solidified sulfur wherein materials containing sulfur in a molten state is stored in a material hopper (1) heated to within a set temperature range not lower than the melting point of sulfur, the materials containing sulfur thus stored is sucked by means of pressure generators (2a, 2b) and led out to cylinders (11a, 11b) heated to within the above-mentioned set temperature range, the materials containing sulfur thus led out is extruded from the cylinders by applying a predetermined pressure by the pressure generators and is poured through an inlet (24) into a formwork (5) that has an inner cavity in an enclosable state and is heated to within the above-mentioned set temperature range, the inlet of the formwork is closed after the cavity is filled with the materials containing sulfur, the materials containing sulfur poured into the cavity is cooled gradually by stopping heating of the formwork, and then a solidified sulfur, which is molded when the materials containing sulfur in the cavity is cooled and solidified, is taken out from the formwork.
C04B 28/36 - Compositions pour mortiers, béton ou pierre artificielle, contenant des liants inorganiques ou contenant le produit de réaction d'un liant inorganique et d'un liant organique, p. ex. contenant des ciments de polycarboxylates contenant du soufre, des sulfures ou de sélénium
A reforming device (10) for a fuel cell for reforming a raw fuel into a hydrogen-enriched reformed gas comprises a reforming section (12) for generating the reformed gas from the raw fuel and a steam supply means (100) for supplying steam into the reforming section (12). The steam supply means (100) includes a heat exchanger (108) for drying-out of water by exchanging heat with the reformed gas generated when the raw fuel is burned. The heat exchanger (108) has a cross sectional area larger than that of the pipe connected to the upstream side.
C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
H01M 8/06 - Combinaison d’éléments à combustible avec des moyens de production de réactifs ou pour le traitement de résidus
H01M 8/10 - Éléments à combustible avec électrolytes solides
A coating composition for hiding which comprises: a dispersion medium comprising 98-80 parts by mass of polybutene having a number-average molecular weight of 1,000-2,500 and 2-20 parts by mass of polyethylene having a density of 0.916-0.930 g/cm3 and an MFR of 4 or higher (the sum of both is 100 parts by mass); and 0.1-10 parts by mass of an inorganic pigment dispersed in the dispersion medium. The composition is excellent in the property of optically hiding the surface to be coated and the property of sealing the area to be coated. The coating surface has an excellent appearance. Whether the coating material is present in a coated area can be easily ascertained. This composition is intended to improve suitability for macroscopic/optical inspection steps in product assembly, etc. This coating composition for hiding is a highly functional composition which is superior to conventional compositions in heat resistance and applicability.
The present invention provides feedstock compositions for use of the production of an activated carbon for electric double layer capacitor electrodes or the production of needle coke, comprising a first heavy oil with an initial boiling point of 300° C. or higher, an asphalten content of 12 percent by mass or less, a saturate content of 50 percent by mass or more and a sulfur content of 0.3 percent by mass or less, produced as a residue resulting from vacuum-distillation of a petroleum-based oil and a second heavy oil with an initial boiling point of 150° C. or higher and a sulfur content of 0.5 percent by mass or less, produced by subjecting a hydrocarbon oil to fluidized catalytic cracking.
H01G 9/00 - Condensateurs électrolytiques, redresseurs électrolytiques, détecteurs électrolytiques, dispositifs de commutation électrolytiques, dispositifs électrolytiques photosensibles ou sensibles à la températureProcédés pour leur fabrication
C10C 3/00 - Traitement du brai, de l'asphalte, du bitume
C10G 11/00 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures
C10G 9/14 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures dans des tubes ou serpentins avec ou sans dispositifs auxiliaires, p. ex. "digesteurs", chambres de maturation, dispositifs d'expansion
H01B 1/04 - Conducteurs ou corps conducteurs caractérisés par les matériaux conducteurs utilisésEmploi de matériaux spécifiés comme conducteurs composés principalement soit de compositions à base de carbone-silicium, soit de carbone soit de silicium
H01B 1/24 - Matériau conducteur dispersé dans un matériau organique non conducteur le matériau conducteur comportant des compositions à base de carbone-silicium, du carbone ou du silicium
C10B 53/00 - Distillation destructive spécialement conçue pour des matières premières solides particulières ou sous forme spéciale
C10B 51/00 - Distillation destructive des matières carbonées solides par emploi combiné du chauffage direct et du chauffage indirect
Disclosed is an additive composition for lubricants, which can be prepared easily and is composed of a phosphorus-containing compound metal salt. The additive composition for lubricants has no adverse effect on rubber sealings such as swelling, while having excellent storage stability. Specifically disclosed is an additive composition for lubricants, which is characterized by blending, based on the total amount of the composition, 10-90% by mass of a metal salt of a phosphorus-containing compound represented by general formula (1) (wherein X4-X7 respectively represent an oxygen or sulfur atom, with at least one of X4-X7 being an oxygen atom; and R1-R3 respectively represent a hydrogen atom or a hydrocarbon group having 3-18 carbon atoms, with at least one of R1-R3 not being a hydrogen atom) into a lubricant base oil which is selected from mineral oils, synthetic oils and mixtures thereof, and has a kinematic viscosity at 100˚C of 0.5-3 mm2/s, a %CA of not more than 3, and a sulfur content of not more than 0.05% by mass. (1)
C10M 107/08 - Polymères d'hydrocarburesPolymères d'hydrocarbures modifiés par oxydation contenant du butène
C10M 107/10 - Polymères d'hydrocarburesPolymères d'hydrocarbures modifiés par oxydation contenant un monomère aliphatique comportant plus de 4 atomes de carbone
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
A metal working fluid composition is provided which has excellent lubricity under highly severe conditions and satisfies requirements including oil removability, low odorousness, safety, and lubricant stability. The metal working fluid composition is characterized by comprising at least one lube base oil selected from mineral oils, synthetic oils, and fats and at least one specific amino acid derivative, the content of the amino acid derivative therein being 0.01-3 mass% of the whole amount of the composition. The composition is applied to metal processing including cold rolling, warm and hot rolling, pressing, punching, ironing, squeezing, drawing, forging, cutting, and grinding.
C10N 30/00 - Propriétés physiques ou chimiques particulières améliorées par l'additif caractérisant la composition lubrifiante, p. ex. additifs multifonctionnels
Disclosed is a lubricating oil composition that has a high metal-to-metal friction coefficient, has excellent shudder preventive properties and is suitable for use as automatic transmission oils and/or continuously variable transmission oils. The lubricating oil composition is characterized by comprising a lubricating base oil and the following materials (A) and (B) incorproated in the lubricating base oil: (A) 0.005 to 0.1% by mass in terms of boron (BoA) and 0.01 to 0.4% by mass in terms of nitrogen, based on the total amount of the composition, of (a1) a boronated alkylsuccinimide and/or a boronated alkenylsuccinimide having a weight average molecular weight of 1,000 to 20,000 or a mixture of (a1) a boronated alkylsuccinimide and/or a boronated alkenylsuccinimide with (a2) a non-boronated alkylsuccinimide and/or a non-boronated alkenylsuccinimide; and (B) 0.01 to 0.5% by mass in terms of a metal (MeB), based on the total amount of the composition, of a metallic cleaning agent containing a straight-chain alkyl group having 6 to 60 carbon atoms derived from an ethylene oligomer and having a base number of 100 to 500 mg KOH/g.
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
C10M 159/24 - Mélanges réactionnels comportant un excès de base neutralisante, p. ex. produits appelés superbasiques ou hautement basiques contenant des radicaux sulfoniques
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 40/04 - Bains d'huileBoîtes de vitessesTransmissions automatiquesMécanismes de traction
49.
Fuel for homogeneous charge compression ignition engine
Provided are a composite material and the like, which can realize a highly efficient photoelectric conversion material and the like. One aspect of the invention is a dye-sensitized solar cell device (10) that is characterized by comprising: a first substrate (11), a first conductive layer (12) formed on top of the first substrate; a Pt catalyst layer formed on top of the first conductive layer; an electrolyte layer (13) formed on top of the Pt catalyst layer; a dye adsorption metal oxide layer (14), formed on top of the electrolyte layer, where 7, 7, 8, 8- tetracyanoquinodimethane is adsorbed by anatase-type titanium oxide; a second conductive layer (15) formed on top of the dye adsorption metal oxide layer; and a second substrate (16) formed on top of the second conductive layer. The structure makes it possible to obtain a highly efficient dye-sensitized solar cell device, which can efficiently convert light over a broad wavelength range.
C09B 23/00 - Colorants méthiniques ou polyméthiniques, p. ex. du type cyanine
C09B 57/00 - Autres colorants synthétiques de structure connue
C09B 67/02 - Préparations tinctoriales caractérisées par un aspect physique particulier, p. ex. tablettes, feuilles
H01L 31/04 - Dispositifs à semi-conducteurs sensibles aux rayons infrarouges, à la lumière, au rayonnement électromagnétique d'ondes plus courtes, ou au rayonnement corpusculaire, et spécialement adaptés, soit comme convertisseurs de l'énergie dudit rayonnement e; Procédés ou appareils spécialement adaptés à la fabrication ou au traitement de ces dispositifs ou de leurs parties constitutives; Leurs détails adaptés comme dispositifs de conversion photovoltaïque [PV]
51.
PRESSURE-SENSITIVE ADHESIVE COMPOSITION FOR TRAPPING SMALL ORGANISMS
As a pressure-sensitive adhesive composition for trapping small organisms, use is made of a composition comprising: (A) 70 to 98% by mass of liquid polybutene having a number-average molecular weight of 200 to 1200; (B) 1.0 to 8.0% by mass of high-pressure method polyethylene having a melt index of 0.04 to 35; (C) 1.0 to 8.0% by mass of butyl rubber having a Mooney viscosity ML1+8 (at 125oC) of 30 to 60; and (D) 5 to 29% by mass of an alicyclic hydrocarbon resin. Thus, a pressure-sensitive adhesive composition for trapping small organisms, which has a high pressure-sensitive adhesiveness and good coating properties to an adherend, and in which the starting materials of the pressure-sensitive adhesive composition can be easily obtained and the pressure-sensitive composition can be produced at a good workability, is provided.
C09J 123/22 - Copolymères de l'isobutèneCaoutchouc butyl
C09J 145/00 - Adhésifs à base d'homopolymères ou de copolymères de composés ne possédant pas de radicaux aliphatiques non saturés dans une chaîne latérale et contenant une ou plusieurs liaisons doubles carbone-carbone dans un système carbocyclique ou hétérocycliqueAdhésifs à base de dérivés de tels polymères
52.
ELLIPTICAL POLARIZER, METHOD FOR PRODUCING THE SAME AND IMAGE DISPLAY EMPLOYING ELLIPTICAL POLARIZER
Provided is an elliptical polarizer which can be made thin while exhibiting a high production efficiency and can reduce the extent that a display image becomes hard to be seen because of the direction of the polarization axis even when a screen is observed through an optical member having polarization effect, e.g. through sunglasses. The elliptical polarizer comprises a translucent protective film, an anisotropic optical element consisting of a liquid crystal layer, a polarization element, and a translucent protective film that are laminated in the order mentioned. Also provided is a method for producing the elliptical polarizer, and an image display in which the elliptical polarizer is arranged.
G02F 1/1335 - Association structurelle de cellules avec des dispositifs optiques, p. ex. des polariseurs ou des réflecteurs
G06F 9/00 - Dispositions pour la commande par programme, p. ex. unités de commande
H01L 51/50 - Dispositifs à l'état solide qui utilisent des matériaux organiques comme partie active, ou qui utilisent comme partie active une combinaison de matériaux organiques et d'autres matériaux; Procédés ou appareils spécialement adaptés à la fabrication ou au traitement de tels dispositifs ou de leurs parties constitutives spécialement adaptés pour l'émission de lumière, p.ex. diodes émettrices de lumière organiques (OLED) ou dispositifs émetteurs de lumière à base de polymères (PLED)
Disclosed is a lubricant composition containing a lubricant base oil having a kinematic viscosity at 100˚C of 1-10 mm2/s, a %Cp of not less than 70 and a %CA of not more than 2, which composition also contains, based on the total amount of the composition, 0.01-10% by mass of a first viscosity index improver which is composed of a poly(meth)acrylate having a weight average molecular weight of not more than 100,000 and 0.01-50% by mass of a second viscosity index improver which is composed of a polymer having a weight average molecular weight of not less than 100,000 and containing a structural unit represented by Formula (1) in an amount of 0.5-70% by mole. The lubricant composition has a kinematic viscosity at 100˚C of 4-12 mm2/s and a viscosity index of 140-300. [In Formula (1), R1 represents a hydrogen atom or a methyl group; and R2 represents a linear or branched hydrocarbon group having 16 or more carbon atoms or a linear or branched organic group containing an oxygen atom and/or a nitrogen group and having 16 or more carbon atoms.]
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 129/76 - Esters contenant des groupes hydroxyle ou carboxyle libres
C10M 135/18 - ThioacidesThiocyanatesLeurs dérivés comportant une liaison double carbone-soufre du type thiocarbamique, c.-à-d. contenant les groupes
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 149/02 - Composés macromoléculaires obtenus par des réactions faisant intervenir uniquement des liaisons non saturées carbone-carbone
A gas oil composition which contains a low environmental load type gas oil base prepared by using, as the raw material, either an animal or vegetable oil or fat or hydrocarbons containing triglycerides resulting from an animal or vegetable oil or fat and which is excellent in life cycle CO2 emission characteristics, oxidation resistance and influence on members, specifically, a gas oil composition which is produced by blending 5 to 90vol% of a low environmental load type gas oil base prepared by subjecting an oil to be treated, which is obtained by mixing an animal or vegetable oil or fat and/or a component resulting from an animal or vegetable oil or fat with a sulfur-containing hydrocarbon compound in such amounts as to give a sulfur content of 1ppm to 2% by mass, to hydrotreating in the presence of hydrogen under prescribed conditions in two stages with 95 to 10vol% of a hydrotreated oil prepared from crude oil or the like and adding a predetermined amount of a low-temperature fluidity improver to the obtained blend and of which the 90% distillation temperature, flash point, cetane number, cold filter plugging point, sulfur content, oxygen content, triglyceride content, fatty acid alkyl ester content, total acid value, and acid value increase after oxidation resistance test fall within specific ranges respectively.
C10L 1/08 - Combustibles carbonés liquides à base essentielle de mélanges d'hydrocarbures pour allumage par compression
C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
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 45/08 - 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
C10G 65/02 - Traitement des huiles d'hydrocarbures, uniquement par plusieurs procédés d'hydrotraitement uniquement par plusieurs étapes en série
The present invention provides a process for producing aromatic hydrocarbons at a sufficiently high yield, from a light hydrocarbon containing mainly hydrocarbons having 7 or fewer carbon atoms. The process of the present invention comprises bringing a feedstock containing mainly light hydrocarbons having 2 to 7 carbon atoms into contact with a catalyst composition comprising at least a gallium-containing crystalline aluminosilicate wherein a reaction step for converting the feedstock to aromatic hydrocarbons comprises at least two or more reaction layers formed of the catalyst composition, arranged in series and heating means arranged either between or in the reaction layers, the amount of the catalyst in the first stage reaction layer is 30 percent by volume or less of the total catalyst volume, and/or the yield of the aromatics in the product outflowing from the first reaction layer is from 0.5 to 30 percent by mass.
C07C 2/54 - Préparation d'hydrocarbures à partir d'hydrocarbures contenant un plus petit nombre d'atomes de carbone par addition d'hydrocarbures non saturés à des hydrocarbures saturés, ou à des hydrocarbures contenant un cycle aromatique à six chaînons ne comportant pas d'autre insaturation que celle du cycle aromatique
The hydrorefining method of the invention is characterized by contacting, in the presence of hydrogen, a fuel stock comprising normal paraffins and oxygen-containing compounds, with a hydrorefining catalyst comprising a support containing USY zeolite and at least one solid acid selected from among silica-alumina, alumina-boria, silica-zirconia, silica-magnesia and silica-titania, and at least one metal selected from among metals of Group VIb and metals of Group VIII of the Periodic Table supported on the support.
C10G 45/12 - 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 des alumino-silicates cristallins, p. ex. des tamis moléculaires
C10G 45/64 - Raffinage des huiles d'hydrocarbures au moyen d'hydrogène ou de composés donneurs d'hydrogène pour changer la structure du squelette de certains hydrocarbures sans craquer les autres hydrocarbures présents, p. ex. pour abaisser le point d'écoulementHydrocraquage sélectif des paraffines normales caractérisé par le catalyseur utilisé contenant des alumino-silicates cristallins, p. ex. des tamis moléculaires
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
B01J 21/06 - Silicium, titane, zirconium ou hafniumLeurs oxydes ou hydroxydes
C10G 45/62 - Raffinage des huiles d'hydrocarbures au moyen d'hydrogène ou de composés donneurs d'hydrogène pour changer la structure du squelette de certains hydrocarbures sans craquer les autres hydrocarbures présents, p. ex. pour abaisser le point d'écoulementHydrocraquage sélectif des paraffines normales caractérisé par le catalyseur utilisé contenant des métaux du groupe du platine ou leur composés
C10G 45/10 - 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 des métaux du groupe du platine ou leurs composés
B01J 21/02 - Bore ou aluminiumLeurs oxydes ou hydroxydes
B01J 35/02 - Catalyseurs caractérisés par leur forme ou leurs propriétés physiques, en général solides
57.
SHEET MATERIAL, SHEET MATERIAL FOR ELECTROMAGNETIC WAVE SHIELD, WALL PAPER, AND ELECTROMAGNETIC WAVE-SHIELDING TAPE FOR ELECTRIC WIRE
Disclosed is a sheet material which is lightweight and thin and which has a large quantity of a metal adhered thereon. The sheet material comprises a base cloth (2) comprising at least one fiber-arranged layer (12A, 12B, 12C, 12D) on which unbroken long fibers are stretched and arranged almost linearly in one direction, wherein at least one surface of the base cloth (2) is plated.
H05K 9/00 - Blindage d'appareils ou de composants contre les champs électriques ou magnétiques
B32B 15/14 - Produits stratifiés composés essentiellement de métal adjacent à une couche fibreuse ou filamenteuse
D04H 3/16 - Non-tissés formés uniquement ou principalement de fils ou de matériaux filamenteux similaires de bonne longueur caractérisés par la méthode de renforcement ou de consolidation avec liages produits par soudage entre fils thermoplastiques ou filaments avec liages entre filaments thermoplastiques produits en relation avec la formation des filaments, p. ex. suivant immédiatement l'extrusion
58.
CYLINDER LUBRICATING OIL COMPOSITION FOR CROSSHEAD TYPE DIESEL ENGINE
A cylinder lubricating oil composition for diesel engines of the crosshead type is provided which is excellent in heat resistance and anti-seizing properties. The composition comprises a lube base oil and a phenate type metallic detergent (A) having an alkylphenol sulfide metal salt having five or more alkylphenol structures in the same molecule. This composition is useful especially in a two-stroke cycle diesel engine operated under such conditions that any or all of the following are satisfied: the bore size is 70 cm or larger; the engine is an ultra-long-stroke engine with a mean piston speed of 8 m/s or higher; the combustion pressure is 1.8 MPa or higher in terms of brake mean effective pressure (BMEP); and the cylinder wall temperature reaches 250°C or higher.
C10M 135/30 - ThiolsSulfuresPolysulfures contenant des atomes de soufre liés à un atome de carbone d'un cycle aromatique à six chaînons contenant des groupes hydroxyleLeurs dérivés
C10M 159/22 - Mélanges réactionnels comportant un excès de base neutralisante, p. ex. produits appelés superbasiques ou hautement basiques contenant des radicaux phénol
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 159/20 - Mélanges réactionnels comportant un excès de base neutralisante, p. ex. produits appelés superbasiques ou hautement basiques
C10M 159/24 - Mélanges réactionnels comportant un excès de base neutralisante, p. ex. produits appelés superbasiques ou hautement basiques contenant des radicaux sulfoniques
C10N 30/02 - Point d'écoulementIndice de viscosité
C10N 30/06 - OnctuositéRésistance du filmAnti-usureRésistance aux pressions extrêmes
Japan Oil, Gas and Metals National Corporation (Japon)
INPEX CORPORATION (Japon)
NIPPON OIL CORPORATION (Japon)
Japan Petroleum Exploration Co., Ltd. (Japon)
COSMO OIL CO., LTD. (Japon)
NIPPON STEEL ENGINEERING CO., LTD. (Japon)
Inventeur(s)
Nakashizu, Shigenori
Miyata, Yutaka
Sato, Kazuhito
Abrégé
Disclosed is a method for the management of a wax fraction storage tank, which enables the management of a tank for storing a wax fraction produced by Fischer-Tropsch synthesis until the wax fraction is subjected to hydrogenolysis. The method is characterized by keeping the temperature in the tank at a temperature ranging from 90 to 130˚C and maintaining the inside of the tank in an inert gas atmosphere.
Provided is a method for starting a fuel cell system which can surely prevent oxidization/degradation of an anode by performing reformation from an early stage. The method is used for starting a fuel cell system having a reformer for reforming a carbon hydride-based fuel and a high-temperature type fuel cell. [A] M flow rates Fj are preset as a fuel flow rate, wherein M is an integer not smaller than 2 and 0 ឬ F1, Fj ឬ Fj+1 (wherein j is an integer not smaller than 1 and not greater than M-1), and FM is a fuel flow rate upon start completion. [B] The temperature of a reforming catalyst layer is increased while measuring the temperature of the reforming catalysis layer. [C] A fuel flow rate FR capable of reformation is calculated according to the measured temperature. [D] F = 0 if FR ឬ F1 and F = Fj if Fj ≤ FR ឬ Fj+1 (wherein j is an integer not smaller than 1 and not greater than M-1), and F = FM if FM ≤ FR. [E] If F exceeds the current value of the fuel flow rate, the fuel of the flow rate F is supplied to the catalyst layer and the reformed gas obtained by reformation is supplied to a fuel cell anode. The steps [C] to [E] are repeated until the fuel supply amount to the catalyst layer reaches FM. The fuel cell system may be appropriately applied to the method.
C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
H01M 8/04 - Dispositions auxiliaires, p. ex. pour la commande de la pression ou pour la circulation des fluides
H01M 8/06 - Combinaison d’éléments à combustible avec des moyens de production de réactifs ou pour le traitement de résidus
H01M 8/12 - Éléments à combustible avec électrolytes solides fonctionnant à haute température, p. ex. avec un électrolyte en ZrO2 stabilisé
Disclosed is a process for producing a hydrocarbon oil, which comprises the following steps: a washing step of contacting and mixing a raw material oil comprising an oil-and-fat component derived from an animal or plant with an acidic aqueous solution, thereby washing the raw material oil until the total content of an alkali metal component, an alkali earth metal component and a transition metal component in the raw material oil becomes 15 ppm by mass or less; and a hydrogenation/deoxidation step of contacting the washed raw material oil produced in the washing step with a hydrogenation catalyst under a pressurized hydrogen gas to produce the hydrocarbon oil. According to the process, the content of oxygen can be reduced satisfactorily in the production of a hydrocarbon oil by the hydrogenation/deoxidation of a raw material oil comprising an oil-and-fat component derived from an animal or plant, and it becomes possible to efficiently and stably produce a hydrocarbon oil having the stability against oxidation at a practically applicable level for use as a fuel oil. Also disclosed is a light oil for a diesel engine, which comprises a hydrocarbon oil having the above-mentioned properties as a base oil.
Disclosed is a lubricant oil composition. The lubricant oil composition comprises: a lubricant base oil containing a lubricant base oil component in an amount of 10 to 100 mass% relative to the total amount of the base oil; and a poly(meth)acrylate-type viscosity index improver having therein a constituent unit represented by the general formula (1) at a ratio of 0.5 to 70 mol%, wherein the lubricant base oil component has a urea adduct value of 4 mass% or less, a kinematic viscosity of 25 mm2/s or less at 40°C, and a viscosity index of 120 or more. The lubricant oil composition has a kinematic viscosity of 4 to 12 mm2/s at 100°C and a viscosity index of 140 to 300. (1) wherein R1 represents a hydrogen or a methyl group; and R2 represents a linear or branched hydrocarbon group having 16 or more carbon atoms.
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 40/04 - Bains d'huileBoîtes de vitessesTransmissions automatiquesMécanismes de traction
A method for transporting a fluid catalytic cracking catalyst which can greatly reduce friction at a bend of a transportation piping when a fluid catalytic cracking catalyst (FCC catalyst) is transported therein in a dry state. The method for transporting a FCC catalyst comprises a step for transporting a FCC catalyst on a gas by feeding the gas in the transportation piping having a bend. The transportation piping is formed of a metal material and the bend consists of a first portion in the shape of a straight pipe, and a second portion in the shape of a straight pipe connected with the first portion. In the transportation step, the superficial air velocity of the gas is set at 5-20 m/s, the direction of the gas flowing through the second portion makes an angle of 45°-90° to the direction of the gas flowing through the first portion, and the density of the FCC catalyst is set at 5-10 g/L or 15-20 g/L.
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"
64.
RAW MATERIAL CHARCOAL COMPOSITION FOR NEGATIVE ELECTRODE MATERIAL OF LITHIUM ION SECONDARY BATTERY AND METHOD FOR PRODUCING THE SAME
Disclosed is a raw material charcoal composition which is used as a raw material for a negative electrode material of lithium ion secondary batteries. This raw material charcoal composition is characterized in that when the composition is graphitized in an inert gas atmosphere at 2,800˚C, the ratio between the crystallite size Lc(002) and the lattice constant co(002) of the (002) plane as determined by x-ray diffraction analysis, namely Lc(002)/co(002), is not more than 180, and the ratio between the crystallite size La(110) and the lattice constant ao(110) of the (110) plane as determined by x-ray diffraction analysis, namely La(110)/ao(110), is not more than 1,500.
C10B 57/04 - Autres procédés de carbonisation ou de cokéfactionCaractéristiques générales des procédés de distillation destructive utilisant des charges de composition spéciale
C10G 9/00 - Craquage thermique non catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures
65.
REFRIGERATOR OIL AND REFRIGERATING MACHINE WORKING FLUID COMPOSITION COMPRISING A POLYALKYLENE GLYCOL AND A FLUOROPROPENE REFRIGERANT
The refrigerator oil of the invention comprises an ester of a polyhydric alcohol and a fatty acid with a content of a C5-C9 fatty acid of 50-100 % by mole, a content of a C5-C9 branched fatty acid of at least 30 % by mole and a content of a C5 or lower straight-chain fatty acid of not greater than 40 % by mole, and it is used with a fluoropropene refrigerant and/or trifluoroiodomethane refrigerant. The working fluid composition for a refrigerating machine according to the invention comprises the ester and a fluoropropene refrigerant and/or trifluoroiodomethane refrigerant.
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
Disclosed is a refrigerator oil characterized by containing an ester of a polyhydric alcohol and a fatty acid containing 50-100% by mole of a fatty acid having 5-9 carbon atoms, not less than 30% by mole of a branched fatty acid having 5-9 carbon atoms, and not more than 40% by mole of a straight chain fatty acid having 5 or less carbon atoms. This refrigerator oil is also characterized by being used together with a fluoropropene refrigerant and/or a trifluoroiodomethane refrigerant. Also disclosed is a working fluid composition for refrigerating machines which is characterized by containing the above-described ester, and a fluoropropene refrigerant and/or a trifluoroiodomethane refrigerant.
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
67.
APPARATUS FOR PRODUCING REFORMING RAW MATERIAL AND FUEL CELL SYSTEM
Disclosed is an apparatus (4) for producing a reforming raw material for a fuel cell system (1), wherein a desulfurizer (6) for removing a sulfur component from a liquid fuel is disposed within a water vaporizer (5), which heats water (L) in a liquid phase state, through heat exchange with an off gas discharged from an SOFC stack (3), to vaporize the water(L), so that the desulfurizer (6) is immersed in the water (L) in the liquid phase state. According to this constitution, a desulfurizing agent within the desulfurizer (6) is heated to a temperature around the boiling point of the water (L) in the liquid phase state by heat exchange with the water (L) in the liquid phase state reservoired in the water vaporizer (5). In this case, the pressure of water (V) in a gas phase state within the water vaporizer (5) is regulated through an orifice (7) provided in a water vapor supply line (18). Accordingly, the boiling point of the water within the water vaporizer is regulated to a predetermined temperature. Thus, the desulfurizing agent within the desulfurizer (6) can be easily and reliably maintained at a proper temperature.
C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
H01M 8/04 - Dispositions auxiliaires, p. ex. pour la commande de la pression ou pour la circulation des fluides
H01M 8/06 - Combinaison d’éléments à combustible avec des moyens de production de réactifs ou pour le traitement de résidus
H01M 8/12 - Éléments à combustible avec électrolytes solides fonctionnant à haute température, p. ex. avec un électrolyte en ZrO2 stabilisé
A multifunctional, high-performance hydrocarbon composition is demanded. Concretely, a metalworking oil composition having high workability even under a severer lubricating condition while resisting to high productivity, and further capable of suppressing deterioration of working environments or degradation of quality of a product without rise of lubricant cost, a metalworking oil composition for minimal quantitative lubrication system, which is excellent in characteristics as a water-insoluble lubricant for nonferrous metalworking and also in characteristics as a lubricant for cutting/grinding by minimal quantitative lubrication method, and can attain improvement in working efficiency and a further extended tool life, an electric discharge machining oil improved in working environments such as odor or skin roughness and further improved in processing rate, particularly processing rate in high-level finish, a rust preventing oil composition improved in resin compatibility, and a detergent excellent in adaptability with organic material are demanded.
3, and including a n-paraffin content of 10 to 90% by mass, an aromatic content of 0 to 3% by volume, and a naphthene content of 0 to 20% by volume, a metalworking oil including the above-mentioned base oil and ester oil, and electric discharge machining oil, rust preventing oil, and a detergent composition including the above-mentioned base oil are provided.
C10M 107/02 - Polymères d'hydrocarburesPolymères d'hydrocarbures modifiés par oxydation
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
C23G 5/024 - Nettoyage ou dégraissage des matériaux métalliques par d'autres méthodesAppareils pour le nettoyage ou le dégraissage de matériaux métalliques au moyen de solvants organiques au moyen de solvants organiques contenant des hydrocarbures
69.
Solid phosphoric acid catalyst and methods of olefin dimerization reaction with the same
5) derived from the phosphoric acid. A method of olefin dimerization comprises bringing an olefin-containing feed material containing water in an amount of 10-1000 mass ppm into contact with the catalyst to initiate the reaction.
Disclosed is a method for producing an optical film wherein a homeotropic alignment liquid crystal layer can be easily formed by using an alignment film which is composed of a polyvinyl alcohol having a saponification degree of 75-90%. In this method for producing an optical film, the homeotropic alignment liquid crystal layer can be easily transferred to another member.
A process comprising: a first step in which catalytically cracked gasoline is hydrodesulfurized so that olefins contained in the catalytically cracked gasoline come to have a degree of hydrogenation of 25 mol% or lower and the catalytically cracked gasoline comes to have a total sulfur content not higher than 20 mass ppm of the product oil to be yielded, a content of sulfur derived from thiophene compounds and benzothiophene compounds not higher than 5 mass ppm of the product oil, and a content of sulfur derived from thiacyclopentane compounds not higher than 0.1 mass ppm of the product oil; and a second step in which the product oil obtained in the first step is further hydrodesulfurized so that the sum of the degree of olefin hydrogenation in the first step and the degree of olefin hydrogenation in this step is 30 mol% or less and the product oil comes to have a total sulfur content not higher than 10 mass ppm of the product oil and a content of sulfur derived from thiol compounds not higher than 5 mass ppm of the product oil.
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
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 45/08 - 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
C10L 1/06 - Combustibles carbonés liquides à base essentielle de mélanges d'hydrocarbures pour allumage par bougie
72.
ARTIFICIAL GRAPHITE FOR NEGATIVE ELECTRODE OF LITHIUM ION SECONDARY BATTERY, AND METHOD FOR PRODUCTION THEREOF
Disclosed is an artificial graphite for a negative electrode of a lithium ion secondary battery, which is characterized by having a crystallite size (Lc) in the c-axis direction of 60 to 120 nm as measured by X-ray diffraction and also having a crystallite size (Lc) of 150 nm or greater after being graphitized at a temperature of 3000°C in an inert gas atmosphere.
An antiblocking-agent masterbatch obtained by compounding 100 parts by mass of a polyolefin resin with 1-40 parts by mass of fine polymer particles obtained by: passing two or more fluids including a liquid medium, a monomer, and a polymerization initiator successively through nets which are disposed at given intervals in a cylindrical passage and have a plane crossing the direction of the passage to thereby obtain an emulsion comprising the liquid medium and, dispersed therein, droplets comprising the monomer and the polymerization initiator; and heating this emulsion to polymerize the monomer. Also provided is a process for producing the masterbatch. When the fine polymer particles are incorporated into a polyolefin resin to produce the masterbatch for polyolefin resin films, gum generation can be prevented.
C08L 23/00 - 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
74.
METHOD AND APPARATUS FOR REGULATING PARTICLE DIAMETER AND PARTICLE DIAMETER DISTRIBUTION OF EMULSIFIED PARTICLES IN EMULSION
A method of regulating the particle diameter and particle diameter distribution of emulsified particles in emulsion production which comprises successively passing two or more liquids which are substantially insoluble in each other through 50-200, excluding 50, sieve materials disposed in a cylindrical channel at intervals of 5-200 mm, the sieve materials corresponding to a 35- to 4,000-mesh sieve according to ASTM, and having a side crossing the direction of the channel to thereby attain the regulation. Also provided is an emulsifier as an apparatus for the method. The emulsifier is characterized by comprising: a liquid feed pump which feeds two or more liquids which are substantially insoluble in each other; and a cylindrical channel to which the two or more liquids are sent by the liquid feed pump, the cylindrical channel having a given number of sieve materials which have been disposed therein at a given interval and which each has a side crossing the direction of the channel.
B01F 3/08 - Mélange, p.ex. dispersion, émulsion, selon les phases à mélanger de liquides avec des liquides; Emulsion
B01F 5/06 - Mélangeurs dans lesquels les composants du mélange sont pressés ensemble au travers de fentes, d'orifices, ou de tamis
B01J 13/00 - Chimie des colloïdes, p. ex. production de substances colloïdales ou de leurs solutions, non prévue ailleursFabrication de microcapsules ou de microbilles
B01J 13/02 - Fabrication de microcapsules ou de microbilles
C08F 2/24 - Polymérisation en émulsion utilisant des agents émulsifiants
Japan Oil, Gas and Metals National Corporation (Japon)
INPEX CORPORATION (Japon)
NIPPON OIL CORPORATION (Japon)
Japan Petroleum Exploration Co., Ltd. (Japon)
COSMO OIL CO., LTD. (Japon)
NIPPON STEEL ENGINEERING CO., LTD. (Japon)
Inventeur(s)
Tanaka, Yuichi
Abrégé
A process for producing a diesel fuel, characterized by fractionating in a first rectifier a synthetic oil obtained by the Fischer-Tropsch synthesis method into at least two fractions, i.e., an intermediate fraction and a wax fraction containing a wax ingredient heavier than the intermediate fraction, bringing the intermediate fraction into contact with a hydroisomerization catalyst to hydroisomerize the fraction and thereby obtain an isomerized intermediate fraction, bringing the wax fraction into contact with a hydrocracking catalyst to hydrocrack the fraction and thereby obtain a cracked wax fraction, fractionating the isomerized intermediate fraction and the cracked wax fraction in a second rectifier to fractionate these fractions into at least two fractions comprising a kerosine fraction and a gas oil fraction, and mixing the at least two fractions in a given proportion to obtain a diesel fuel having a dynamic viscosity as measured at 30°C of 2.5 mm2/s or higher and a pour point of -7.5°C or lower.
C10G 65/14 - Traitement des huiles d'hydrocarbures, uniquement par plusieurs procédés d'hydrotraitement uniquement par plusieurs étapes en parallèle
C10G 2/00 - Production de mélanges liquides d'hydrocarbures de composition non définie à partir d'oxydes de carbone
C10G 45/58 - Raffinage des huiles d'hydrocarbures au moyen d'hydrogène ou de composés donneurs d'hydrogène pour changer la structure du squelette de certains hydrocarbures sans craquer les autres hydrocarbures présents, p. ex. pour abaisser le point d'écoulementHydrocraquage sélectif des paraffines normales
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
C10L 1/08 - Combustibles carbonés liquides à base essentielle de mélanges d'hydrocarbures pour allumage par compression
76.
PROCESS FOR PRODUCING DIESEL FUEL BASE AND DIESEL FUEL BASE OBTAINED
Japan Oil, Gas and Metals National Corporation (Japon)
INPEX CORPORATION (Japon)
NIPPON OIL CORPORATION (Japon)
Japan Petroleum Exploration Co., Ltd. (Japon)
COSMO OIL CO., LTD. (Japon)
NIPPON STEEL ENGINEERING CO., LTD. (Japon)
Inventeur(s)
Tanaka, Yuichi
Sato, Kazuhito
Abrégé
A process for producing a diesel fuel base having improved low-temperature flowability which comprises: fractionating an FT synthetic oil in a first rectifier into a first intermediate fraction and a wax fraction heavier than the first intermediate fraction; hydroisomerizing the first intermediate fraction to obtain an isomerized intermediate fraction; hydrocracking the wax fraction to obtain a cracked wax fraction; and then subjecting a mixture of the resultant isomerized intermediate fraction and cracked wax fraction to fractional distillation in a second rectifier to obtain a diesel fuel base as a second intermediate fraction. Rectification conditions in the first rectifier and/or second rectifier are regulated to selectively reduce the content of n-paraffins having 19 or more carbon atoms in the heavy components of the diesel fuel base. Also provided is a diesel fuel base obtained by the process.
C10G 65/14 - Traitement des huiles d'hydrocarbures, uniquement par plusieurs procédés d'hydrotraitement uniquement par plusieurs étapes en parallèle
C10G 2/00 - Production de mélanges liquides d'hydrocarbures de composition non définie à partir d'oxydes de carbone
C10G 45/58 - Raffinage des huiles d'hydrocarbures au moyen d'hydrogène ou de composés donneurs d'hydrogène pour changer la structure du squelette de certains hydrocarbures sans craquer les autres hydrocarbures présents, p. ex. pour abaisser le point d'écoulementHydrocraquage sélectif des paraffines normales
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
C10L 1/08 - Combustibles carbonés liquides à base essentielle de mélanges d'hydrocarbures pour allumage par compression
Japan Oil, Gas and Metals National Corporation (Japon)
INPEX CORPORATION (Japon)
NIPPON OIL CORPORATION (Japon)
Japan Petroleum Exploration Co., Ltd. (Japon)
COSMO OIL CO., LTD. (Japon)
NIPPON STEEL ENGINEERING CO., LTD. (Japon)
Inventeur(s)
Tanaka, Yuichi
Abrégé
A process for the production of naphtha which comprises hydrotreating a naphtha fraction separated from synthetic oil obtained by Fischer-Tropsch process, namely, FT synthetic oil, wherein the quantity of olefins in a hydrotreating unit is reduced by recycling a hydrotreated naphtha component in a controlled amount to the unit, whereby heat generation in the unit is inhibited to attain stable operation of the unit; and a process for the production of naphtha wherein the quantity of olefins in a hydrorefining unit is reduced by controlling the temperature at which a naphtha fraction is cut from FT synthetic oil through fractional distillation to attain stable operation of the unit.
C10G 45/02 - 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
78.
BUBBLING TOWER HYDROCARBON REACTOR AND METHOD OF DETECTING SLURRY SURFACE LEVEL
Japan Oil, Gas and Metals National Corporation (Japon)
INPEX CORPORATION (Japon)
NIPPON OIL CORPORATION (Japon)
Japan Petroleum Exploration Co., Ltd. (Japon)
COSMO OIL CO., LTD. (Japon)
Inventeur(s)
Onishi, Yasuhiro
Kato, Yuzuru
Yamada, Eiichi
Abrégé
A bubbling tower hydrocarbon reactor in which a hydrocarbon compound is synthesized by the chemical reaction of synthesis gas, which comprises hydrogen and carbon monoxide as main components, with a slurry obtained by suspending solid catalyst particles in a liquid. The bubbling tower hydrocarbon reactor comprises: a reactor main body which holds the slurry therein; a synthesis-gas supply unit which supplies the synthesis gas to the slurry; a pressure sensor which has been disposed above the surface of the slurry and measures the pressure of the synthesis gas above the liquid surface; other pressure sensors, which have been disposed below the surface of the slurry and measure the pressure of the slurry; and a level detector which detects the position of the surface of the slurry based on the results of measurements with the pressure sensors. The other pressure sensors have been disposed apart from each other in the axis direction for the reactor main body.
C10G 2/00 - Production de mélanges liquides d'hydrocarbures de composition non définie à partir d'oxydes de carbone
B01J 8/22 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées l'agent fluidisant étant un liquide du gaz étant introduit dans le liquide
G01F 23/14 - Indication ou mesure du niveau des liquides ou des matériaux solides fluents, p. ex. indication en fonction du volume ou indication au moyen d'un signal d'alarme par mesurage de la pression
Japan Oil, Gas and Metals National Corporation (Japon)
INPEX CORPORATION (Japon)
NIPPON OIL CORPORATION (Japon)
Japan Petroleum Exploration Co., Ltd. (Japon)
COSMO OIL CO., LTD. (Japon)
Inventeur(s)
Onishi, Yasuhiro
Abrégé
Disclosed is a synthesis reaction system for synthesizing a hydrocarbon compound through the chemical reaction between a synthetic gas mainly composed of hydrogen and carbon monoxide with a slurry comprising a solid catalyst particle suspended in a liquid and then collecting the hydrocarbon compound from the slurry. The synthesis reaction system comprises: a reactor main body for containing the slurry therein; a separator for separating the hydrocarbon compound contained in the slurry from the slurry; a first flow path for allowing the slurry containing the hydrocarbon compound to flow from the reactor main body into the separator; a second flow path for allowing the slurry to flow from the separator into the reactor main body; and a fluid supply nozzle for supplying the fluid to at least any one of the separator, the first flow path and the second flow path.
C10G 2/00 - Production de mélanges liquides d'hydrocarbures de composition non définie à partir d'oxydes de carbone
B01J 8/22 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées l'agent fluidisant étant un liquide du gaz étant introduit dans le liquide
80.
BUBBLE-COLUMN-TYPE HYDROCARBON SYNTHESIS REACTOR, AND HYDROCARBON SYNTHESIS REACTION SYSTEM HAVING THE REACTOR
Japan Oil, Gas and Metals National Corporation (Japon)
INPEX CORPORATION (Japon)
NIPPON OIL CORPORATION (Japon)
Japan Petroleum Exploration Co., Ltd. (Japon)
COSMO OIL CO., LTD. (Japon)
Inventeur(s)
Onishi, Yasuhiro
Kato, Yuzuru
Yamada, Eiichi
Abrégé
Disclosed is a bubble-column-type hydrocarbon synthesis reactor for synthesizing a hydrocarbon compound through the chemical reaction between a synthetic gas mainly composed of hydrogen and carbon monoxide with a slurry comprising a solid catalyst particle suspended in a liquid. The bubble-column-type hydrocarbon synthesis reactor comprises: a reactor main body for containing the slurry therein; a synthetic gas supply unit for supplying the synthetic gas to the slurry; and an introduction unit for introducing a cooling fluid having a temperature lower than that of the slurry into the interior of the reactor main body.
C10G 2/00 - Production de mélanges liquides d'hydrocarbures de composition non définie à partir d'oxydes de carbone
B01J 8/22 - Procédés chimiques ou physiques en général, conduits en présence de fluides et de particules solidesAppareillage pour de tels procédés les particules étant fluidisées l'agent fluidisant étant un liquide du gaz étant introduit dans le liquide
81.
METHOD FOR EFFECTIVELY UTILIZING HEAT IN TUBULAR REFORMER
Japan Oil, Gas and Metals National Corporation (Japon)
INPEX CORPORATION (Japon)
NIPPON OIL CORPORATION (Japon)
Japan Petroleum Exploration Co., Ltd. (Japon)
COSMO OIL CO., LTD. (Japon)
NIPPON STEEL ENGINEERING CO., LTD. (Japon)
CHIYODA CORPORATION (Japon)
Inventeur(s)
Yagi, Fuyuki
Kawazuishi, Kenichi
Abrégé
This invention provides a method for effectively utilizing heat in a tubular reformer which, in using a steam reforming method or a carbon dioxide reforming method in a reforming step in a GTL process for producing various hydrocarbon oils from natural gas, can improve the thermal utilization efficiency. The method comprises a synthesis gas producing step of passing natural gas and steam and/or carbon dioxide gas through a tubular reformer packed with a reforming catalyst to convert them to a synthesis gas, a Fischer-Tropsh oil producing step of subjecting the produced synthesis gas to a Fischer-Tropsh reaction to produce a Fischer-Tropsh oil, and an upgrading step of hydrogenating and distilling the produced Fischer-Tropsh oil to produce various hydrocarbon oils. Excess heat produced in the synthesis gas production process is recovered, and the recovered heat is used as heat for hydrogenation and/or distillation in the upgrading step.
C10G 2/00 - Production de mélanges liquides d'hydrocarbures de composition non définie à partir d'oxydes de carbone
C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
C10G 45/00 - Raffinage des huiles d'hydrocarbures au moyen d'hydrogène ou de composés donneurs d'hydrogène
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
82.
AMORPHOUS CARBON MATERIAL FOR NEGATIVE ELECTRODE OF LITHIUM ION SECONDARY BATTERY AND METHOD FOR PRODUCING THE SAME
Disclosed is an amorphous carbon material for negative electrodes of lithium ion secondary batteries, which is characterized by having a true density of 1.800-2.165 g/cm3. This amorphous carbon material for negative electrodes of lithium ion secondary batteries is also characterized in that the true density becomes not less than 2.255 g/cm3 when it is graphitized at a temperature of 3000˚C in an inert gas atmosphere.
Provided is a wiping cloth capable of efficiently removing micro-dusts. The wiping cloth (1) comprises a fiber layer laminate (11) constituted by laminating fiber layers (12A-12D). The fiber layer (12A) forming a wiping surface is formed in a fiber-arranged layer in which continuous long fibers are substantially linearly arranged in one direction.
D04H 3/04 - Non-tissés formés uniquement ou principalement de fils ou de matériaux filamenteux similaires de bonne longueur caractérisés par la méthode de formation des voiles ou couches, p. ex. par la réorientation des fils ou filaments avec parcours rectiligne, p. ex. se croisant à angles droits
D04H 3/16 - Non-tissés formés uniquement ou principalement de fils ou de matériaux filamenteux similaires de bonne longueur caractérisés par la méthode de renforcement ou de consolidation avec liages produits par soudage entre fils thermoplastiques ou filaments avec liages entre filaments thermoplastiques produits en relation avec la formation des filaments, p. ex. suivant immédiatement l'extrusion
84.
AIR PURIFICATION FILTER AND AIR PURIFICATION FILTER ASSEMBLY
An air purification filter that is used together with another filter, prevents scatter of cut pieces of fibers separated from the another filter, and effectively reinforces the another filter. The air purification filter (2) has a fiber array layer body formed by layering fiber array layers over each other, where, in each of the fiber array layers, continuous long fibers are substantially linearly arranged aligned in one direction. The air purification filter (2) is adapted to be placed closer to a space (10) to be air conditioned than the another air purification filter (1) placed at an air outlet of an air conditioning facility. In the fiber array layers, some fiber array layers and the remaining fiber array layers are layered over each other such that the directions of extension of the fibers of the some and remaining fiber array layers are different.
F24F 7/10 - Ventilation avec réseau de gaines à circulation d'air forcée, p. ex. par un ventilateur avec amenée ou évacuation de l'air au travers de parois, planchers ou plafonds perforés
B01D 39/14 - Autres substances filtrantes autoportantes
B01D 39/16 - Autres substances filtrantes autoportantes en substance organique, p. ex. fibres synthétiques
B01D 46/10 - Séparateurs de particules utilisant des plaques, des feuilles ou des tampons filtrants à surface plane, p. ex. appareils de précipitation de poussières
B03C 3/28 - Installations fonctionnant sans alimentation en électricité, p. ex. utilisant des "électrets"
D04H 3/04 - Non-tissés formés uniquement ou principalement de fils ou de matériaux filamenteux similaires de bonne longueur caractérisés par la méthode de formation des voiles ou couches, p. ex. par la réorientation des fils ou filaments avec parcours rectiligne, p. ex. se croisant à angles droits
D04H 3/14 - Non-tissés formés uniquement ou principalement de fils ou de matériaux filamenteux similaires de bonne longueur caractérisés par la méthode de renforcement ou de consolidation avec liages produits par soudage entre fils thermoplastiques ou filaments
TUNGSTEN-CONTAINING MESOPOROUS SILICA THIN FILM, HIGHLY HYDROPHILIC MATERIAL CONTAINING THE SAME, AND METHOD FOR PRODUCING TUNGSTEN-CONTAINING MESOPOROUS SILICA THIN FILM
Disclosed is a tungsten-containing mesoporous silica thin film, which is a mesoporous silica thin film made from a solution containing a silica precursor and a water-soluble tungsten compound. This tungsten-containing mesoporous silica thin film has a molar ratio of the tungsten content relative to the silicon content, namely W/Si of 0.001-0.04, a film thickness of 0.1-5 μm and an average pore diameter of not more than 20 nm.
A fuel cell system (1) having a PEFC stack (4) in an internal space (S) of a housing (6) has a sheath heater (13) provided in the internal space (S) and heating the internal space (S). The sheath heater (13) is mounted on the bottom surface side of the internal space (S) of the housing (6) with a gap provided between the bottom surface and the sheath heater (13). A mounting plate (12) on which internal devices including the PEFC stack (4) are mounted is placed in the internal space (S) of the housing (6). The sheath heater (13) is placed between the mounting plate (12) and the bottom surface of the internal space (S).
This invention provides a method for starting a fuel cell system which can reliably conduct reforming from an early stage and can more reliably prevent an oxidative deterioration in anode, and a fuel cell system suitable for the method. The method is a method for starting a fuel cell system comprising a reformer comprising a reforming catalyst layer for reforming a hydrocarbon fuel to produce a hydrogen-containing gas, and a high temperature-type fuel cell for generating electric power using a hydrogen-containing gas. The method comprises a) the step of raising the temperature of the reforming catalyst layer while measuring the temperature of the reforming catalyst layer, b) the step of calculating the flow rate of a hydrocarbon fuel which can be reformed in the reforming catalyst layer based on the measured temperature of the reforming catalyst layer, and c) the step of supplying the hydrocarbon fuel at the calculated flow rate into the reforming catalyst layer to reform the fuel, and supplying the resultant reformed gas into an anode of a high temperature-type fuel cell. The amount of the hydrocarbon fuel supplied into the reforming catalyst layer is increased while repeating step b) and step c) until the amount of the hydrocarbon fuel supplied into the reforming catalyst layer reaches the flow rate at the time of the completion of the start.
C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
H01M 8/04 - Dispositions auxiliaires, p. ex. pour la commande de la pression ou pour la circulation des fluides
H01M 8/06 - Combinaison d’éléments à combustible avec des moyens de production de réactifs ou pour le traitement de résidus
H01M 8/12 - Éléments à combustible avec électrolytes solides fonctionnant à haute température, p. ex. avec un électrolyte en ZrO2 stabilisé
88.
ELLIPTICALLY POLARIZING PLATE, METHOD FOR PRODUCING THE SAME, AND LIQUID CRYSTAL DISPLAY DEVICE USING THE SAME
Disclosed is an elliptically polarizing plate having a homeotropically aligned liquid crystal layer, which is improved in viewing angle and contrast, while being reduced in thickness. This elliptically polarizing plate is composed of at least a homeotropically aligned liquid crystal layer, which is formed by homeotropically aligning a positive uniaxial liquid crystal composition in a liquid crystal state and then fixing the alignment, a retardation film having a retardation function, and a linear polarizing plate having a multilayer structure wherein one side of a polarizer is protected by a light-transmitting protective film. The elliptically polarizing plate is characterized by having either of the following multilayer structures: (A) the light-transmitting protective film/the polarizer/the retardation film/the homeotropically aligned liquid crystal layer; and (B) the light-transmitting protective film/the polarizer/the homeotropically aligned liquid crystal layer/the retardation film.
Provided is an elliptic polarization plate having excellent view angle improving effects. In the elliptic polarization plate, a polarization plate, a first optical anisotropic layer and a second optical anisotropic layer are laminated in this order. The first optical anisotropic layer satisfies inequalities of 0.8≤NZ1≤1.6 and 120≤Re1≤250. The layers are laminated so that the slow axis of the first optical anisotropic layer and the absorption axis of the polarization plate orthogonally intersect with each other. The phase difference of the second optical anisotropic layer within a surface with a wavelength of 550nm is 30-150nm. The second optical anisotropic layer is a liquid crystal film composed of a liquid crystalline polymer exhibiting optically positive uniaxial characteristic and has a fixed nematic hybrid orientation structure having a liquid crystal molecule average tilt angle of 5-50°. The orientation direction of the second optical anisotropic layer and the absorption axis of the polarization plate are laminated in parallel, and the elliptic polarization plate is used in a TN type liquid crystal display device by having the second optical anisotropic layer side on the liquid crystal cell side.
Disclosed are: a highly pure, inexpensive and safe composition having a high carotenoid content; a method for the industrial production of the composition; a functional food, a pharmaceutical composition or a cosmetic comprising the composition; and a method for the production of a composition having a carotenoid content of at least 80%, which is characterized by extracting a microbial culture with a lower alcohol having a temperature of 80˚C or higher or a combination of water and an lower alcohol both having temperatures of 80˚C or higher to produce an extract, and washing and filtrating a precipitate obtained from the extract with a combination of a lower alcohol and water.
C12P 23/00 - Préparation de composés contenant un cycle cyclohexène comportant une chaîne latérale non saturée d'au moins dix atomes de carbone liés par des doubles liaisons conjuguées, p. ex. carotènes
A23L 1/30 - contenant des additifs (A23L 1/308 a priorité);;
A61K 8/35 - Cétones, p. ex. quinones, benzophénone
A61K 31/122 - Cétones ayant l'atome d'oxygène lié directement à un cycle, p. ex. quinones, vitamine K1, anthraline
Provided is a method for correctly inspecting defects of an optical film which includes a first liquid crystal film wherein a liquid crystal is aligned in hybrid nematic orientation. A defect inspecting element irradiates an optical film with light through a first polarization plate from a light source, and is composed of a second liquid crystal film and a second polarization plate. In the second liquid crystal film, liquid crystal is aligned in hybrid nematic orientation to the opposite side to the light source with respect to the optical film. The defect inspecting element is arranged so that the second liquid crystal film side is adjacent to the optical film side. The optical film is inspected by tilting the defect inspecting element from the optical film.
G02F 1/13 - Dispositifs ou dispositions pour la commande de l'intensité, de la couleur, de la phase, de la polarisation ou de la direction de la lumière arrivant d'une source lumineuse indépendante, p. ex. commutation, ouverture de porte ou modulationOptique non linéaire pour la commande de l'intensité, de la phase, de la polarisation ou de la couleur basés sur des cristaux liquides, p. ex. cellules d'affichage individuelles à cristaux liquides
G02F 1/13363 - Éléments à biréfringence, p. ex. pour la compensation optique
It is possible to assure particle capturing performance, further reduce the weight, and improve the shape stability of a filter duct. The filter duct has a bag-shaped fiber arrangement layered body (101) having an opening through which a gas flows in. The gas which has flown into the interior of the bag through its opening flows out through the fiber arrangement layered body (101). The fiber arrangement layered body is formed by layering a plurality of fiber arrangement layers (101A to 101D) in which fibers (103A to 103D) are arranged substantially in a straight line in one direction. A part of the fiber arrangement layers (101A, 101C) and other fiber arrangement layers (101B, 101D) are layered so that the fiber extension directions (105A-105D) orthogonally intersect each other.
B01D 39/16 - Autres substances filtrantes autoportantes en substance organique, p. ex. fibres synthétiques
B01D 46/02 - Séparateurs de particules comportant des filtres creux faits en un matériau souple, p. ex. appareils de précipitation de poussières
D04H 3/16 - Non-tissés formés uniquement ou principalement de fils ou de matériaux filamenteux similaires de bonne longueur caractérisés par la méthode de renforcement ou de consolidation avec liages produits par soudage entre fils thermoplastiques ou filaments avec liages entre filaments thermoplastiques produits en relation avec la formation des filaments, p. ex. suivant immédiatement l'extrusion
A gas oil composition which contains an environmentally friendly gas oil base produced from, as raw materials, an animal/vegetable fat and triglyceride-containing hydrocarbons which are an ingredient derived from an animal/vegetable fat. It is excellent in life-cycle CO2 emission characteristics, fuel efficiency, and oxidative stability and in member stability. The gas oil composition contains: 5-50 mass% saturated chain hydrocarbons produced by contacting an animal/vegetable fat and/or a feed oil comprising an ingredient derived from an animal/vegetable fat with a given porous inorganic oxide and a catalyst containing one or more metals selected among the elements in Groups 6A and 8 of the periodic table and deposited on the porous inorganic oxide, under the conditions of a hydrogen pressure of 2-13 MPa, liquid space velocity of 0.1-3.0 h-1, hydrogen/oil ratio of 150-1,500 NL/L, and reaction temperature of 150-480°C; and 5-30 mass% catalytically-cracked gas oil base obtained by hydrotreating a gas oil fraction obtained with a catalytic cracking apparatus. The composition has a cetane number of 54 or larger and an aromatic content of 17 vol.% or higher.
C10L 1/08 - Combustibles carbonés liquides à base essentielle de mélanges d'hydrocarbures pour allumage par compression
C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
C10G 11/00 - Craquage catalytique, en l'absence d'hydrogène, des huiles d'hydrocarbures
C10G 45/02 - 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
A gas oil composition obtained by mixing 5-70 vol.% hydrotreated petroleum oil with 95-30 vol.% gas oil base obtained by mixing a hydrocracked gas oil fraction and/or a dewaxed gas oil base with an environmentally friendly gas oil base produced by contacting a raw oil with a catalyst comprising a given porous inorganic oxide and an active metal under given reaction conditions, the raw oil being one obtained by mixing an animal/vegetable fat and/or an ingredient derived from an animal/vegetable fat with a sulfur-containing hydrocarbon compound. The gas oil composition has a 90% running temperature of 360°C or lower, sulfur content of 10 mass ppm or lower, oxygen content of 1 mass% or lower, fatty acid/alkyl ester content of 3.5 mass% or lower, total acid value of 0.13 mg-KOH/g or less, methanol content of 0.01 mass% or lower, glyceride content of 0.01 mass% or lower, and cold filter plugging point of -5°C or lower. The gas oil composition is excellent in life-cycle CO2 emission characteristics and oxidative stability and in member stability.
C10L 1/08 - Combustibles carbonés liquides à base essentielle de mélanges d'hydrocarbures pour allumage par compression
C10G 3/00 - Production de mélanges liquides d'hydrocarbures à partir de matières organiques contenant de l'oxygène, p. ex. huiles, acides gras
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
Disclosed is a method for producing a norbornene derivative, wherein a norbornadiene derivative represented by the general formula (3) below is reacted with a bromine compound represented by the general formula (4) below in the presence of palladium and at least one compound selected from the phosphorus compounds represented by the general formulae (1) and (2) below, thereby producing a norbornene derivative represented by the general formula (5) below wherein a substituent represented by Z is in the exo configuration. (In the formula (1), R1, R2, R3 and R4 independently represent a hydrogen atom or the like; and R5 and R6 independently represent a branched saturated hydrocarbon group having 3-10 carbon atoms or the like.) (In the formula (2), R7 represents a branched saturated hydrocarbon group having 3-10 carbon atom.) (In the formula (3), R8, R9, R10, R11 and R12 independently represent a hydrogen atom or the like; l represents an integer of 0 or 1; m represents an integer of 0 or 1; and n represents an integer of 0 or 1.) (In the formula (4) Br-Z-R13, Z represents a phenylene group or the like; and R13 represents a hydrogen atom or the like.) (In the formula (5), R14, R15, R16, R17 and R18 independently represent a hydrogen atom or the like; Z represents a phenylene group or the like; R19 represents a hydrogen atom or the like; l represents an integer of 0 or 1; m represents an integer of 0 or 1; and n represents an integer of 0 or 1.)
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
C07C 13/605 - Hydrocarbures polycycliques ou leurs dérivés hydrocarbonés acycliques à cycles condensés à trois cycles condensés à système cyclique ponté
A method of regenerating an oil adsorbent without taking it out of the equipment even when an oil has been adsorbed thereon in a large quantity. The regeneration method comprises washing a carbonaceous oil adsorbent which comprises a calcined coke and has adsorbed an oil with water having a temperature of 40°C or higher or with bubble-containing water having a temperature of 40°C or higher.
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
C02F 1/28 - Traitement de l'eau, des eaux résiduaires ou des eaux d'égout par absorption ou adsorption
97.
METHOD AND APPARATUS FOR HYDROGEN PRODUCTION AND CARBON DIOXIDE RECOVERY
A method and apparatus with which production of highly purified hydrogen and recovery of carbon dioxide can be efficiently carried out. There is disclosed a method for hydrogen production and carbon dioxide recovery adapted to carry out production of hydrogen and recovery of carbon dioxide from a carbonaceous fuel. The method comprises the membrane separation reforming step of, using a reformer with hydrogen permeation membrane, simultaneously carrying out reforming of the carbonaceous fuel and separation of hydrogen to thereby obtain a hydrogen-permeation-membrane permeated gas being a gas having permeated the hydrogen permeation membrane and a reformer offgas being a gas not having permeated the hydrogen permeation membrane. The method further comprises the step of treating the reformer offgas with the use of a hydrogen separation membrane and a carbon dioxide separation membrane to thereby obtain a hydrogen-enriched gas and a carbon-dioxide-enriched gas, or the step of performing a shift reaction of the reformer offgas and thereafter carrying out separation into a carbon-dioxide-enriched gas and a gas enriched in components other than carbon dioxide. Moreover, there is disclosed an apparatus for carrying out the method.
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
B01D 53/22 - 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 diffusion
C01B 3/38 - Production d'hydrogène ou de mélanges gazeux contenant de l'hydrogène par réaction de composés organiques gazeux ou liquides avec des agents gazéifiants, p. ex. de l'eau, du gaz carbonique, de l'air par réaction d'hydrocarbures avec des agents gazéifiants avec des catalyseurs
The following process for producing a hydrocarbon oil is provided. First, in the presence of hydrogen, a raw oil containing an oxygenous organic compound and a water-insoluble chlorinous compound is brought into contact with a hydrogenation catalyst composed of a support containing a porous inorganic oxide and, supported thereon, at least one metal selected from among those of Group VIA and Group VIII of the periodic table so as to form a hydrocarbon oil and water through hydrogenation deoxygenation of the oxygenous organic compound and convert the water-insoluble chlorinous compound to a water-soluble chlorinous compound, thereby obtaining a reaction product containing the hydrocarbon oil, water and the water-soluble chlorinous compound. Subsequently, the water containing the water-soluble chlorinous compound is separated from the reaction product, thereby obtaining a produced oil containing the hydrocarbon oil.
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
99.
METHOD FOR PRODUCTION OF MONOSACCHARIDE AND/OR WATER-SOLUBLE POLYSACCHARIDE, AND METHOD FOR PRODUCTION OF CARBONACEOUS MATERIAL HAVING SULFONATE GROUP
Disclosed is a method for producing a monosaccharide and/or a water-soluble polysaccharide at low cost by hydrolyzing a polysaccharide. A carbonaceous material having a sulfonate group can be produced at low cost by carbonizing and sulfonating a woody plant or a herbaceous plant without purification. A monosaccharide and/or a water-soluble polysaccharide can be produced at low cost by using the carbonaceous material.
Monosaccharides are effectively produced by hydrolyzing a cellulose-containing material by using a sulfonate group-containing carbonaceous material, neutralizing the reaction mixture and then enzymatically saccharifying the liquid components and the solid components.
brevets
