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公开(公告)号：US20240208888A1
公开(公告)日：2024-06-27
申请号：US18288310
申请日：2022-04-26
IPC分类号： C07C29/151 , C01B3/32
CPC分类号： C07C29/1518 , C01B3/32 , C01B2203/061 , C01B2210/001 , C01B2210/0014
摘要： The invention relates to a process and to a plant for producing methanol from a synthesis gas having a hydrogen deficit. A fresh gas stream from a reformer unit which includes hydrogen and carbon oxides is combined with a hydrogen-containing stream from a hydrogen recovery stage. This affords a synthesis gas stream having a stoichiometry number SN, defined as SN=[n(H2)−n(CO2)]/[n(CO)+n(CO2)], of less than 2.0. The synthesis gas stream is combined with a residual gas stream and the synthesis gas stream and the residual gas stream are passed through a bed of a methanol synthesis catalyst at elevated pressure and elevated temperature to obtain a product stream having methanol and the residual gas stream, and the product stream is cooled to separate methanol from the residual gas stream.
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公开(公告)号：US20240183047A1
公开(公告)日：2024-06-06
申请号：US18285950
申请日：2022-03-10
发明人： Denis SIRAC , Johan ANDRE
IPC分类号： C25B11/036 , C25B9/23 , C25B11/031 , H01M4/86 , H01M8/10 , H01M8/1004
CPC分类号： C25B11/036 , C25B9/23 , C25B11/031 , H01M4/8631 , H01M8/1004 , H01M2004/8694 , H01M2008/1095
摘要： A bipolar plate for a fuel cell stack or for an electrolyzer stack, having an anode plate and a cathode plate which are joined to face-to-face. Wherein the face of the anode plate that faces the face of the cathode plate delimits an internal space that forms a circuit for the distribution of a first fluid, thereby forming a bipolar plate. Wherein the first opening and the second opening facing one another thereby forming a collector configured to enable the passage of the first fluid or a second fluid through the bipolar plate. Wherein the first opening and the second opening have distinct dimensions such the peripheral end of the first opening and the peripheral end of the second opening are offset in relation to one another in the plane of the bipolar plate, forming a shoulder at the peripheral end of the collector.
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公开(公告)号：US20240151597A1
公开(公告)日：2024-05-09
申请号：US18281101
申请日：2022-02-04
发明人： Fangyan SUN , Olivier ONDO
CPC分类号： G01L1/2206 , F17C13/02 , G01L9/04 , G01M5/0041 , G01M5/0083 , F17C2250/0469 , F17C2270/0745
摘要： A method for fixing an assembly onto a gas vessel configured to contain a pressurized fluid. The assembly including a housing, an electronic acquisition board secured to the housing, and a strain gauge. The method including fixing the strain gauge to the vessel using a second adhesive means, the strain gauge being fixed to the vessel in such a way to allow deformation along with the vessel under the effect of the pressurized gas contained in the vessel. Electrically connecting the strain gauge and the electronic acquisition board using at least one electric cable thereby allowing the housing to be free to move relative to the strain gauge. Fixing the housing to the vessel using a first adhesive means so as to cover the strain gauge and thereby leaving a volume of air between the housing and the strain gauge and/or between the strain gauge and the electronic acquisition board.
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4.发明公开公开(公告)号：US20240124303A1
公开(公告)日：2024-04-18
申请号：US18377950
申请日：2023-10-09
发明人： Alexander ROESCH , Jasmin JUNGER
CPC分类号： C01B3/42 , C01B3/384 , C01B32/40 , C01B2203/0233 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0811 , C01B2203/0833 , C01B2203/0883 , C01B2203/1235 , C01B2203/1258 , C01B2210/0051
摘要： A process for producing a carbon dioxide depleted synthesis gas product by steam reforming is provided. The process includes cooling crude synthesis gas stream produced in a main reforming stage in a first cooling device and reacting in a carbon dioxide absorption column, reacting a carbon dioxide loaded absorbent stream from the carbon dioxide absorption column in an absorbent regeneration column, cooling the carbon dioxide enriched hot vapor stream from the absorbent regeneration column in a second cooling device and cooling a carbon dioxide depleted hot absorbent stream from the absorbent regeneration column in a third cooling device. Preheated air streams from the cooling devices are fed as oxidant to the main reforming stage.
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公开(公告)号：US20240025787A1
公开(公告)日：2024-01-25
申请号：US18224380
申请日：2023-07-20
申请人： L'Air Liquide, Société Anonyme pour I'Etude et I'Exploitation des Procédés Georges Claude , American Air Liquide, Inc.
发明人： Remi TSIAVA , Bhupesh DHUNGEL
IPC分类号： C03B5/237 , F23L15/04 , F23J15/04 , F27D17/00 , C01B3/04 , B01D53/56 , B01D53/79 , C03B5/225
CPC分类号： C03B5/237 , F23L15/045 , F23J15/04 , F27D17/004 , C01B3/047 , B01D53/56 , B01D53/79 , C03B5/225 , F23C2900/9901 , C01B2203/0277 , C01B2203/0272 , C01B2203/0827 , B01D2251/2062 , B01D2257/404
摘要： A method for operating a furnace, the method including the steps of: combusting fuel with oxidant, thereby generating thermal energy and fumes, heating the furnace with a first part of the thermal energy generated in step a, evacuating the generated fumes from the furnace at a temperature of at least 900° C., the evacuated fumes containing a second part of the thermal energy generated in step a, and using the second part of the thermal energy generated in step a for heating the oxidant and as a heat source for cracking ammonia in a cracker into a mixture including hydrogen, nitrogen and un-cracked ammonia, at least part of the mixture produced in step d-ii being combusted as fuel in step a with at least part of the heated oxidant produced in step d-i.
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公开(公告)号：US20240024835A1
公开(公告)日：2024-01-25
申请号：US18224363
申请日：2023-07-20
发明人： Dieter ULBER , Peter WEIGAND , Holger SCHLICHTING , Stefan WALTER
CPC分类号： B01J8/1836 , B01J19/24 , B01J19/0013 , B01J19/02 , B01J8/1827 , B01J8/0015 , C01B3/363 , B01J2219/00157 , B01J2208/00504 , C01B2203/0255 , C01B2203/0261 , B01J2219/024
摘要： Provided is a burner arrangement for producing synthesis gas by non-catalytic or catalytic partial oxidation of fluid or fluidized carbon-containing fuels in the presence of an oxidant and a moderator, including following assemblies: (a) a feeding means for separately feeding three fluid reaction media streams or two fluid and one fluidized reaction media stream into a burner, (b) at least one burner, (c) outer wall of the at least one burner is fluid-tightly connected to a burner mounting plate, (d) a reaction chamber, (e) the at least one burner is insertable into the reaction chamber, and (f) outer wall of the at least one burner and the side of the at least one burner mounting plate facing away from the interior of the reaction chamber are designed to allow cooling by indirect heat exchange with a cooling fluid.
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公开(公告)号：US20230314069A1
公开(公告)日：2023-10-05
申请号：US18130542
申请日：2023-04-04
发明人： Michael A. TURNEY , Alain Guillard
CPC分类号： F25J1/0234 , F25J1/0015 , F25J1/0017 , F25J3/04054 , F25J2215/40 , F25J2280/10
摘要： A process for the production of at least liquid oxygen and/or liquid nitrogen in cryogenic rectification. During a first period, during which electrical power prices are low, a process stream utilized by the ASU is liquefied and stored. During a second period, during which electrical prices high, at least a portion of the stored, liquefied process stream is withdrawn and introduced into the ASU. Wherein the MAC has a discharge pressure of greater than 10 bara during the first period, a first molar flowrate (LF) and a first pressure (LP) during the first period, a second molar flowrate (HF) and a second pressure (HP) during the second period. Wherein C=(LF/HF)/(LP/HP). And wherein second molar flowrate (HF) is
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公开(公告)号：US20230077286A1
公开(公告)日：2023-03-09
申请号：US17799401
申请日：2021-01-26
发明人： Luc JARRY
摘要： A method for the use of a gaseous effluent containing a CO2 gas fraction and a non-CO2 gas fraction, including at a first location: providing liquid nitrogen at a temperature less than −196° C., and causing the gaseous effluent to contact the liquid nitrogen to as to capture at least part of the CO2 present in the CO2 gas fraction as a mixture of CO2 particles and liquid nitrogen. Conveying at least part of the mixture to a second location, and at the second location, bringing the mixture into contact with one or more ingredients of a wet concrete before and/or during and/or after the wet concrete is prepared by blending the ingredients of the wet concrete in a blender, so that the mixture extracts heat from said one or more ingredients of the wet concrete, and CO2 from the mixture partially carbonates Ca-compounds present in the wet concrete.
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公开(公告)号：US20230068126A1
公开(公告)日：2023-03-02
申请号：US17713710
申请日：2022-04-05
发明人： Michael A. Turney , Alain Guillard
摘要： A system and method for cooling an oxygen stream by heat exchange with a warming supply nitrogen stream having of a heat exchanger having at least a Zone A and a Zone B, the system having indirect heat exchange between a gaseous oxygen stream, and a high-pressure liquid nitrogen stream split into at least a first portion which passes through a Zone A, and a second portion which passes through a Zone B during a first phase of operation. And a high-pressure liquid nitrogen stream passing through Zone A, thereby producing a high-pressure nitrogen vapor stream, which passes through an expansion turbine, thereby producing an expansion turbine outlet stream which then passes through Zone B, during a second phase of operation, thereby producing a liquid oxygen stream.
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10.发明申请公开(公告)号：US20220356060A1
公开(公告)日：2022-11-10
申请号：US17736539
申请日：2022-05-04
摘要： In a process for the separation of a mixture containing hydrogen and carbon monoxide to produce gaseous hydrogen, the mixture is cooled down to a temperature below −180° C. and then separated at a temperature below −100° C. to produce a gas enriched in hydrogen and a fluid enriched in carbon monoxide, at least a part of the gas enriched in hydrogen is sent to a pressure swing adsorption separation apparatus operating at a temperature above 0° C. to produce a gas rich in hydrogen at a pressure of at least 20 bars, and at least a part of the gas rich in hydrogen is cooled in the heat exchanger down to a temperature below −100° C., reduced in pressure in a turbine down to a pressure of at least 8 bars and reheated in the heat exchanger to constitute a product rich in hydrogen at a pressure of at least 8 bars.
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