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公开(公告)号:US11088372B2
公开(公告)日:2021-08-10
申请号:US16466946
申请日:2017-12-01
Applicant: Haldor Topsøe A/S
Inventor: Tobias Holt Nørby , Bengt Peter Gustav Blennow , Rainer Küngas , Jeppe Rass-Hansen , Thomas Heiredal-Clausen
IPC: H01M4/64 , H01M8/0228 , H01M8/021 , H01M8/0215 , H01M8/124
Abstract: Improved contact between interconnect and oxygen electrode material in solid oxide cell (SOC) stacks is achieved through a contact point between the oxygen electrode or an oxygen-side contact layer of the SOC and a coated ferritic stainless steel interconnect in the SOC stack, where the coating on the metallic interconnect comprises Cu.
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公开(公告)号:US11078131B2
公开(公告)日:2021-08-03
申请号:US16547173
申请日:2019-08-21
Applicant: Haldor Topsøe A/S
Inventor: Hassan Modarresi
IPC: C07C2/80 , H01M8/0606 , H01M8/0612 , H01M8/0637 , H01M8/0662 , H01M8/04089 , C01B3/38 , H01M8/12 , H01M8/124
Abstract: A fuel cell reactor, preferably a solid oxide fuel cell (SOFC) reactor, for performing direct conversion of a hydrocarbon-containing gas to a higher hydrocarbons product is confined by walls, where reactants are flown in the anode compartments and air is introduced to the cathode compartments, and where oxygen is transferred from one side of the walls to the other side to promote or inhibit a chemical reaction. The process for direct conversion of a hydrocarbon-containing gas to a higher hydrocarbons product takes place in the anode compartment of the reactor, in which produced hydrogen, limiting the conversion to the equilibrium, is reacted in situ with oxygen ions transferred from the cathode compartment to produce steam, thereby removing the equilibrium-limiting hydrogen from the reaction.
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33.
公开(公告)号:US11060036B2
公开(公告)日:2021-07-13
申请号:US17040863
申请日:2019-05-02
Applicant: Haldor Topsøe A/S
Inventor: Martin Dan Palis Sørensen
IPC: C10G3/00
Abstract: Process for the conversion of oxygenates to C5+ hydrocarbons boiling in the gasoline boiling range, comprising the steps of continuously a) providing one or more feed streams of one or more oxygenate compounds; b) heating the one or more feed streams to an inlet temperature of one or more downstream conversion reactors; c) introducing the one or more heated feed stream into inlet of the one or more conversion reactors; d) converting in the one or more conversion reactors the one or more heated feed stream in presence of catalyst to a converted oxygenate product comprising C5+ hydrocarbons; e) withdrawing from the one or more conversion reactors the converted oxygenate product; f) determining at outlet of the one or more conversion reactors amount of the one or more unconverted oxygenate compounds in the withdrawn converted oxygenate product; g) separating the converted oxygenate product into a C4− hydrocarbon fraction, a fraction with the C5+ hydrocarbons boiling in the gasoline boiling range and a fraction comprising water and the one or more unconverted oxygenate compounds, wherein the inlet temperature of the one or more feed streams in step b is continuously adjusted to maintain a constant amount of the one or more unconverted oxygenate compounds as determined in step f.
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公开(公告)号:US11059719B2
公开(公告)日:2021-07-13
申请号:US16087943
申请日:2017-04-24
Applicant: HALDOR TOPSØE A/S
Inventor: Peter Mølgaard Mortensen , Martin Østberg , Poul Erik Højlund Nielsen
Abstract: In a process for producing hydrogen or syngas by methanol cracking, whereby methanol is catalytically decomposed into hydrogen and carbon monoxide in an endothermal reaction, said reaction takes place in a reactor with direct inductive heating in the reaction zone. The heating is obtained by passing an alternating current through a metallic coil located inside the reactor or by using induction heated catalyzed hardware in the shape of a ferromagnetic structure, which is coated with an oxide impregnated with the catalytically active phase.
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公开(公告)号:US11040934B2
公开(公告)日:2021-06-22
申请号:US16394009
申请日:2019-04-25
Applicant: HALDOR TOPSØE A/S
Inventor: Esben Taarning , Irantzu Sadaba Zubiri , Sebastian Meier
IPC: C07C59/42 , C07C67/39 , C07C51/16 , B01J29/70 , C07C69/732
Abstract: Preparation of 2,5,6-trihydroxy-3-hexenoic acid and 2,5-dihydroxy-3-pentenoic acid and esters thereof from C6 and C5 sugars in the presence of a Lewis Acid material, wherein the yield of the 2,5,6-trihydroxy-3-hexenoic acid or 2,5-dihydroxy-3-pentenoic acid or esters thereof exceeds 15%. The process including the steps of contacting a saccharide composition including one or more C6 and/or C5 saccharide units with a Lewis Acid material; and recovering 2,5,6-trihydroxy-3-hexenoic acid and/or 2,5-dihydroxy-3-pentenoic acid or the esters thereof.
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36.
公开(公告)号:US20210139394A1
公开(公告)日:2021-05-13
申请号:US16492281
申请日:2018-03-02
Applicant: HALDOR TOPSØE A/S
Abstract: In a process for the catalytic dehydrogenation of lower alkanes to the corresponding alkenes, a regenerable catalyst comprising iron carbide supported on a carrier is used. A small amount (below 100 ppm) of a sulfur compound, such as H2S, is added during the process.
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公开(公告)号:US20210130190A1
公开(公告)日:2021-05-06
申请号:US17041834
申请日:2019-05-06
Applicant: HALDOR TOPSØE A/S
Inventor: Jonathan HØJBERG , Søren DAHL , Jakob Weiland HØJ , Christian Fink ELKJÆR
IPC: C01G53/00
Abstract: The invention relates to a lithium positive electrode active material for a high voltage secondary battery, where the cathode is fully or partially operated above 4.4 V vs. Li/Li+. The lithium positive electrode active material comprises at least 95 wt % spinel having a chemical composition of LixNiyMn2-y-zDzO4, wherein 0.9≤x≤1.1, 0.4≤y≤0.5, 0.02≤z≤0.2, wherein D is a dopant chosen between the following elements: Co, Cu, Ti, Zn, Mg, Fe or combinations thereof. The lithium positive electrode active material is a powder composed of secondary particles formed by primary particles, wherein said lithium positive electrode active material has a tap density of at least 1.9 g/cm3. The invention also relates to process for preparing the lithium positive electrode active material of the invention and a secondary battery comprising the lithium positive electrode active material of the invention.
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公开(公告)号:US10941038B2
公开(公告)日:2021-03-09
申请号:US16074515
申请日:2017-02-02
Applicant: HALDOR TOPSØE A/S
Inventor: Annette E. Krøll Jensen , Per Juul Dahl , Niels Christian Schjødt
Abstract: A process for producing an ammonia synthesis gas, said process including the steps of: reforming a hydrocarbon feed in a reforming step thereby obtaining a synthesis gas comprising CH4, CO, CO2, H2 and H2O; and shifting said synthesis gas in a high temperature shift step over a promoted zinc-aluminum oxide based high temperature shift catalyst, wherein the steam/carbon ratio in the reforming step is less than 2.6.
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公开(公告)号:US20210054510A1
公开(公告)日:2021-02-25
申请号:US17046050
申请日:2019-04-11
Applicant: HALDOR TOPSØE A/S
Abstract: A method for the generation of a gas mixture comprising carbon monoxide, carbon dioxide and optionally hydrogen for use in hydroformylation plants or in carbonylation plants, including mixing an optional steam with carbon dioxide in the desired molar ratio, feeding the resulting gas to a solid oxide electrolysis cell (SOEC) or an SOEC stack at a sufficient temperature for the cell or cell stack to operate while effecting a partial conversion of carbon dioxide to carbon monoxide and optionally of steam to hydrogen, removing some or all the remaining steam from the raw product gas stream by cooling the raw product gas stream and separating the remaining product gas from a liquid, and using said gas mixture containing CO and CO2 for liquid phase synthesis reactions utilizing carbon monoxide as one of the reactants while recycling CO2 to the SOEC or SOEC stack.
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公开(公告)号:US20210032761A1
公开(公告)日:2021-02-04
申请号:US16641007
申请日:2018-10-01
Applicant: HALDOR TOPSØE A/S
Inventor: John Bøgild HANSEN
IPC: C25B1/04
Abstract: In a method for generating ammonia synthesis gas by electrolysis, comprising feeding a mixture of steam and compressed air into the first of a series of electrolysis units and passing the outlet from one electrolysis unit to the inlet of the next electrolysis unit together with air, the electrolysis units are run in endothermal mode and the nitrogen part of the synthesis gas is provided by burning the hydrogen produced by steam electrolysis by air in or between the electrolysis units. The electrolysis units are preferably solid oxide electrolysis cell (SOEC) stacks.
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