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公开(公告)号:US20180079643A1
公开(公告)日:2018-03-22
申请号:US15564521
申请日:2016-03-31
Applicant: Haldor Topsøe A/S
Inventor: Peter Mølgaard MORTENSEN , Martin ØSTBERG
CPC classification number: C01B3/38 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/041 , C01B2203/0475
Abstract: A reformer device including a reaction chamber for carrying out a reaction having a hydrocarbon stream as a reactant gas and with hydrogen rich synthesis gas as a reaction product. The membrane is provided within the reaction chamber. The reformer device further includes a heating reactor for heating the reaction chamber, where the membrane is a semi-permeable membrane arranged to allow CO2 pass through it; the reaction chamber includes a catalyst material arranged to catalyze a steam methane reforming reaction and to catalyze a water gas shift reaction; and the reformer device is arranged to carry out the steam methane reforming reaction at a pressure between about 15 and about 50 barg within the reaction chamber. A method for carrying out a reaction having a hydrocarbon stream as a reactant gas and with hydrogen rich synthesis gas as reaction product, in a reformer device.
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公开(公告)号:US20170341047A1
公开(公告)日:2017-11-30
申请号:US15536123
申请日:2015-12-16
Applicant: HALDOR TOPSØE A/S
Inventor: Emir ZAHIROVIC , Klaus RISBJERG JARLKOV , Karthik Gopal MANOHARAN , Flemming PLOUGSTRUP NIELSEN , Roberta CENNI
CPC classification number: B01J8/0065 , B01J4/002 , B01J4/005 , B01J8/0085 , B01J8/0278 , B01J8/0492 , B01J2208/00761 , B01J2208/00902 , B01J2219/00247 , C10G49/002 , C10G67/02
Abstract: A particle separating catalytic reactor comprising a kinetic particle separator.
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公开(公告)号:US20170239618A1
公开(公告)日:2017-08-24
申请号:US15507841
申请日:2015-09-09
Applicant: HALDOR TOPSØE A/S
Inventor: Souheil Saadi , Niklas Bengt Jakobsson
IPC: B01D53/86 , C01B17/50 , C01B17/765 , B01D46/24 , B01D53/50
CPC classification number: B01D53/8612 , B01D46/2407 , B01D53/502 , B01D53/508 , B01D53/869 , B01D2251/11 , B01D2251/404 , B01D2251/604 , B01D2255/1023 , B01D2255/2065 , B01D2255/20723 , B01D2255/2073 , B01D2255/20761 , B01D2255/20769 , B01D2255/20776 , B01D2255/20784 , B01D2255/904 , B01D2257/302 , B01D2257/304 , C01B17/508 , C01B17/74 , C01B17/765 , Y02P20/129
Abstract: A process for the oxidation of hydrogen sulfide to sulfur trioxide with subsequent sulfur trioxide removal comprises oxidizing hydrogen sulfide to sulfur trioxide in at least one catalyst-containing reactor and feeding the effluent from the last reactor to a candle filter unit for SO3 removal, where it is mixed with an injected alkaline sorbent slurry or powder to form an alkali sulfate and a hot clean gas. Preferably the oxidation is done in two reactors, the first oxidizing H2S to SO2 over a monolith type catalyst and the second oxidizing SO2 to SO3 over a VK type catalyst.
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公开(公告)号:US20170233661A1
公开(公告)日:2017-08-17
申请号:US15519049
申请日:2015-10-30
Applicant: Haldor Topsøe A/S
Inventor: Arne Knudsen , Ian Menjon , Jan Due Nielsen
IPC: C10G3/00
CPC classification number: C10G3/49 , C10G3/42 , C10G2300/1011 , C10G2300/202 , C10G2400/02 , C10G2400/04 , Y02P30/20
Abstract: The invention relates to a processes comprising the steps of: in an evaporator forming a gas phase methanol rich stream from a feed stream; withdrawing a liquid purge stream from the evaporator, said liquid purge stream comprising oxygenates and water; providing the gas phase methanol rich stream to a conversion step; and adding at least part of said liquid purge stream upstream the conversion step.
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公开(公告)号:US20170226915A1
公开(公告)日:2017-08-10
申请号:US15502727
申请日:2015-07-24
Applicant: Haldor Topsøe A/S , Ecospray Technologies S.r.I.
Inventor: Maurizio Archetti
CPC classification number: F01N3/34 , F01N3/035 , F01N3/22 , F01N3/306 , F01N9/002 , F01N2470/30 , F01N2590/02 , Y02T10/47
Abstract: Method and system for thermal regeneration of a catalyst by inlet turbine exhaust gas from a diesel engine, where a gas split stream (08) is led from the engine exhaust (02) through an eductor (04) and further to regeneration of a catalyst, wherein a cold air stream (09) is used to keep the regeneration gas stream at a desired constant temperature range.
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96.
公开(公告)号:US20170129913A1
公开(公告)日:2017-05-11
申请号:US15319332
申请日:2015-06-18
Applicant: Haldor Topsøe A/S
Inventor: Saravanamurugan Shunmugavel , Irantzu Sandaba Zubiri , Esben Taarning , Martin Spangsberg Holm
IPC: C07H1/00 , B01J29/04 , B01J29/70 , B01J37/00 , B01J37/04 , B01J37/10 , B01J37/02 , C01B39/46 , C01B37/00 , C01B39/02 , C07D307/36 , C07C67/08 , C07C51/16 , C07H3/02 , A23L33/10 , A23L27/30 , B01J29/89
CPC classification number: C07H1/00 , A23L27/34 , A23L33/10 , A23V2002/00 , B01J29/041 , B01J29/405 , B01J29/7049 , B01J29/7057 , B01J29/89 , B01J37/0018 , B01J37/0201 , B01J37/04 , B01J37/10 , B01J2229/186 , B01J2229/37 , C01B37/005 , C01B39/026 , C01B39/085 , C01B39/40 , C01B39/46 , C07C51/16 , C07C67/08 , C07D307/36 , C07H3/02
Abstract: A process for the preparation of C4 oxygenate compounds such as threose, erythrose or erythrulose starting from a composition comprising C1-3 oxygenate compounds such as formaldehyde, glycolaldehyde, glyoxal, pyruvaldehyde or acetol, wherein the process is carried out in the presence of a crystalline microporous material having a ring pore structure selected from an eight-membered ring pore structure or a ten-membered ring pore structure.
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公开(公告)号:US20170113212A1
公开(公告)日:2017-04-27
申请号:US15127881
申请日:2014-10-15
Applicant: HALDOR TOPSØE A/S
Inventor: Ton V.W. Janssens , Peter N.R. Vennestrøm
CPC classification number: B01J29/85 , B01D53/9418 , B01D2251/2062 , B01D2251/208 , B01D2255/20761 , B01D2255/50 , B01J29/084 , B01J29/84 , B01J37/0018 , B01J37/0036 , B01J37/0238 , B01J37/04 , B01J37/08 , B01J37/30 , B01J38/08 , B01J2229/183 , B01J2229/186 , B01J2229/38 , B01J2229/40 , C01B39/54 , F01N3/208 , F01N2370/02 , F01N2570/14 , F01N2610/02 , F01N2610/03 , F01N2610/10 , Y02P20/584
Abstract: Method for the preparation of a metal exchanged crystalline microporous metalloaluminophosphate or mixtures containing metal exchanged microporous metalloaluminophosphates materials comprising the steps of providing a dry mixture containing a) one or more metalloaluminophosphates starting materials that exhibit ion exchange capacity, and b) one or more metal compounds; heating the mixture in a gaseous atmosphere containing ammonia to a temperature and for a time sufficient to initiate and perform a solid state ion exchange of ions of the metal compound and ions of the crystalline microporous material; and obtaining the metal-exchanged microporous metalloaluminophosphate material or mixtures containing the metal-exchanged microporous metalloaluminophosphate material.
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公开(公告)号:US20170080387A1
公开(公告)日:2017-03-23
申请号:US15126218
申请日:2015-03-20
Applicant: HALDOR TOPSØE A/S , FLSMIDTH A/S
IPC: B01D53/86 , B01J23/648 , B01J23/22 , B01D46/00 , B01D46/02
CPC classification number: B01D53/8631 , B01D46/0024 , B01D46/02 , B01D53/75 , B01D53/86 , B01D53/88 , B01D2255/1023 , B01D2255/20707 , B01D2255/20723 , B01D2257/404 , B01D2257/502 , B01D2257/70 , B01D2257/708 , B01D2258/0233 , B01D2258/0283 , B01D2258/0291 , B01D2271/02 , B01J23/22 , B01J23/6482
Abstract: Filter bag assembly for use in cleaning of process gas comprising an outer tubular filter bag and one or more inner tubular filter bags separately arranged within the outer tubular filter bag, and said one or more inner tubular filter bags also separately arranged within each other, the one or more inner tubular filter bags and the outer tubular filter bags having an open end and a closed end, and at least one of the inner tubular filter bags and/or the outer tubular filter bag being provided with catalytically active material.
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公开(公告)号:US20170080376A1
公开(公告)日:2017-03-23
申请号:US15312000
申请日:2015-05-28
Applicant: HALDOR TOPSØE A/S
Inventor: Niklas Bengt Jakobsson , Joakim Reimer Thøgersen
CPC classification number: B01D53/0462 , B01D53/02 , B01D53/62 , B01D53/82 , B01D2253/104 , B01D2253/25 , B01D2253/304 , B01D2253/311 , B01D2253/342 , B01D2253/3425 , B01D2257/504 , B01D2258/0283 , B01J20/08 , B01J20/103 , B01J20/2804 , B01J20/28042 , B01J20/28045 , B01J20/3204 , B01J20/3236 , B01J20/3433 , B01J20/3483 , Y02C10/08
Abstract: The invention relates to a gas treatment monolith article, said gas treatment article comprising: a full body porous material comprising a porous substrate and an aluminium oxide coating homogeneously distributed throughout said porous substrate, wherein said porous substrate is a fibrous material; and at least one acid gas absorption active component or a precursor thereof impregnated into said porous aluminium oxide coated substrate. The invention further relates to uses of the gas treatment monolith article of the invention.
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100.
公开(公告)号:US20160107961A1
公开(公告)日:2016-04-21
申请号:US14892124
申请日:2014-05-15
Applicant: HALDOR TOPSØE A/S
Inventor: Hassan Modarresi , Christian Wix
IPC: C07C29/152 , B01J19/18 , B01J8/02
CPC classification number: C07C29/152 , B01J8/0292 , B01J8/0453 , B01J19/1856 , B01J2208/00274 , B01J2208/027 , C07C31/04
Abstract: In a process for the preparation of methanolin parallel reactors, comprising the steps of (a) reacting carbon oxides and hydrogen in the presence of a methanol catalyst in a first methanol reactor to obtain a first methanol-containing effluent, (b) introducing and reacting unconverted synthesis gas in a second methanol reactor in the presence of a methanol catalyst to obtain a second methanol-containing effluent, the first methanol reactor and the second methanol reactor being connected in parallel, (c) combining the first and second effluent, and (d) cooling and separating the combined and cooled effluent into a methanol-containing liquid phase and unconverted synthesis gas, the methanol catalyst in the first methanol reactor is indirectly cooled by boiling water and the methanol catalyst in the second methanol reactor is either directly or indirectly cooled by the unconverted synthesis gas prior to conversion into the second effluent.
Abstract translation: 在制备甲醇并行反应器的方法中,包括以下步骤:(a)在甲醇催化剂存在下,在第一甲醇反应器中使碳氧化物和氢气反应,得到第一含甲醇的流出物,(b)引入和反应 未转化的合成气在第二甲醇反应器中在甲醇催化剂存在下得到第二含甲醇的流出物,第一甲醇反应器和第二甲醇反应器并联连接,(c)将第一和第二流出物与( d)冷却并将合并后的流出物分离成含甲醇的液相和未转化的合成气,第一甲醇反应器中的甲醇催化剂由沸水间接冷却,第二甲醇反应器中的甲醇催化剂直接或间接地 在转化成第二流出物之前由未转化的合成气冷却。
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