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公开(公告)号:US10550055B2
公开(公告)日:2020-02-04
申请号:US15749607
申请日:2016-07-15
Applicant: Haldor Topsøe A/S
Inventor: Hassan Modarresi
IPC: C07C29/151 , B01J19/00 , C07C31/04
Abstract: In a novel process for methanol production from low quality synthesis gas, in which relatively smaller adiabatic reactors can be operated more efficiently, some of the inherent disadvantages of adiabatic reactors for methanol production are avoided. This is done by controlling the outlet temperature in the pre-converter by rapid adjustment of the recycle gas, i.e. by manipulating the gas hourly space velocity in the pre-converter.
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公开(公告)号:US10525503B2
公开(公告)日:2020-01-07
申请号:US16067635
申请日:2017-02-22
Applicant: Haldor Topsøe A/S
Inventor: Keld Johansen
IPC: B05D7/22 , B01J23/44 , B01J35/04 , B01D53/94 , F01N3/28 , F01N3/035 , B01J35/00 , B01J23/10 , B01J37/02 , B01J37/08 , B01J37/34
Abstract: A method for the preparation of a catalyzed monolithic body or a catalyzed particular filter. The method includes the step of suctioning a sol-solution containing catalytically active material and metal oxide catalyst carriers or precursors thereof into pores of a monolithic substrate, solely by capillary forces and without the application of vacuum or pressure.
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公开(公告)号:US10471406B2
公开(公告)日:2019-11-12
申请号:US15540852
申请日:2015-12-18
Applicant: Haldor Topsøe A/S
Inventor: Emir Zahirovic , Klaus Risbjerg Jarlkov , Roberta Cenni
Abstract: A particle separation system for a catalytic chemical reactor.
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公开(公告)号:US10286360B2
公开(公告)日:2019-05-14
申请号:US15500579
申请日:2015-02-23
Applicant: Haldor Topsøe A/S , Ecospray Technologies S.r.I.
Inventor: Keld Johansen , Maurizio Archetti
IPC: B01D53/94 , F01N13/00 , B01D46/00 , F01N3/04 , F01N3/10 , F01N3/20 , F01N5/04 , F01N9/00 , F01N13/08 , F01N3/023 , F01N3/032 , F01N3/035 , B01D53/50 , B01J23/652 , B01J35/00 , B01J35/04 , B01J21/06 , B01J23/22 , B01J23/30 , B01J23/44
Abstract: Method for removal of soot, ash and metals or metal compounds, together with removal of NOx and SOx being present in process off-gasses or engine exhaust gasses.
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公开(公告)号:US10074864B2
公开(公告)日:2018-09-11
申请号:US14888599
申请日:2013-05-02
Applicant: Haldor Topsøe A/S
Inventor: Thomas Heiredal-Clausen , Casper Buchholtz Frederiksen
IPC: C25B9/00 , C25B9/18 , C25B15/08 , H01M8/02 , H01M8/04 , H01M8/12 , H01M8/24 , H01M8/04082 , H01M8/2425 , H01M8/0258 , H01M8/0202 , H01M8/1246 , H01M8/2483 , H01M8/2428 , H01M8/124
CPC classification number: H01M8/04 , C25B9/00 , C25B9/18 , C25B15/08 , H01M8/0258 , H01M8/1246 , H01M8/2425 , H01M8/2428 , H01M8/2483 , H01M2008/1293
Abstract: Multiple gas inlet or outlets for a SOC unit is provided by stacked layers with cut outs for gas channels which overlap.
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公开(公告)号:US20180238628A1
公开(公告)日:2018-08-23
申请号:US15514961
申请日:2015-10-05
Applicant: Haldor Topsoe A/S
Inventor: Per Juul Dahl
Abstract: A heat exchanger has a pass baffle which is formed as an enclosure with two openings, one opening for connection to a shell-side fluid opening and one opening for passing heat exchanger tubes.
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公开(公告)号:US10029224B2
公开(公告)日:2018-07-24
申请号:US15216075
申请日:2016-07-21
Applicant: Haldor Topsøe A/S
Inventor: Lari Bjerg Knudsen , Martin Frahm Jensen
IPC: B01J7/00 , B01J19/24 , C01C1/04 , C07C29/15 , C07C41/01 , B01J19/00 , C01B3/38 , C10G2/00 , C07C29/151
Abstract: The invention relates to the production of synthesis gas by means of particularly a series arrangement of heat exchange reforming and autothermal reforming stages, in which the heat required for the reforming reactions in the heat exchange reforming stage is provided by hot effluent synthesis gas from the autothermal reforming stage. More particularly, the invention relates to optimisation of the operation and control of an arrangement of heat exchange reforming and autothermal reforming stages and introduction of an additional waste heat boiler.
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公开(公告)号:US10011548B2
公开(公告)日:2018-07-03
申请号:US14422433
申请日:2013-08-14
Applicant: Haldor Topsøe A/S
Inventor: Per Juul Dahl , Janni Østergaard
CPC classification number: C07C41/42 , B01D3/143 , B01J19/24 , B01J2219/00006 , B01J2219/24 , C07C41/09 , C07C43/043
Abstract: The invention provides a process for the production of purified dimethylether (DME). Methanol is dehydrated to provide a first DME-containing product. The first DME-containing product is purified in a two-stage process. The invention also provides an apparatus arranged to carry out said process.
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公开(公告)号:US09988330B2
公开(公告)日:2018-06-05
申请号:US14651083
申请日:2013-12-18
Applicant: Haldor Topsøe A/S
Inventor: Hassan Modarresi , Christian Wix
IPC: C07C29/152 , C07C29/32
CPC classification number: C07C29/152 , C07C29/32 , C07C31/04 , C07C31/08 , C07C31/12
Abstract: In a process for the production of higher alcohols, i.e. C4+ alcohols, from syngas, the syngas is first reacted in a heterogeneous alcohol pre-converter (A) using an alcohol synthesis catalyst, whereby methanol as the main product in a concentration corresponding to or close to the equilibrium concentration is produced. Then the effluent from the pre-converter is mixed with unconverted wet recycle gas and reacted in a heterogeneous reactor for higher alcohols synthesis (B) containing a higher alcohols synthesis catalyst, and finally the effluent from the reactor for higher alcohols synthesis is separated into (i) unconverted syngas, which is recycled to the higher alcohols synthesis reactor, (ii) methanol and light alcohols, which are recycled to the higher alcohols synthesis reactor, and (iii) the final product consisting of higher alcohols.
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公开(公告)号:US09890041B2
公开(公告)日:2018-02-13
申请号:US15039242
申请日:2014-12-11
Applicant: Haldor Topsøe A/S
Inventor: Thomas Sandahl Christensen , Pia Elholm
CPC classification number: C01B3/40 , C01B3/38 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/04 , C01B2203/0495 , C01B2203/062 , C01B2203/1058 , C01B2203/1241 , C01B2203/1247 , C01B2203/1258 , C01B2203/1264 , C01B2203/127 , C01B2203/141 , C01B2203/142 , C01B2203/143 , C01B2203/148 , C01B2203/169 , C10G2/30 , C10L3/103 , C10L2290/541
Abstract: Process for the production of synthesis gas from hydrocarbon feed containing higher hydrocarbons comprising bypassing a portion of the hydrocarbon feed around a first pre-reforming stage and passing the pre-reformed and bypassed portions through at least a second pre-reforming stage.
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