公开(公告)号：WO2021257381A1

公开(公告)日：2021-12-23

申请号：PCT/US2021/036850

申请日：2021-06-10

Applicant: SAUDI ARABIAN OIL COMPANY ,  ARAMCO SERVICES COMPANY

Inventor： HARALE, Aadesh ,  JAMAL, Aqil ,  PAGLIERI, Stephen N. ,  VAN VEEN, Henk ,  SEBASTIANI, Francesco ,  KATIKANENI, Sai P.

IPC: C01B3/38 ,  B01D53/22 ,  B01J8/00 ,  B01J19/24 ,  C01B3/50 ,  C01B32/50 ,  B01D2256/16 ,  B01J19/2475 ,  B01J6/008 ,  B01J8/009 ,  B01J8/0207 ,  B01J8/0214 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/041 ,  C01B2203/0475 ,  C01B2203/085 ,  C01B2203/1035 ,  C01B2203/1058 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/142 ,  C01B3/505

Abstract: A system and method of producing hydrogen, including converting hydrocarbon to methane via steam and pre-reforming catalyst in a pre-reformer, converting the methane to hydrogen and carbon dioxide by steam reforming via a reforming catalyst in a membrane reformer, diffusing through hydrogen through a tubular membrane in the membrane reformer.

公开(公告)号：WO2021250083A1

公开(公告)日：2021-12-16

申请号：PCT/EP2021/065433

申请日：2021-06-09

Applicant: SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. ,  SHELL OIL COMPANY

Inventor： GOSWAMI, Tathagata ,  SCHOUWENAAR, Robert ,  TURLEY, Michael ,  FELSKE, Sven

IPC: C01B3/36 ,  C01B3/48 ,  C01B3/52 ,  B01D53/14 ,  C01B32/50 ,  B01D53/047 ,  B01D2252/20447 ,  B01D2252/20489 ,  B01D2252/2056 ,  B01D2256/22 ,  B01D53/1475 ,  C01B2203/025 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/0877 ,  C01B2203/0894 ,  C01B2203/1241 ,  C01B2203/86

Abstract: The present invention relates to a method for the production of hydrogen. Hydrogen is used in many different chemical and industrial processes. Hydrogen is also an important fuel for future transportation and other uses as it does not generate any carbon dioxide emissions when used. The invention provides for a process for producing hydrogen comprising the steps of partially oxidizing a hydrocarbon to obtain a synthesis gas, providing the synthesis gas to a reactor in which carbon monoxide is converted to carbon dioxide, removing the carbon dioxide to obtain hydrogen. The carbon dioxide is used in a chemical process and/or stored in a geological reservoir.

公开(公告)号：WO2021134034A1

公开(公告)日：2021-07-01

申请号：PCT/US2020/067049

申请日：2020-12-25

Applicant: SAUDI ARABIAN OIL COMPANY ,  ARAMCO SERVICES COMPANY ,  KOREA ADVANCED INSTITUTE OF SCIENCE AND TECHNOLOGY

Inventor： HARALE, Aadesh ,  KATIKANENI, Sai ,  AL-NAIMI, Ahmed ,  MA, Youshan ,  BAE, Joongmyeon

IPC: B01J23/46 ,  B01J23/755 ,  B01J23/10 ,  B01J23/83 ,  B01J23/894 ,  B01J23/94 ,  B01J23/96 ,  B01J35/0013 ,  B01J35/023 ,  B01J35/026 ,  B01J37/08 ,  B01J37/18 ,  B01J38/06 ,  B01J38/10 ,  B63B35/32 ,  B63C7/006 ,  C01B2203/0233 ,  C01B2203/041 ,  C01B2203/1041 ,  C01B2203/1058 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/142 ,  C01B3/38 ,  C01B3/382 ,  C01B3/40 ,  C07C2523/10 ,  C07C2523/46 ,  C07C2523/755 ,  C07C4/06 ,  C10G11/02

Abstract: A method for producing a methane-rich gas from a heavy hydrocarbon feed, the method comprising the steps of introducing the heavy hydrocarbon stream to a catalytic reactor, the catalytic reactor comprising an activated catalyst, the activated catalyst comprising 20 wt% of nickel, 70 wt% of a cerium oxide component, and 10 wt% of a gadolinium oxide component; applying the heavy hydrocarbon stream to the activated catalyst; and producing the methane-rich gas over the activated catalyst, wherein the methane-rich gas is selected from the group consisting of methane, carbon dioxide, carbon monoxide, hydrogen, and combinations of the same.

公开(公告)号：WO2023279034A1

公开(公告)日：2023-01-05

申请号：PCT/US2022/073272

申请日：2022-06-29

Applicant: DO, Robert, T.

Inventor： MOTYCKA, Sylvain André, Luc

IPC: C01B3/56 ,  B01J6/008 ,  C01B2203/0272 ,  C01B2203/042 ,  C01B2203/0861 ,  C01B2203/1241 ,  C01B3/24 ,  C09C1/46 ,  C09C1/485 ,  C09C1/50 ,  C09C1/52 ,  C09C1/54

Abstract: Provided herein are novel devices, systems, and methods of using the same, that enable plasma-enhanced pyrolysis of biogenic waste material comprising pyrolysis systems including primary tuyeres for introduction of natural gas directly to a molten lava bed, one or more plasma torches for introducing inert gas into the system, together with mechanisms for capture and collection of combustion products including, but not limited to, turquoise hydrogen and carbon black.

公开(公告)号：WO2022238672A1

公开(公告)日：2022-11-17

申请号：PCT/GB2022/050998

申请日：2022-04-21

Applicant: JOHNSON MATTHEY DAVY TECHNOLOGIES LIMITED

Inventor： CASSIDY, Paul ,  JANARDHANAN, Madhan

IPC: C07C29/151 ,  C07C29/154 ,  C07C31/04 ,  C01B3/34 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0255 ,  C01B2203/0261 ,  C01B2203/0405 ,  C01B2203/061 ,  C01B2203/1241 ,  C01B2203/127 ,  C01B2203/143 ,  C01B2203/148 ,  C01B3/382 ,  C07C29/1518

Abstract: A process is described for synthesising methanol comprising the steps of: (i) passing a hydrocarbon feedstock to a synthesis gas generation unit to form a synthesis gas containing hydrogen, carbon monoxide, carbon dioxide and steam; (ii) cooling the synthesis gas in one or more stages of heat exchange and recovering a process condensate from the cooled synthesis gas to form a make-up gas having a stoichiometry value R in the range of 1.70 to 1.94; (iii) passing a feed gas comprising the make-up gas to a methanol synthesis unit comprising one or more methanol synthesis reactors containing a copper methanol synthesis catalyst, and; (iv) recovering a purge gas and a crude methanol product from the methanol synthesis unit, wherein a hydrogen- rich gas is recovered from the purge gas and combined with the make-up gas, and a stream of water or steam is added to the feed gas to the methanol synthesis unit.

公开(公告)号：WO2021248019A1

公开(公告)日：2021-12-09

申请号：PCT/US2021/035932

申请日：2021-06-04

Applicant: TECHNIP PROCESS TECHNOLOGY, INC.

Inventor： MILLS, Kevin J.

IPC: C07C1/20 ,  C07C9/22 ,  C10G1/06 ,  C01B2203/0233 ,  C01B2203/1241 ,  C01B3/34 ,  C10B47/00 ,  C10B49/02 ,  C10B51/00 ,  C10B53/02

Abstract: A process for converting lignocellulosic feedstock includes providing a lignocellulosic feedstock into a first inlet of a first reactor at a first end, and providing a hot feedstock into a second inlet of the first reactor at a second end of the first reactor. The process includes heating and reacting the lignocellulosic feedstock with the hot feedstock and outputting a first product stream from a first product outlet of the first reactor. The first product stream is an alkane rich product stream. A reactor system includes a first reactor having a first inlet at a first end, a second inlet at a second end and at least one product outlet. The first reactor is configured to receive a lignocellulosic feedstock at the first inlet and a hot feedstock at the second inlet. The system includes a second reactor having a first inlet downstream from the at least one product outlet.

公开(公告)号：WO2021133661A1

公开(公告)日：2021-07-01

申请号：PCT/US2020/065932

申请日：2020-12-18

Applicant: SAUDI ARABIAN OIL COMPANY ,  ARAMCO AMERICAS

Inventor： ALSOLAMI, Bandar H. ,  JAMAL, Aqil

IPC: C10K3/06 ,  C01B3/38 ,  C25B1/04 ,  C10G2/00 ,  C01B3/04 ,  C01B2203/0238 ,  C01B2203/0244 ,  C01B2203/062 ,  C01B2203/1094 ,  C01B2203/1241 ,  C01B2203/14 ,  C01B3/382 ,  C01B3/384 ,  C01B3/40 ,  C10G2/33 ,  C10G2/332 ,  C10G2/333 ,  C10G2/341 ,  C10G2400/10 ,  C25B15/081

Abstract: A system and method for converting (dry reforming) natural gas (methane) and carbon dioxide via reformer catalyst in a dry reformer into syngas including carbon monoxide and hydrogen, and discharging the syngas to a Fischer-Tropsch (FT) reactor. Supplemental hydrogen is generated via water electrolysis and added to the syngas in route to the FT reactor to increase the molar ratio of hydrogen to carbon monoxide in the syngas. The syngas may be converted via FT catalyst in the FT reactor into FT waxes.

公开(公告)号：WO2022266337A1

公开(公告)日：2022-12-22

申请号：PCT/US2022/033815

申请日：2022-06-16

Applicant: OHMIUM INTERNATIONAL, INC.

Inventor： BALLANTINE, Arne ,  KARUPPAIAH, Chockkalingam ,  AGHATEHRANI, Rasool ,  WORSTER, Roby ,  MUELLER, Celeste

IPC: H01M8/04 ,  C01B3/02 ,  F17D3/01 ,  H01M8/00 ,  B01J2204/005 ,  B01J4/001 ,  C01B2203/0233 ,  C01B2203/1241 ,  C01B3/34 ,  C25B1/02 ,  G05D16/204

Abstract: Provided herein are systems and methods for generating gas and delivering the gas at multiple output pressures. The system includes a plurality of gas generators and a plurality of applications, each application having a different header pressure. A plurality of header valves directs the gas flow to the plurality of applications such that energy loss is minimized.

公开(公告)号：WO2022213056A1

公开(公告)日：2022-10-06

申请号：PCT/US2022/071388

申请日：2022-03-28

Applicant: UOP LLC

Inventor： CRUZ, Addison ,  RUSSELL, Bradley ,  BENNETT III, Erick J. ,  CADY, William ,  KRAUS, Kurt ,  BIETTO, Stefano ,  CUELLAR, Kyle ,  KAYODE, Oluwaseyi

IPC: C01B3/56 ,  C01B3/34 ,  C01B3/12 ,  B01D2256/16 ,  B01D2256/22 ,  B01D2257/102 ,  B01D2257/108 ,  B01D2257/11 ,  B01D2257/502 ,  B01D2257/504 ,  B01D2257/7025 ,  B01D2257/80 ,  B01D2259/40015 ,  B01D2259/4003 ,  B01D2259/40043 ,  B01D2259/40079 ,  B01D2259/40081 ,  B01D2259/402 ,  B01D3/143 ,  B01D53/0438 ,  B01D53/047 ,  B01D53/26 ,  C01B2203/0233 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/042 ,  C01B2203/0833 ,  C01B2203/1241 ,  C01B2203/1288 ,  C01B2203/148 ,  C01B2203/1628 ,  C01B3/382 ,  C01B3/386 ,  C01B3/48 ,  C01B3/508 ,  C01B32/50

Abstract: A process and apparatus for producing a hydrogen-enriched product and recovering CO2 from an effluent stream from a hydrogen production unit are described. The effluent from the hydrogen production unit, which comprises a mixture of gases comprising hydrogen, carbon dioxide, water, and at least one of methane, carbon monoxide, nitrogen, and argon, is sent to a PSA system that produces at least two product streams for separation. The PSA system that produces at least two product streams separates the gas mixture into a high- pressure hydrogen stream enriched in hydrogen, optionally a second gas stream containing the majority of the impurities, and a low-pressure tail gas stream enriched in CO2 and some impurities. The CO2-rich tail gas stream is compressed and sent to a CO2 recovery unit, where a CO2-enriched stream is recovered. The CO2-depleted overhead gas stream is recycled to the PSA system that produces at least two product streams.

公开(公告)号：WO2022010967A1

公开(公告)日：2022-01-13

申请号：PCT/US2021/040615

申请日：2021-07-07

Applicant: PROTEUM ENERGY, LLC

Inventor： KENNON, Robert Terry ,  HOAGLAN, Dean C. ,  JOHNSON, Scott V. ,  RAPIER, Charles Robert ,  DELFIN, Karen Lizeth

IPC: C07C4/06 ,  C01B3/38 ,  C07C4/02 ,  C10L3/06 ,  C10L3/08 ,  C10L3/10 ,  C01B2203/0233 ,  C01B2203/0277 ,  C01B2203/0495 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/1276 ,  C01B2203/1294 ,  C01B2203/142 ,  C01B2203/145 ,  C01B2203/148 ,  C01B3/26 ,  C01B3/346 ,  C01B3/382

Abstract: The disclosure relates to methods, systems, and apparatus arranged and designed for converting non-methane hydrocarbon gases into multiple product gas streams including a predominately hydrogen gas stream and a predominately methane gas steam. Hydrocarbon gas streams are reformed, cracked, or converted into a synthesis gas stream and methane gas stream by receiving a volume of flare gas or other hydrocarbon liquid or gas feed, where the volume of hydrocarbon feed includes a volume of methane and a volume of nonmethane hydrocarbons. The hydrogen contained in the syngas may be separated into a pure hydrogen gas stream. A corresponding gas conversion system can include a super heater to provide a hydrocarbon feed/steam mixture, a heavy hydrocarbon reactor for synthesis gas formation, and a hydrogen separator to recover the hydrogen portion of the synthesis gas.