-
11.
公开(公告)号:US20170136447A1
公开(公告)日:2017-05-18
申请号:US15322486
申请日:2015-06-29
Applicant: SHELL OIL COMPANY
IPC: B01J27/057 , C07C5/48
CPC classification number: B01J27/0576 , B01J23/002 , B01J23/28 , B01J23/92 , B01J27/30 , B01J37/08 , B01J38/04 , B01J38/14 , B01J2523/00 , C07C5/48 , C07C51/16 , C07C2523/20 , C07C2523/22 , C07C2523/28 , C07C2527/057 , Y02P20/52 , Y02P20/584 , C07C11/04 , C07C11/06 , C07C11/08 , C07C53/08 , C07C57/04 , B01J2523/55 , B01J2523/56 , B01J2523/64 , B01J2523/68
Abstract: The invention relates to a process for treatment of a mixed metal oxide catalyst containing molybdenum, vanadium, niobium and optionally tellurium, comprising contacting a gas stream comprising methane, an inert gas or oxygen or any combination of two or more of these with the catalyst, wherein said gas stream comprises 0 to 25 vol. % of an alkane containing 2 to 6 carbon atoms and/or alkene containing 2 to 6 carbon atoms.
-
公开(公告)号:US20240002221A1
公开(公告)日:2024-01-04
申请号:US18254230
申请日:2021-12-16
Applicant: SHELL OIL COMPANY
Inventor: Ronald Jan SCHOONEBEEK , Alouisius Nicolaas Renée BOS , Dominik Johannes Michael UNRUH , Dennis Patrick VAN DER SLOOT
CPC classification number: C01B3/02 , C01B32/40 , C01B2203/0288 , C01B2203/0495 , C01B2203/1205 , C01B2203/0833
Abstract: A method for producing syngas that comprises providing a feed stream comprising H2 and CO2; heating the feed stream in a first heat exchanger to obtain a first heated feed stream; introducing the first heated feed stream into a first RWGS reactor to obtain a first syngas containing stream; cooling the first syngas containing stream in the first heat exchanger against the feed stream to obtain a first cooled syngas stream; separating the first cooled syngas stream in a first gas/liquid separator to obtain a water-enriched stream and a water-depleted syngas stream; heating the water-depleted syngas stream in a second heat exchanger to obtain a heated water-depleted syngas stream; introducing the heated water-depleted syngas stream into a second RWGS reactor to obtain a second syngas containing stream; and cooling the second syngas containing stream in the second heat exchanger against the water-depleted syngas to obtain a cooled syngas product stream.
-
公开(公告)号:US20200223768A1
公开(公告)日:2020-07-16
申请号:US16638944
申请日:2018-08-02
Applicant: SHELL OIL COMPANY
Inventor: Guus VAN ROSSUM , Ronald Jan SCHOONEBEEK , Laura Mariel CALVO , Ivana Daniela ESPOSITO CASSIBBA , Georgios MITKIDIS , Pejman PAJAND , Maria SAN ROMAN MACIA , Peter Anton August KLUSENER
IPC: C07C5/48
Abstract: The invention relates to a process for oxidative dehydrogenation of ethane, comprising the steps of: (a) subjecting a stream comprising ethane to oxidative dehydrogenation conditions; (b) removing water from at least part of the effluent resulting from step (a); (c) optionally removing unconverted oxygen and/or carbon monoxide and/or ycetylene from at least part of the stream comprising ethylene, unconverted ethane, carbon dioxide, optionally unconverted oxygen, optionally carbon monoxide and optionally acetylene resulting from step (b); (d) removing ethylene from at least part of the stream comprising ethylene, unconverted ethane and carbon dioxide resulting from step (b) or (c) by a complexation separation method; (e) partially and selectively removing carbon dioxide from at least part of the stream comprising unconverted ethane and carbon dioxide resulting from step (d); (f) recycling at least part of the stream comprising unconverted ethane and carbon dioxide resulting from step (e) to step (a).
-
公开(公告)号:US20190248716A1
公开(公告)日:2019-08-15
申请号:US16319933
申请日:2017-07-24
Applicant: SHELL OIL COMPANY
Abstract: Processes and associated reaction systems for the oxidative dehydrogenation of ethane are provided. In particular, a process is provided that comprises supplying a feed gas comprising ethane and oxygen to a multitubular fixed-bed reactor, allowing the ethane and oxygen to react in the presence of an oxidative dehydrogenation catalyst to yield a reactor effluent comprising ethylene; supplying a coolant to an upstream region of an interior shell space of the reactor in a flow pattern that is counter-current with the flow of the feed gas; and withdrawing the coolant from the upstream region and supplying at least a portion of the coolant withdrawn from the upstream region to the downstream region in a flow pattern that is co-current with the flow of the feed gas.
-
公开(公告)号:US20190055176A1
公开(公告)日:2019-02-21
申请号:US15770522
申请日:2016-10-25
Applicant: SHELL OIL COMPANY
Inventor: Georgios MITKIDIS , Maria SAN ROMAN MACIA , Guus VAN ROSSUM , Ronald Jan SCHOONEBEEK
CPC classification number: C07C5/48 , C07C7/04 , C07C7/11 , C07C51/215 , C07C51/25 , C07C51/48 , C07C2523/18 , C07C2523/20 , C07C2523/22 , C07C2523/28 , C07C2527/00 , C07C2527/057 , C07C9/06 , C07C11/04 , C07C53/08
Abstract: The invention concerns a process for oxidative dehydrogenation of ethane. In the process an ethane comprising stream is fed to a distillation column to remove propane. The purified ethane stream is subjected to oxidative dehydrogenation using a catalyst comprising Mo/V/Sb, or Mo/V/Nb and Te or Sb in the orthorhombic M1 crystalline phase. The reactor effluent comprises ethylene. The effluent is washed with water to remove acetic acid. The acetic acid is recovered from the aqueous stream by means of solvent extraction.
-
公开(公告)号:US20170137347A1
公开(公告)日:2017-05-18
申请号:US15322479
申请日:2015-06-29
Applicant: SHELL OIL COMPANY
Inventor: Alouisius Nicolaas Renée BOS , Ronald Jan SCHOONEBEEK , Frank SPIES , Michiel Johannes F. M. VERHAAK
CPC classification number: C07C5/48 , B01J27/0576 , B01J35/023 , B01J35/026 , B01J37/0036 , B01J37/0236 , B01J37/031 , B01J37/04 , B01J37/06 , B01J37/08 , B01J2523/00 , C07C2523/28 , C07C2523/847 , C07C2527/057 , Y02P20/52 , C07C11/04 , B01J2523/55 , B01J2523/56 , B01J2523/64 , B01J2523/68
Abstract: The invention relates to a process of the oxidative dehydrogenation of an alkane containing 2 to 6 carbon atoms and/or the oxidation of an alkene containing 2 to 6 carbon atoms, comprising contacting a first gas stream comprising oxygen and the alkane containing 2 to 6 carbon atoms and/or the alkene containing 2 to 6 carbon atoms with a mixed metal oxide catalyst containing molybdenum, vanadium, niobium and optionally tellurium; followed by contacting a second gas stream comprising methane, an inert gas or oxygen or any combination of two or more of these with the catalyst, wherein the second gas stream comprises 0 to 25 vol. % of the alkane containing 2 to 6 carbon atoms and/or alkene containing 2 to 6 carbon atoms.
-
17.
公开(公告)号:US20160304432A1
公开(公告)日:2016-10-20
申请号:US15101034
申请日:2014-12-04
Applicant: SHELL OIL COMPANY
Inventor: Alouisius Nicolaas Renée BOS , Ronald Jan SCHOONEBEEK , Michiel Johannes Franciscus Maria VERHAAK
CPC classification number: C07C51/25 , B01J27/0576 , B01J35/023 , B01J37/0036 , B01J37/0236 , B01J37/031 , B01J2523/00 , C07C5/48 , C07C51/252 , C07C2523/20 , C07C2523/22 , C07C2523/28 , C07C2527/057 , Y02P20/52 , C07C11/04 , C07C11/06 , C07C53/08 , C07C57/04 , B01J2523/55 , B01J2523/56 , B01J2523/64 , B01J2523/68
Abstract: The invention relates to a process of the oxidative dehydrogenation of an alkane containing 2 to 6 carbon atoms and/or the oxidation of an alkene containing 2 to 6 carbon atoms, wherein a gas stream comprising oxygen and the alkane and/or alkene is contacted with a mixed metal oxide catalyst containing molybdenum, vanadium, niobium and optionally tellurium, and wherein the linear velocity of said gas stream is at least 10 cm/sec.
Abstract translation: 本发明涉及含有2至6个碳原子的烷烃和/或含2至6个碳原子的烯烃的氧化的氧化脱氢方法,其中包含氧气和烷烃和/或烯烃的气流与 含有钼,钒,铌和任选的碲的混合金属氧化物催化剂,并且其中所述气流的线速度为至少10cm / sec。
-
公开(公告)号:US20210130309A1
公开(公告)日:2021-05-06
申请号:US17045807
申请日:2019-04-04
Applicant: SHELL OIL COMPANY
Inventor: Guus VAN ROSSUM , Ivana Daniela ESPOSITO CASSIBBA , Ronald Jan SCHOONEBEEK , Alouisius Nicolaas Renée BOS , Peter Alexander SCHUT , Laura Mariel CALVO
IPC: C07D301/06 , C07C5/48 , C07C29/10
Abstract: The invention relates to a Process for the production of ethylene oxide, comprising the steps of: (a) producing ethylene by subjecting a stream comprising ethane to oxidative dehydrogenation conditions, resulting in a stream comprising ethylene, ethane, water and acetic acid; (b) separating at least part of the stream resulting from step (a) into a stream comprising ethylene and ethane and a stream comprising water and acetic acid; (c) producing ethylene oxide by subjecting ethylene and ethane from the stream comprising ethylene and ethane resulting from step (b) to oxidation conditions, resulting in a stream comprising ethylene oxide, ethylene, ethane and water; (d) separating at least part of the stream resulting from step (c) into a stream comprising ethylene and ethane and a stream comprising ethylene oxide and water; (e) recycling ethylene and ethane from the stream comprising ethylene and ethane resulting from step (d) to step (a), wherein carbon dioxide is produced in steps (a) and (c) and is removed in an additional step between steps (b) and (c) and/or between steps (d) and (e).
-
公开(公告)号:US20200223769A1
公开(公告)日:2020-07-16
申请号:US16638955
申请日:2018-08-02
Applicant: SHELL OIL COMPANY
Inventor: Laura Mariel CALVO , Ivana Daniela ESPOSITO CASSIBBA , Georgios MITKIDIS , Pejman PAJAND , Guus VAN ROSSUM , Maria SAN ROMAN MACIA , Ronald Jan SCHOONEBEEK , Peter Anton August KLUSENER
IPC: C07C5/48
Abstract: The invention relates to a process for oxidative dehydrogenation of ethane, comprising the steps of: (a) subjecting a stream comprising ethane to oxidative dehydrogenation conditions; (b) removing water from at least part of the effluent resulting from step (a); (c) optionally removing unconverted oxygen and/or carbon monoxide and/or acetylene from at least part of the stream comprising ethylene, unconverted ethane, carbon dioxide, optionally unconverted oxygen, optionally carbon monoxide and optionally acetylene resulting from step (b); (d) removing ethylene from at least part of the stream comprising ethylene, unconverted ethane and carbon dioxide resulting from step (b) or (c) by a complexation separation method; (e) partially and selectively removing carbon dioxide from at least part of the stream comprising unconverted ethane and carbon dioxide resulting from step (d); (f) recycling at least part of the stream comprising unconverted ethane and carbon dioxided resulting from step (e) to step (a).
-
公开(公告)号:US20200002251A1
公开(公告)日:2020-01-02
申请号:US16486535
申请日:2018-02-20
Applicant: SHELL OIL COMPANY
Inventor: Georgios MITKIDIS , Guus VAN ROSSUM , Maria SAN ROMAN MACIA , Ronald Jan SCHOONEBEEK , Michael Johannes Franciscus Maria VERHAAK
Abstract: The invention relates to a process for the production of an alkene by alkane oxidative dehydrogenation, comprising: (a) subjecting a stream comprising an alkane to oxidative dehydrogenation conditions, comprising contacting the alkane with oxygen in the presence of a catalyst comprising a mixed metal oxide, resulting in a stream comprising alkene, unconverted alkane, water, carbon dioxide, unconverted oxygen, carbon monoxide and optionally an alkyne; (b) removing water from at least part of the stream comprising alkene, unconverted alkane, water, carbon dioxide, unconverted oxygen, carbon monoxide and optionally an alkyne resulting from step (a), resulting in a stream comprising alkene, unconverted alkane, carbon dioxide, unconverted oxygen, carbon monoxide and optionally alkyne; (c) removing unconverted oxygen, carbon monoxide and optionally alkyne from at least part of the stream comprising alkene, unconverted alkane, carbon dioxide, unconverted oxygen, carbon monoxide and optionally alkyne resulting from step (b), wherein carbon monoxide and optionally alkyne are oxidized into carbon dioxide, resulting in a stream comprising alkene, unconverted alkane and carbon dioxide; (d) optionally removing carbon dioxide from at least part of the stream comprising alkene, unconverted alkane in and carbon dioxide resulting from step (c), resulting in a stream comprising alkene and unconverted alkane; (e) optionally separating at least part of the stream comprising alkene and unconverted alkane resulting from step (d), into a stream comprising alkene and a stream comprising unconverted alkane; (f) optionally recycling unconverted alkane from at least part of the stream comprising unconverted alkane resulting from step (e), to step (a).
-
-
-
-
-
-
-
-
-