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公开(公告)号:US10316259B2
公开(公告)日:2019-06-11
申请号:US15120949
申请日:2014-12-23
发明人: Christoph Dittrich , Joris Van Willigenburg , Raúl Velasco Pelaez , Egidius Jacoba Maria Schaerlaeckens , Vijayanand Rajagopalan , Andrew Mark Ward , Arno Johannes Maria Oprins , Ravichander Narayanaswamy
摘要: A process for converting hydrocarbon feedstock into olefins and BTX including feeding a hydrocarbon feedstock to a first hydrocracking unit, feeding effluent from the first hydrocracking unit to a first separation section to be separated, feeding a steam including propane to a dehydrogenation unit, and feeding effluent from the dehydrogenation unit to a second separation section.
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公开(公告)号:US10301561B2
公开(公告)日:2019-05-28
申请号:US15120681
申请日:2014-12-23
发明人: Christoph Dittrich , Joris Van Willigenburg , Raúl Velasco Pelaez , Egidius Jacoba Maria Schaerlaeckens , Andrew Mark Ward , Arno Johannes Maria Oprins , Vijayanand Rajagopalan , Ravichander Narayanaswamy
摘要: A process for converting hydrocarbons into olefins and BTX based on a combination of hydrocracking, thermal and catalytic dehydrogenation.
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公开(公告)号:US20170088496A1
公开(公告)日:2017-03-30
申请号:US15126710
申请日:2015-03-17
CPC分类号: C07C41/14 , B01J19/245 , B01J2219/24 , C07C7/10 , C07C41/06 , C07C41/50 , C07C41/54 , C07C41/60 , C10L1/026 , C10L2200/0476 , C07C43/046 , C07C43/10 , C07C43/135
摘要: A process of generating a glycerol ether is provided. The process includes reacting isobutylene with an alcohol to obtain a tertiary alkyl ether through an etherification reaction and generating a glycerol ether from the tertiary alkyl ether and glycerol through a transetherification reaction, A system for generating a glycerol ether is also provided.
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公开(公告)号:US20160369186A1
公开(公告)日:2016-12-22
申请号:US15120949
申请日:2014-12-23
发明人: Christoph Dittrich , Joris Van Willigenburg , Raúl Velasco Pelaez , Egidius Jacoba Maria Schaerlaeckens , Vijayanand Rajagopalan , Andrew Mark Ward , Amo Johannes Maria Oprins , Ravichander Narayanaswamy
IPC分类号: C10G69/00
CPC分类号: C10G69/00 , C10G69/04 , C10G69/06 , C10G2400/20 , C10G2400/30
摘要: A process for converting hydrocarbon feedstock into olefins and BTX including feeding a hydrocarbon feedstock to a first hydrocracking unit, feeding effluent from the first hydrocracking unit to a first separation section to be separated, feeding a steam including propane to a dehydrogenation unit, and feeding effluent from the dehydrogenation unit to a second separation section.
摘要翻译: 将烃原料转化成烯烃和BTX的方法,包括将烃原料进料到第一加氢裂化装置,将来自第一加氢裂化装置的流出物供给到待分离的第一分离段,将含丙烷的蒸汽供给脱氢装置, 从脱氢装置到第二分离部。
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公开(公告)号:US20170129827A1
公开(公告)日:2017-05-11
申请号:US15323587
申请日:2015-07-02
发明人: Christoph Dittrich
CPC分类号: C07C2/76 , B01J8/001 , B01J8/0403 , B01J8/0419 , B01J8/0457 , B01J8/0492 , B01J8/0496 , B01J2208/00044 , B01J2208/00061 , B01J2208/00176 , B01J2208/00371 , B01J2208/0053 , B01J2208/065 , B01J2219/002 , B01J2219/00202 , B01J2219/00213 , B01J2219/00225 , C07C2527/22 , C07C2529/04 , C07C2529/076 , C07C15/02
摘要: The present invention relates to a process for converting natural gas to higher hydrocarbon(s) including aromatic hydrocarbon(s) in n reaction zones operated in series, wherein m reaction zones are not participating in the conversion process and only (n−m) reaction zones are operated under reaction conditions sufficient to convert at least a portion of said natural gas to an effluent having said higher hydrocarbon(s). An object of the present invention is to provide a process for converting natural gas to higher hydrocarbon(s) including aromatic hydrocarbon(s) wherein a high reactant, i.e. methane, conversion can be achieved.
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公开(公告)号:US10913906B2
公开(公告)日:2021-02-09
申请号:US16061391
申请日:2016-12-12
发明人: Kokil Jain , Christoph Dittrich , Kumar Prashant
摘要: The present invention relates to a process for the separation of aromatic hydrocarbons from a hydrocarbon feed stream comprising contacting a hydrocarbon feed stream with a solvent for aromatics (aromatics solvent) to provide an aromatics-laden solvent stream and subjecting the aromatics-laden solvent stream to solvent regeneration to provide regenerated aromatics solvent and an aromatics stream.
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公开(公告)号:US10344223B2
公开(公告)日:2019-07-09
申请号:US15571599
申请日:2016-05-03
摘要: The invention relates to a process for hydrocracking a feedstream comprising hydrocarbons to obtain BTX in a gas phase hydrocracking reactor system which comprises (i) an upstream end and a downstream end, (ii) a plurality of successive reaction zones distributed along the reactor between the upstream end and the downstream end, wherein each of the reaction zones has a bed of a hydrocracking catalyst contained therein and (iii) a plurality of quench zones, the quench zones being distributed along the reactor and each being situated between successive reaction zones, wherein the process comprises: (a) injecting a first portion of a hydrogen gas into the upstream end and a first portion of a hydrocarbon gas into the upstream end and (b) injecting a second portion of the hydrogen gas into at least one of the quench zones and injecting a second portion of the hydrocarbon gas into at least one of the quench zones, wherein the molar ratio between hydrogen and hydrocarbons entering each of the reaction zones is 1:1 to 4:1, wherein the molar ratio between hydrogen and hydrocarbons entering the reaction zones decreases with the distance of the reaction zone from the upstream end of the reactor.
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公开(公告)号:US20190127646A1
公开(公告)日:2019-05-02
申请号:US15571599
申请日:2016-05-03
CPC分类号: C10G47/18 , B01J8/0492 , B01J8/0496 , B01J29/46 , B01J2208/00371 , C07C4/06 , C07C2521/12 , C07C2529/40 , C07C2529/44 , C10G49/002 , C10G65/10 , C10G2300/1044 , C10G2400/30
摘要: The invention relates to a process for hydrocracking a feedstream comprising hydrocarbons to obtain BTX in a gas phase hydrocracking reactor system which comprises (i) an upstream end and a downstream end, (ii) a plurality of successive reaction zones distributed along the reactor between the upstream end and the downstream end, wherein each of the reaction zones has a bed of a hydrocracking catalyst contained therein and (iii) a plurality of quench zones, the quench zones being distributed along the reactor and each being situated between successive reaction zones, wherein the process comprises: (a) injecting a first portion of a hydrogen gas into the upstream end and a first portion of a hydrocarbon gas into the upstream end and (b) injecting a second portion of the hydrogen gas into at least one of the quench zones and injecting a second portion of the hydrocarbon gas into at least one of the quench zones, wherein the molar ratio between hydrogen and hydrocarbons entering each of the reaction zones is 1:1 to 4:1, wherein the molar ratio between hydrogen and hydrocarbons entering the reaction zones decreases with the distance of the reaction zone from the upstream end of the reactor.
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公开(公告)号:US20190040324A1
公开(公告)日:2019-02-07
申请号:US16061395
申请日:2016-12-06
发明人: Christoph Dittrich
摘要: The present invention relates to a process for converting a feed comprising C2-C4 alkanes to higher hydrocarbon(s) including aromatic hydrocarbon(s) in n reaction zones operated in series, wherein m reaction zones are not participating in the conversion process and only (n-m) reaction zones are operated under reaction conditions sufficient to convert at least a portion of said a feed comprising C2-C4 alkanes to an effluent having said higher hydrocarbon(s). An object of the present invention is to provide a process for converting LPG to higher hydrocarbon(s) including aromatic hydrocarbon(s) wherein a high reactant, i.e. ethane, propane and/or butane, conversion can be achieved.
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公开(公告)号:US10781379B2
公开(公告)日:2020-09-22
申请号:US16061395
申请日:2016-12-06
发明人: Christoph Dittrich
摘要: A process for converting a feed comprising C2-C4 alkanes to higher hydrocarbon(s) including aromatic hydrocarbon(s) in n reaction zones operated in series, wherein m reaction zones are not participating in the conversion process and only (n-m) reaction zones are operated under reaction conditions sufficient to convert at least a portion of said a feed comprising C2-C4 alkanes to an effluent having said higher hydrocarbon(s). An object of the present invention is to provide a process for converting LPG to higher hydrocarbon(s) including aromatic hydrocarbon(s) wherein a high reactant, i.e. ethane, propane and/or butane, conversion can be achieved.
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