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公开(公告)号：US3676331A
公开(公告)日：1972-07-11
申请号：US3676331D
申请日：1970-06-19
发明人： PITCHFORD ARMIN C
CPC分类号： C10G45/24
摘要： A method and catalyst for the upgrading of hydrocarbons which employs a multiple component catalyst system to generate hydrogen in situ and to thereby produce, within the hydrocarbons, materials of low molecular weight, and of reduced carbon residue and sulfur content.
摘要翻译： 一种用于升级烃的方法和催化剂，其使用多组分催化剂体系在原位生成氢，并由此在烃内产生低分子量的材料，并且还原碳残余物和硫含量。
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12.发明授权
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公开(公告)号：US2420218A
公开(公告)日：1947-05-06
申请号：US55539444
申请日：1944-09-22
申请人： PURE OIL CO
发明人： AYERS GEORGE W
IPC分类号： C10G45/24
CPC分类号： C10G45/24
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公开(公告)号：US1472882A
公开(公告)日：1923-11-06
申请号：US21571518
申请日：1918-02-06
IPC分类号： C10G45/24
CPC分类号： C10G45/24 , C10G2400/10
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公开(公告)号：US10662383B2
公开(公告)日：2020-05-26
申请号：US16415513
申请日：2019-05-17
发明人： Fanglin Chen , Libin Lei , Tong Liu , Shumin Fang
IPC分类号： C25C7/02 , C10G2/00 , C10G45/24 , C25B3/04 , B01J23/10 , B01J23/78 , C25B15/02 , C25B15/08 , C25B9/10 , B01J23/83 , C07C1/12 , C07C1/10
摘要： A method for generating hydrocarbons using a solid oxide electrolysis cell (SOEC) and a Fischer-Tropsch unit in a single microtubular reactor is described. This method can directly synthesize hydrocarbons from carbon dioxide and water. The method integrates high temperature co-electrolysis of H2O and CO2 and low temperature Fischer-Tropsch (F-T) process in a single microtubular reactor by designation of a temperature gradient along the axial length of the microtubular reactor. In practice, methods disclosed herein can provide direct conversion of CO2 to hydrocarbons for use as feedstock or energy storage.
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16.发明申请公开(公告)号：US20200123459A1
公开(公告)日：2020-04-23
申请号：US16555808
申请日：2019-08-29
IPC分类号： C10G69/14 , B01D3/14 , C10G45/24 , C10G47/02 , C10G7/06 , C10G69/08 , C10G69/06 , C10G67/04 , C10G47/00 , C10G21/00 , C10G9/36
摘要： Process scheme configurations are disclosed that enable conversion of crude oil feeds with several processing units in an integrated manner into petrochemicals. The designs utilize minimum capital expenditures to prepare suitable feedstocks for the steam cracker complex. The integrated process for converting crude oil to petrochemical products including olefins and aromatics, and fuel products, includes mixed feed steam cracking and gas oil steam cracking. Feeds to the mixed feed steam cracker include light products and naphtha from hydroprocessing zones within the battery limits, recycle streams from the C3 and C4 olefins recovery steps, and raffinate from a pyrolysis gasoline aromatics extraction zone within the battery limits. Feeds to the gas oil steam cracker include hydrotreated gas oil range intermediates from the vacuum gas oil hydroprocessing zone. Furthermore, vacuum residue is processed in a solvent deasphalting unit to produce deasphalted oil as additional feed to the gas oil hydroprocessing zone.
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公开(公告)号：US10407630B2
公开(公告)日：2019-09-10
申请号：US15817140
申请日：2017-11-17
IPC分类号： C10G7/00 , C10G7/06 , C10G47/00 , C10G47/32 , C10G69/14 , C10G47/02 , C10G45/24 , B01D3/14 , C10G67/04 , C10G69/06 , C10G69/08 , C10G9/36 , C10G21/00
摘要： Process scheme configurations are disclosed that enable conversion of crude oil feeds with several processing units in an integrated manner into petrochemicals. The designs utilize minimum capital expenditures to prepare suitable feedstocks for the steam cracker complex. The integrated process for converting crude oil to petrochemical products including olefins and aromatics, and fuel products, includes mixed feed steam cracking and gas oil steam cracking. Feeds to the mixed feed steam cracker include light products and naphtha from hydroprocessing zones within the battery limits, recycle streams from the C3 and C4 olefins recovery steps, and raffinate from a pyrolysis gasoline aromatics extraction zone within the battery limits. Feeds to the gas oil steam cracker include hydrotreated gas oil range intermediates from the vacuum gas oil hydroprocessing zone. Furthermore, vacuum residue is processed in a solvent deasphalting unit to produce deasphalted oil as additional feed to the gas oil hydroprocessing zone.
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公开(公告)号：US4888029A
公开(公告)日：1989-12-19
申请号：US203272
申请日：1988-06-07
申请人： Richard H. Shiley , Randall E. Hughes , John R. Webster , Conrad C. Hinckley , Gerald V. Smith , Tomasz Wiltowski
发明人： Richard H. Shiley , Randall E. Hughes , John R. Webster , Conrad C. Hinckley , Gerald V. Smith , Tomasz Wiltowski
CPC分类号： C10G1/00 , C10G45/24 , C10L9/04 , Y10S44/905
摘要： A process for desulfurizing carbonaceous material containing inorganic bound sulfur, organic bound sulfur, or conbinations thereof. The process comprises reacting the carbonaceous material at desulfurization conditions with a hydrogen source material in the presence of a reaction accelerator to enhance production and reactivity of atomic hydrogen supplied by the hydrogen source. The reaction is prefereably carried out in the presence of a flowing reaction medium which carries away hydrogen sulfide products and other volatile desulfurization products separating them from the carbonaceous material.
摘要翻译： 一种含有无机结合硫，有机结合硫或其配合物的含碳材料脱硫的方法。 该方法包括在反应促进剂存在下使脱硫条件下的碳质材料与氢源材料反应，以提高由氢源供应的原子氢的产生和反应性。 反应优选在流动的反应介质存在下进行，该反应介质携带硫化氢产物和将其与碳质材料分离的其它挥发性脱硫产物。
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公开(公告)号：US4439311B1
公开(公告)日：1987-09-22
申请号：US33690082
申请日：1982-01-04
IPC分类号： C10G29/06 , C10G45/24 , C10M175/00 , C10N40/25 , C10N60/02
CPC分类号： C10M175/0016
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公开(公告)号：US3160580A
公开(公告)日：1964-12-08
申请号：US23314962
申请日：1962-10-25
发明人： KARL ACHENBACH , KURT OSTERLOH , WILFRIED ROTHE
CPC分类号： C10K1/20 , C07C7/148 , C07C7/14833 , C07C7/1485 , C07C7/14858 , C07C7/163 , C10G19/00 , C10G45/24 , C07C15/02
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