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公开(公告)号:US2459425A
公开(公告)日:1949-01-18
申请号:US46862442
申请日:1942-12-11
申请人: STANDARD OIL DEV CO
发明人: HEMMINGER CHARLES E
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公开(公告)号:US2458109A
公开(公告)日:1949-01-04
申请号:US60745745
申请日:1945-07-27
发明人: SIMPSON THOMAS P
IPC分类号: C10G11/16
CPC分类号: C10G11/16
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公开(公告)号:US2437383A
公开(公告)日:1948-03-09
申请号:US66679646
申请日:1946-05-02
发明人: DALTON SWANTON D
IPC分类号: C10G11/16
CPC分类号: C10G11/16
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公开(公告)号:US2432344A
公开(公告)日:1947-12-09
申请号:US64646846
申请日:1946-02-08
发明人: SINCLAIR EDWARD L
IPC分类号: C10G11/16
CPC分类号: C10G11/16
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公开(公告)号:US2419517A
公开(公告)日:1947-04-22
申请号:US60745845
申请日:1945-07-27
发明人: EASTWOOD SYLVANDER C
IPC分类号: C10G11/16
CPC分类号: C10G11/16
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公开(公告)号:US2390708A
公开(公告)日:1945-12-11
申请号:US48360243
申请日:1943-04-19
申请人: STANDARD OIL DEV CO
发明人: HEMMINGER CHARLES E
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公开(公告)号:US2356611A
公开(公告)日:1944-08-22
申请号:US36767040
申请日:1940-11-28
申请人: KURT PETERS
发明人: KURT PETERS
IPC分类号: C10G11/16
CPC分类号: C10G11/16
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公开(公告)号:US2351214A
公开(公告)日:1944-06-13
申请号:US28854639
申请日:1939-08-05
申请人: HERMANN KAUFMANN , RUDOLF KEINKE
发明人: HERMANN KAUFMANN , RUDOLF KEINKE
IPC分类号: C10G11/16
CPC分类号: C10G11/16
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公开(公告)号:US2246654A
公开(公告)日:1941-06-24
申请号:US31188639
申请日:1939-12-30
申请人: STANDARD OIL CO
发明人: ARVESON MAURLCE H
CPC分类号: C10G11/16 , B01J8/06 , B01J2208/00212 , B01J2208/00221 , B01J2208/0069 , Y10T137/86501
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80.
公开(公告)号:US11306258B2
公开(公告)日:2022-04-19
申请号:US16942350
申请日:2020-07-29
发明人: Musaed Salem Al-Ghrami , Wei Xu , Aaron Chi Akah
摘要: Systems and methods for steam and catalytic cracking of a hydrocarbon inlet stream comprising hydrocarbons. Systems and methods can include a catalyst feed stream, where the catalyst feed stream comprises a fluid and a heterogeneous catalyst, the heterogeneous catalyst operable to catalyze cracking of the hydrocarbons on surfaces of the heterogeneous catalyst a steam feed stream, where the steam feed stream is operable to effect steam cracking of the hydrocarbons, and where the steam feed stream decreases coking of the heterogeneous catalyst; and a downflow reactor, where the downflow reactor is operable to accept and mix the hydrocarbon inlet stream, the catalyst feed stream, and the steam feed stream, where the downflow reactor is operable to produce light olefins by steam cracking and catalytic cracking, and where the downflow reactor is operable to allow the heterogeneous catalyst to flow downwardly by gravity.
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