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公开(公告)号:ES2144100T3
公开(公告)日:2000-06-01
申请号:ES95304532
申请日:1995-06-27
Applicant: STANDARD OIL CO OHIO
Inventor: MCDONEL TIMOTHY R , RINKER JEFFREY E , REILING VINCENT G , SARNA JOSEPH C
IPC: B01J8/24 , B01J12/02 , C01C3/02 , C07C253/24 , C07C253/26 , C07C253/34 , C07C255/08
Abstract: Redn. in the amt. of unreacted ammonia exiting the reactor in acrylonitrile mfr., comprises: (a) contacting with a fluid bed catalyst, in the lower portion of a fluid bed reactor, ammonia, O2 and a hydrocarbon comprising propylene or propane, to produce acrylonitrile; (b) feeding O2 free of any oxygenate cpds. into the upper portion of the fluid bed reactor, at a point where the additional O2 does not affect the reaction, but reacts with at least some of the unreacted ammonia; (c) cooling the reactor effluent contg. acrylonitrile by feeding into a water quench column; (d) removing unwanted impurities; and (e) recovering acrylonitrile from the quench column.
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公开(公告)号:ZA9504931B
公开(公告)日:1996-02-07
申请号:ZA9504931
申请日:1995-06-14
Applicant: STANDARD OIL CO OHIO
Inventor: REILING VINCENT G , RINKER JEFFREY E , MCDONEL TIMOTHY R , SARNA JOSEPH C
IPC: B01J8/24 , B01J12/02 , C01C3/02 , C07C253/24 , C07C253/26 , C07C253/34 , C07C255/08 , C07C
CPC classification number: C07C253/24 , C07C253/26 , Y02P20/52 , C07C255/08
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公开(公告)号:BR9503515A
公开(公告)日:1996-06-04
申请号:BR9503515
申请日:1995-08-01
Applicant: STANDARD OIL CO OHIO
Inventor: REILING VINCENT G , RINKER JEFFREY E , MCDONEL TIMOTHY R , SARNA JOSEPH C
IPC: B01J8/24 , B01J12/02 , C01C3/02 , C07C253/24 , C07C253/26 , C07C253/34 , C07C255/08 , C01C1/10
Abstract: Redn. in the amt. of unreacted ammonia exiting the reactor in acrylonitrile mfr., comprises: (a) contacting with a fluid bed catalyst, in the lower portion of a fluid bed reactor, ammonia, O2 and a hydrocarbon comprising propylene or propane, to produce acrylonitrile; (b) feeding O2 free of any oxygenate cpds. into the upper portion of the fluid bed reactor, at a point where the additional O2 does not affect the reaction, but reacts with at least some of the unreacted ammonia; (c) cooling the reactor effluent contg. acrylonitrile by feeding into a water quench column; (d) removing unwanted impurities; and (e) recovering acrylonitrile from the quench column.
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公开(公告)号:TR9500886A2
公开(公告)日:1996-06-21
申请号:TR9500886
申请日:1995-07-20
Applicant: STANDARD OIL CO OHIO
Inventor: REILING VINCENT G , SARNA JOSEPH C , RINKER JEFREY E , MCDONEL TIMOTHY R
IPC: B01J8/24 , B01J12/02 , C01C3/02 , C07C253/24 , C07C253/26 , C07C253/34 , C07C255/08
CPC classification number: C07C253/24 , C07C253/26 , Y02P20/52 , C07C255/08
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公开(公告)号:TR199500886A2
公开(公告)日:1996-06-21
申请号:TR9500886
申请日:1995-07-20
Applicant: STANDARD OIL CO OHIO
Inventor: REILING VINCENT G , SARNA JOSEPH C , RINKER JEFREY E , MCDONEL TIMOTHY R
IPC: B01J8/24 , B01J12/02 , C01C3/02 , C07C253/24 , C07C253/26 , C07C253/34 , C07C255/08
Abstract: Redn. in the amt. of unreacted ammonia exiting the reactor in acrylonitrile mfr., comprises: (a) contacting with a fluid bed catalyst, in the lower portion of a fluid bed reactor, ammonia, O2 and a hydrocarbon comprising propylene or propane, to produce acrylonitrile; (b) feeding O2 free of any oxygenate cpds. into the upper portion of the fluid bed reactor, at a point where the additional O2 does not affect the reaction, but reacts with at least some of the unreacted ammonia; (c) cooling the reactor effluent contg. acrylonitrile by feeding into a water quench column; (d) removing unwanted impurities; and (e) recovering acrylonitrile from the quench column.
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公开(公告)号:ZA954931B
公开(公告)日:1996-02-07
申请号:ZA954931
申请日:1995-06-14
Applicant: STANDARD OIL CO OHIO
Inventor: REILING VINCENT G , RINKER JEFFREY E , MCDONEL TIMOTHY R , SARNA JOSEPH C
IPC: B01J8/24 , B01J12/02 , C01C3/02 , C07C253/24 , C07C253/26 , C07C253/34 , C07C255/08 , C07C
Abstract: Redn. in the amt. of unreacted ammonia exiting the reactor in acrylonitrile mfr., comprises: (a) contacting with a fluid bed catalyst, in the lower portion of a fluid bed reactor, ammonia, O2 and a hydrocarbon comprising propylene or propane, to produce acrylonitrile; (b) feeding O2 free of any oxygenate cpds. into the upper portion of the fluid bed reactor, at a point where the additional O2 does not affect the reaction, but reacts with at least some of the unreacted ammonia; (c) cooling the reactor effluent contg. acrylonitrile by feeding into a water quench column; (d) removing unwanted impurities; and (e) recovering acrylonitrile from the quench column.
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