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公开(公告)号:KR840001470B1
公开(公告)日:1984-09-28
申请号:KR800003042
申请日:1980-07-30
Applicant: STANDARD OIL CO
Inventor: LANDIS NORRIS J
IPC: C07C255/08 , B01D20060101 , B01D3/00 , B01D3/10 , B01D3/40 , C07C20060101 , C07C67/00 , C07C253/00 , C07F3/00 , C08F120/44 , C07C121/32
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公开(公告)号:CA1134863A
公开(公告)日:1982-11-02
申请号:CA350481
申请日:1980-04-23
Applicant: STANDARD OIL CO OHIO
Inventor: LANDIS NORRIS J
IPC: C07C255/08 , B01D20060101 , B01D3/00 , B01D3/10 , B01D3/40 , C07C20060101 , C07C67/00 , C07C253/00 , C07F3/00 , C08F120/44 , C07C121/32
Abstract: (5150) ACRYLONITRILE PURIFICATION A method for purifying acrylonitrile resulting in capital and operating cost savings consists of distilling a solution of acrylonitrile and impurities in a distillation column under vacuum, and removing the purified acrylonitrile as a vaporous sidestream from the column.
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公开(公告)号:CS228134B2
公开(公告)日:1984-05-14
申请号:CS536380
申请日:1980-07-31
Applicant: STANDARD OIL CO OHIO
Inventor: LANDIS NORRIS J
IPC: C07C255/08 , B01D20060101 , B01D3/00 , B01D3/10 , B01D3/40 , C07C20060101 , C07C67/00 , C07C253/00 , C07F3/00 , C08F120/44 , C07C121/32
Abstract: A process for separating acrylonitrile from a solution containing acrylonitrile, water and impurities. Conventionally such a solution is fed to a drying column and then to a product column. The need for a drying column, by feeding the solution direct to a product column is eliminated. In an embodiment an overhead stream from a recovery column (118) is fed to an HCN column (126) for removal of HCN. The solution is then fed to the top a product column (150) which contains between 30 and 60 trays, a sidestream of purified acrylonitrile being removed through a line (159) located in the lower part of the column.
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公开(公告)号:RO80861A
公开(公告)日:1983-02-01
申请号:RO10186480
申请日:1980-08-01
Applicant: STANDARD OIL CO OHIO
Inventor: LANDIS NORRIS J
IPC: B01D20060101 , C07C255/08 , B01D3/00 , B01D3/10 , B01D3/40 , C07C20060101 , C07C67/00 , C07C253/00 , C07F3/00 , C08F120/44 , C07C121/32
Abstract: A process for separating acrylonitrile from a solution containing acrylonitrile, water and impurities. Conventionally such a solution is fed to a drying column and then to a product column. The need for a drying column, by feeding the solution direct to a product column is eliminated. In an embodiment an overhead stream from a recovery column (118) is fed to an HCN column (126) for removal of HCN. The solution is then fed to the top a product column (150) which contains between 30 and 60 trays, a sidestream of purified acrylonitrile being removed through a line (159) located in the lower part of the column.
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