-
公开(公告)号：EP3380461B1
公开(公告)日：2019-07-24
申请号：EP16802026.1
申请日：2016-11-25
发明人： HOFEN, Willi , HAAS, Thomas , WÖLL, Wolfgang , KOLBE, Bärbel , DIETZ, Hans-Christian , BRENDEL, Marc , JAEGER, Bernd , BÄRZ, Manfred , KLEIBER, Michael
IPC分类号： C07D301/12 , C07D301/32
-
公开(公告)号：EP3380461A1
公开(公告)日：2018-10-03
申请号：EP16802026.1
申请日：2016-11-25
发明人： HOFEN, Willi , HAAS, Thomas , WÖLL, Wolfgang , KOLBE, Bärbel , DIETZ, Hans-Christian , BRENDEL, Marc , JAEGER, Bernd , BÄRZ, Manfred , KLEIBER, Michael
IPC分类号： C07D301/12 , C07D301/32
CPC分类号： C07D301/12 , B01D3/14 , B01D2257/7022 , B01D2257/80 , B01J23/30 , B01J29/7049 , C07D301/32
摘要： In a process for the epoxidation of propene, comprising the steps of reacting propene with hydrogen peroxide, separating propene oxide and a recovered propene stream from the reaction mixture, separating propane from all or a part of the recovered propene stream in a C3 splitter column, and passing the overhead product stream of the C3 splitter column to the epoxidation step, a propane starting material with a propane fraction of from 0.002 to 0.10 is used, the epoxidation is operated to provide a propane fraction in the reaction mixture of from 0.05 to 0.20 and the C3 splitter column is operated to provide an overhead product stream which comprises a propane fraction of at least 0.04 in order to reduce the size and the energy consumption of the C3 splitter column.
-
公开(公告)号：EP4025550A1
公开(公告)日：2022-07-13
申请号：EP20757309.8
申请日：2020-08-14
-
公开(公告)号：EP4132672A1
公开(公告)日：2023-02-15
申请号：EP21712873.5
申请日：2021-03-23
发明人： KLEIBER, Michael , HOFEN, Willi
-
公开(公告)号：EP2941412B1
公开(公告)日：2018-10-24
申请号：EP13829059.8
申请日：2013-12-20
发明人： KLEIBER, Michael , GNABS, Ulrike , SCHULZE, Joachim , GHANEGAONKAR, Shashank , GEHRKE, Helmut , GAWENDA, Marcel
CPC分类号： C07C51/44 , B01D1/00 , B01D9/00 , B01D15/02 , B01D61/025 , B01D2311/02 , C07C51/43 , C07C51/47 , C07C55/10
-
6.发明授权
公开(公告)号：EP2734276B1
公开(公告)日：2015-05-27
申请号：EP12730806.2
申请日：2012-06-27
发明人： BENJE, Michael , PETERSEN, Sven , KLEIBER, Michael
CPC分类号： B01D1/0058 , B01D1/065 , B01D1/26 , B01D1/28 , C01D1/42 , C07C17/02 , Y02P20/129 , C07C19/045
-
公开(公告)号：EP4025549A1
公开(公告)日：2022-07-13
申请号：EP20726729.5
申请日：2020-05-08
-
公开(公告)号：EP4025548A1
公开(公告)日：2022-07-13
申请号：EP20757272.8
申请日：2020-08-13
IPC分类号： C07C1/04 , C07C1/24 , C07C29/151 , B01J23/75
-
公开(公告)号：EP2941412A2
公开(公告)日：2015-11-11
申请号：EP13829059.8
申请日：2013-12-20
发明人： KLEIBER, Michael , GNABS, Ulrike , SCHULZE, Joachim , GHANEGAONKAR, Shashank , GEHRKE, Helmut , GAWENDA, Marcel
CPC分类号： C07C51/44 , B01D1/00 , B01D9/00 , B01D15/02 , B01D61/025 , B01D2311/02 , C07C51/43 , C07C51/47 , C07C55/10
摘要： The invention relates to a method and a device for separating and purifying carboxylic acids from fermentation broths containing ammonium carboxylic acid salts, the method comprising the following steps, a) removing biomass and any solids present from the fermentation broth, b) producing a solution containing the desired carboxylic acid and an additional solution containing ammonium salts by performing simulated moving bed chromatography (SMB), c) ultra-purifying the solution containing the desired carboxylic acid from step b), d) concentrating the purified carboxylic acid solution from step c), e) crystalizing the concentrated carboxylic acid solution from step d), f) concentrating the additional solution containing ammonium salts from step b), characterized in that, in the concentration in steps d) and f), a combination of reverse osmosis and concentration by evaporation is performed and the vapor from the concentration by evaporation of step f) is fed into the concentration by evaporation from step d).
-
-
-
-
-
-
-
-
搜索结果
9 条记录 (耗时 0.014 秒)
