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公开(公告)号：US3555820A
公开(公告)日：1971-01-19
申请号：US3555820D
申请日：1969-06-03
Applicant: HOECHST AG
Inventor： CRAMER GERHARD , HECK GUNTER , MALOW EGON
CPC classification number: B01D17/0211 , B01D17/042 , B01D19/0057 , B01D21/00 , B01D21/003 , B01D21/0042 , B01D21/009 , B01D21/02
Abstract: A DECANTING APPARATUS WITH HEAT EXCHANGER AND QUIESCENT CHAMBERS IS DESCRIBED. THE INLET CHAMBER IS CONNECTED VIA A PRODUCT CHAMBER OF A SPIRAL HEAT EXCHANGER TO A DISCHARGE CHAMBER DISPOSED ROUND THE HEAT EXCHANGER, THE SAID PRODUCT CHAMBER BEING NARROW AS COMPARED TO ITS HEIGHT AND BEING ARRANGED IN SEVERAL TURNS ROUND THE INLET CHAMBER.
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2.发明授权
公开(公告)号：US3559378A
公开(公告)日：1971-02-02
申请号：US3559378D
申请日：1970-01-12
Applicant: HOECHST AG
Inventor： KRAUSE WALTER , SCHILKEN HARTMUT , HECK GUNTER , MALOW EGON
Abstract: IMPROVEMENT IN THE PROCESS FOR ISOLATING CARBON DIOXIDE AND ACETYLENE FROM CRACKED GASES WHICH SUBSTANTIALLY CONTAIN HYDROGEN, CARBON MONOXIDE, METHANE, CARBON DIOXIDE, ETHYLENE AND ACETYLENE, BY MULTISTAGE WASHINGS USING ACETONE AND DIMETHYLFORMAMIDE AS SOLVENTS.
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公开(公告)号：US3559374A
公开(公告)日：1971-02-02
申请号：US3559374D
申请日：1969-01-21
Applicant: HOECHST AG
Inventor： KRAUSE WALTER , SCHILKEN HARTMUT , HECK GUNTER , MALOW EGON
Abstract: A PROCESS IS DESCRIBED FOR THE ISOLATION OF CARBON DIOXIDE AND ACETYLENE FROM A CRACKED GAS BY MULTISTAGE WASHINGS USING ACETONE AND DIMETHYLFORMAMIDE, WHEREIN THE CRACKED GAS IS FIRST WSASHED WITH ACETON, THEN ACETYLENE, CARBON DIOXIDE AND ETHYLENE ARE EXPELLED FROM THE
ACETONE SOLUTION BY RELEASE FROM PRESSURE AND THE ACETYLENE IS WASHED OUT OF THIS MIXTURE WITH DIMETHYLFORMAMIDE.-
公开(公告)号：AU9014382A
公开(公告)日：1983-05-12
申请号：AU9014382
申请日：1982-11-04
Applicant: HOECHST AG
Inventor： HECK GUNTER , LIENERTH ALADAR , MALOW EGON , SCHWARZ KARL-HEINZ , FAUST UWE
Abstract: A process for continuous rectification of a liquid mixture containing alcohols, particularly a liquid fermate, employs a plurality of distillation columns to which the liquid mixture is fed in parallel, and which have successively reduced operating pressures and temperatures from an initial one to a final one thereof. The top vapor distillate from the higher-pressure columns supplies driving heat to the sumps of the next successively lower-pressure columns. Direct steam at 130 DEG C. to 160 DEG C. is fed to the sump of the column operated at the highest pressure. Direct steam is generated by indirect heat exchange of water with the top vapor withdrawn from the columns, and the resulting direct steam is fed to the sumps of the next-lower-pressure columns. The apparatus can also include a section for the production of absolute alcohol.
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公开(公告)号：AU7095574A
公开(公告)日：1976-01-08
申请号：AU7095574
申请日：1974-07-08
Applicant: HOECHST AG
Inventor： HECK GUNTER , ROSCHER GUNTER , DONTH RUDOLF
Abstract: Water is separated by distillation from organic multiple component mixtures containing at least one component partly miscible with water. The component miscible with water is distilled azeotropically with the water contained in the mixture, the distillate is separated into water and a zeotrope forming agent and the latter is recycled to the distilling column. In the recycling process, one part of the azeotrope forming agent is conducted to the top of the column and the other part is fed into the column at the feed mixture inlet or at a location thereunder.
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Patent Agency Ranking
公开(公告)号：CA846698A
公开(公告)日：1970-07-14
申请号：CA846698D
Applicant: HOECHST AG
Inventor： WALD WALTER , HECK GUNTER , ROSSBERG MANFRED , OESER HANNS-RUDOLF
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公开(公告)号：DE3274809D1
公开(公告)日：1987-02-05
申请号：DE3274809
申请日：1982-11-02
Applicant: HOECHST AG
Inventor： HECK GUNTER , LIENERTH ALADAR DR , MALOW EGON , SCHWARZ KARL-HEINZ , FAUST UWE DR
Abstract: A process for continuous rectification of a liquid mixture containing alcohols, particularly a liquid fermate, employs a plurality of distillation columns to which the liquid mixture is fed in parallel, and which have successively reduced operating pressures and temperatures from an initial one to a final one thereof. The top vapor distillate from the higher-pressure columns supplies driving heat to the sumps of the next successively lower-pressure columns. Direct steam at 130 DEG C. to 160 DEG C. is fed to the sump of the column operated at the highest pressure. Direct steam is generated by indirect heat exchange of water with the top vapor withdrawn from the columns, and the resulting direct steam is fed to the sumps of the next-lower-pressure columns. The apparatus can also include a section for the production of absolute alcohol.
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公开(公告)号：CA885586A
公开(公告)日：1971-11-09
申请号：CA885586D
Applicant: HOECHST AG
Inventor： MALOW EGON , HECK GUNTER , CRAMER GERHARD
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公开(公告)号：CA881673A
公开(公告)日：1971-09-21
申请号：CA881673D
Applicant: HOECHST AG
Inventor： HECK GUNTER , ANDERS ULRICH
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公开(公告)号：AU554008B2
公开(公告)日：1986-08-07
申请号：AU9014382
申请日：1982-11-04
Applicant: HOECHST AG
Inventor： HECK GUNTER , LIENERTH ALADAR , MALOW EGON , SCHWARZ KARL-HEINZ , FAUST UWE
Abstract: A process for continuous rectification of a liquid mixture containing alcohols, particularly a liquid fermate, employs a plurality of distillation columns to which the liquid mixture is fed in parallel, and which have successively reduced operating pressures and temperatures from an initial one to a final one thereof. The top vapor distillate from the higher-pressure columns supplies driving heat to the sumps of the next successively lower-pressure columns. Direct steam at 130 DEG C. to 160 DEG C. is fed to the sump of the column operated at the highest pressure. Direct steam is generated by indirect heat exchange of water with the top vapor withdrawn from the columns, and the resulting direct steam is fed to the sumps of the next-lower-pressure columns. The apparatus can also include a section for the production of absolute alcohol.
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