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公开(公告)号:RO115052B1
公开(公告)日:1999-10-29
申请号:RO9301169
申请日:1993-08-30
Applicant: DEGUSSA
Inventor: VANHEERTUM RUDOLF , HENDRICX RICHARD , KRIEBITZSCH NORBERT , VAN DE VELDE FRANCOIS , SCHIRRMACHER RUDIGER
IPC: C04B41/48 , C07D251/28
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公开(公告)号:ZA9307106B
公开(公告)日:1994-05-17
申请号:ZA9307106
申请日:1993-09-24
Applicant: DEGUSSA
Inventor: VANHEERTUM RUDOLF , HENDRICX RICHARD , KRIEBITZSCH NORBERT , VELDE FRANCOIS VAN DE , SCHIRRMACHER RUEDIGER
IPC: C04B41/48 , C07D251/28 , C07D
CPC classification number: C07D251/28 , C04B41/4861
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公开(公告)号:HU178914B
公开(公告)日:1982-07-28
申请号:HUDE000914
申请日:1976-05-11
Applicant: DEGUSSA
Inventor: DEVLIES LUC , HENDRICX RICHARD , HENKEL KURT , KRIEBITZSCH NORBERT , PETZOLD MARTIN
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公开(公告)号:HU186283B
公开(公告)日:1985-07-29
申请号:HU193180
申请日:1980-08-01
Applicant: DEGUSSA
Inventor: BITTNER FRIEDRICH , HEIMBERGER WERNER , KRIEBITZSCH NORBERT , HENKEL KURT , PETZOLD MARTIN , PUSCHNER KURT
Abstract: To obtain a cyanogen chloride which is practically free from water and preferably also free from hydrogen cyanide, hydrogen chloride and organic compounds, the crude cyanogen chloride is fractionally distilled. The return is led in countercurrent flow to the crude gas, thereby takes up the impurities and is further evaporated in the lower portion of the column, respectively in a special apparatus, by a liquid whose temperature is higher than the boiling temperature of cyanogen chloride. Thereby this liquid also takes up the impurities. The purification action is aided by a wash for the crude cyanogen chloride connected in series before it enters the fractionating column. It is very advantageous to combine the process with a plant for the production of cyanogen chloride.
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公开(公告)号:RO81945B
公开(公告)日:1983-05-30
申请号:RO10380581
申请日:1981-03-24
Applicant: DEGUSSA
Inventor: KRIEBITZSCH NORBERT , PUSCHNER KURT , HENTSCHEL KLAUS
IPC: B01J8/00 , B01J19/00 , B65G53/08 , C07D251/28
Abstract: Inventia se refera la un procedeu pentru manipularea clorurii de cianuril lichide prin introducerea clorurii de cianuril solide într-o topitura de clorura de cianuril. Procedeul consta în aceea ca, în scopul relizarii unui dop de produs etans, impermeabil la gaze, se introduce clorura de cianuril solida, la temperatura camerei în spatiul de vapori deasupra unei topituri de clorura de cianuril aflata la 170 degree C cu ajutorul unui transportor cu melc care nu mai are elemente elicoidale pe ultima portiune, înainte de intrarea în spatiul de vapori si care poate fi prevazut la capat cu o clapeta încarcata cu o greutate.
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公开(公告)号:RO81945A
公开(公告)日:1983-06-01
申请号:RO10380581
申请日:1981-03-24
Applicant: DEGUSSA
Inventor: KRIEBITZSCH NORBERT , PUSCHNER KURT , HENTSCHEL KLAUS
IPC: B01J8/00 , B01J19/00 , B65G53/08 , C07D251/28
Abstract: Solid cyanuric chloride is supplied to the gas space of a cyanuric chloride melt with the help of a gas tight product stopper. Preferably there is used for this a screw conveyor in which the gas tight stopper is formed at the end of the screw conveyor; it is most favorable if the helix ends before the last section of the tube of the screw conveyor.
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公开(公告)号:FR2465686A1
公开(公告)日:1981-03-27
申请号:FR8015635
申请日:1980-07-15
Applicant: DEGUSSA
Inventor: BITTNER FRIEDRICH , HEIMBERGER WERNER , HENKEL KURT , KRIEBITZSCH NORBERT , PETZOLD MARTIN , PUSCHNER KURT
Abstract: To obtain a cyanogen chloride which is practically free from water and preferably also free from hydrogen cyanide, hydrogen chloride and organic compounds, the crude cyanogen chloride is fractionally distilled. The return is led in countercurrent flow to the crude gas, thereby takes up the impurities and is further evaporated in the lower portion of the column, respectively in a special apparatus, by a liquid whose temperature is higher than the boiling temperature of cyanogen chloride. Thereby this liquid also takes up the impurities. The purification action is aided by a wash for the crude cyanogen chloride connected in series before it enters the fractionating column. It is very advantageous to combine the process with a plant for the production of cyanogen chloride.
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公开(公告)号:IN174699B
公开(公告)日:1995-02-18
申请号:IN379CA1993
申请日:1993-07-02
Applicant: DEGUSSA
Inventor: VANHEERTUM RUDOLF , HENDRICX RICHARD , KRIEBITZSCH NORBERT , VELDE VAN DE FRANCOIS , SCHIRRMACHER RUDIGER
IPC: C01C3/00
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公开(公告)号:ZA937106B
公开(公告)日:1994-05-17
申请号:ZA937106
申请日:1993-09-24
Applicant: DEGUSSA
Inventor: VANHEERTUM RUDOLF , HENDRICX RICHARD , KRIEBITZSCH NORBERT , VELDE FRANCOIS VAN DE , SCHIRRMACHER RUEDIGER
IPC: C04B41/48 , C07D251/28 , C07D
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公开(公告)号:DD152326A5
公开(公告)日:1981-11-25
申请号:DD22294380
申请日:1980-07-29
Applicant: DEGUSSA
Inventor: BITTNER FRIEDRICH , HEIMBERGER WERNER , HENKEL KURT , KRIEBITZSCH NORBERT , PETZOLD MARTIN , PUSCHNER KURT
Abstract: To obtain a cyanogen chloride which is practically free from water and preferably also free from hydrogen cyanide, hydrogen chloride and organic compounds, the crude cyanogen chloride is fractionally distilled. The return is led in countercurrent flow to the crude gas, thereby takes up the impurities and is further evaporated in the lower portion of the column, respectively in a special apparatus, by a liquid whose temperature is higher than the boiling temperature of cyanogen chloride. Thereby this liquid also takes up the impurities. The purification action is aided by a wash for the crude cyanogen chloride connected in series before it enters the fractionating column. It is very advantageous to combine the process with a plant for the production of cyanogen chloride.
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