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公开(公告)号:KR780000228B1
公开(公告)日:1978-07-01
申请号:KR720000870
申请日:1972-06-02
Applicant: HOECHST AG
Inventor: SENNEWALD K , OHORODNIK A , VIERLING H , GEHRMANN K , ERPENBACH H
IPC: B01J27/18 , B01J27/188 , B01J27/192
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公开(公告)号:US3857882A
公开(公告)日:1974-12-31
申请号:US38775473
申请日:1973-08-13
Applicant: HOECHST AG
Inventor: AUER E , VOGT W , GEHRMANN K
IPC: C07C51/00 , C07C51/363 , C07C51/377 , C07C57/54 , C07C67/00
CPC classification number: C07C57/54 , C07C51/377
Abstract: Production of Alpha -chloroacrylic acid. Acrylic acid and chlorine gas are intimately contacted with one another and the resulting crude reaction product, which predominantly consists of 2,3-dichloropropionic acid, is separated into Alpha chloroacrylic acid and hydrogen chloride. To this end, the reaction produce is introduced into a catalyst zone heated to 80* - 160*C and containing one or more known dehydrochlorination catalysts, wherein Alpha -chloroacrylic acid is continuously distilled off under pressures between 10 and 100 mm of mercury.
Abstract translation: 生产α-氯丙烯酸。 丙烯酸和氯气彼此紧密接触,所得粗制反应产物(主要由2,3-二氯丙酸组成)分离成α-氯丙烯酸和氯化氢。 为此,将反应产物引入加热至80-160℃的催化剂区域中,并含有一种或多种已知的脱氯化氢催化剂,其中在10至100mm汞柱之间的压力下连续蒸馏出α-氯代丙烯酸。
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公开(公告)号:SE417791B
公开(公告)日:1981-04-13
申请号:SE7507665
申请日:1975-07-03
Applicant: HOECHST AG
Inventor: OHORODNIK A , MITTLER W , GEHRMANN K , SCHOLZ H , VIERLING H
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公开(公告)号:ZA80167B
公开(公告)日:1981-01-28
申请号:ZA80167
申请日:1980-01-11
Applicant: HOECHST AG
Inventor: OHORODNIK A , GEHRMANN K , AUER E , SCHAEFER S
Abstract: The invention relates to a process permitting the deposition of solid matter in mixtures containing methyldichlorophosphane to be avoided. To this end, the mixture is stabilized by admixing it with phosphoric acid or a soluble compound containing at least one acid group selected from phosphoric acid, phosphonic acid, sulfonic acid, phosphonous acid, thiophosphoric acid or dithiophosphoric acid.
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公开(公告)号:ZA763944B
公开(公告)日:1977-06-29
申请号:ZA763944
申请日:1976-07-02
Applicant: HOECHST AG
Inventor: LOHMAR E , GEHRMANN K , OHORODNIK A , STUTZKE P
Abstract: Beta-halogenoformyl-ethyl phosphinic acid halides of the general formula:
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公开(公告)号:SE7507665L
公开(公告)日:1976-01-07
申请号:SE7507665
申请日:1975-07-03
Applicant: HOECHST AG
Inventor: OHORODNIK A , MILLTER W , GEHRMANN K , SCHOLZ H , VIERLING H
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公开(公告)号:SE372713B
公开(公告)日:1975-01-13
申请号:SE730472
申请日:1972-06-02
Applicant: HOECHST AG
Inventor: OHORODNIK A , GEHRMANN K , SENNEWALD K , ERPENBACH H , VIERLING H
IPC: B01J23/16 , B01J23/88 , B01J27/18 , B01J27/188 , B01J27/192 , B01J37/02 , B01J11/24 , B01J11/46 , B01J11/54
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公开(公告)号:ZA806057B
公开(公告)日:1981-10-28
申请号:ZA806057
申请日:1980-10-01
Applicant: HOECHST AG
Inventor: GEHRMANN K , KUEBBELER H , ERPENBACH H , SCHMITZ K
IPC: C07C53/12 , B01J27/00 , B01J31/00 , C07B61/00 , C07C51/00 , C07C51/54 , C07C51/56 , C07C67/00 , C07C
Abstract: The invention relates to an improved process for making acetic anhydride by reacting methyl acetate and/or dimethylether with carbon monoxide under practically anhydrous conditions, at temperatures of 350 to 575 K., under pressures of 1 to 300 bars, and in the presence of a catalyst system containing noble metals belonging to group VIII of the periodic system of the elements, or compounds thereof, iodine and/or its compounds, and an aliphatic carboxylic acid having 1 to 8 carbon atoms. The improved process is effected in the presence of a catalyst system containing, as additional ingredients, a heterocyclic aromatic compound, in which at least one hetero atom is a quaternary nitrogen atom, or a quaternary organophosphorus compound, and a zirconium compound being soluble in the reaction mixture.
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公开(公告)号:ZA7703919B
公开(公告)日:1979-03-28
申请号:ZA7703919
申请日:1977-06-29
Applicant: HOECHST AG
Inventor: GEHRMANN K , STEIL K , OHORODNIK A , SCHAEFER S
CPC classification number: C07F9/52
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公开(公告)号:SE403096B
公开(公告)日:1978-07-31
申请号:SE7602714
申请日:1976-02-27
Applicant: HOECHST AG
Inventor: SCHEFER S , OHORODNIK A , GEHRMANN K , MAINSKI A
Abstract: Dilute sulfuric acid contaminated with acetic acid and hydrogen chloride is purified with the resultant formation of concentrated sulfuric acid and acetic acid. To this end, the contaminated sulfuric acid is heated in a first step to at most 60 DEG C under 25-30 mm Hg so as to expel all of the hydrogen chloride together with minor proportions of acetic acid and water. In a second step, the sulfuric acid is heated to at most 165 DEG C under 20-25 mm Hg so as to distil off the bulk of acetic acid together with water. In a third step, the sulfuric acid is cooled down to 60 DEG -90 DEG C, diluted with 10-30 wieght % of water with agitation and while cooling is continued. Following this, the sulfuric acid is heated to 160 DEG -165 DEG C under 20-25 mm Hg and thereby freed from the water and residual acetic acid.
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