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公开(公告)号:US3882178A
公开(公告)日:1975-05-06
申请号:US38686173
申请日:1973-08-09
Applicant: HOECHST AG
Inventor: BENNINGER SIEGFRIED , REBSDAT SIEGFRIED , KOHLHAAS RUDOLF
Abstract: Tetrafluoro-ethylene can be added to monoamines having oxyethyl or oxypropyl groups in aprotic polar solvents in the presence of alkali metals. The new monoamines obtained having the radicals tetrafluoro-ethyloxy-ethyl or tetrafluoro-ethyl-oxy-propyl are electrolyzed in anhydrous hydrofluoric acid, thus forming new monoamines in which all or nearly all hydrogen atoms of the starting compounds are replaced by fluorine.
Abstract translation: 在碱金属存在下,四氟乙烯可以加入非质子极性溶剂中具有氧乙基或氧丙基的单胺。 获得的具有四氟乙氧基 - 乙基或四氟 - 乙基 - 氧基 - 丙基基团的新单胺在无水氢氟酸中电解,从而形成新的单胺,其中起始化合物的全部或几乎全部氢原子被氟取代。
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公开(公告)号:US3891625A
公开(公告)日:1975-06-24
申请号:US38685673
申请日:1973-08-09
Applicant: HOECHST AG
Inventor: BENNINGER SIEGFRIED , REBSDAT SIEGFRIED
IPC: C07D211/38 , C07D51/70
CPC classification number: C07D211/38
Abstract: Perfluorinated linear or cyclic oligoamines having ether groups, useful as inert reaction media or as hydraulic liquids, prepared by the electrofluorination, in anhydrous HF, of the addition products formed between hexafluoropropene or tetrafluoroethylene and linear or cyclic oligoamines having nitrogen atoms substituted by oxyalkyl groups.
Abstract translation: 具有醚基团的全氟化线型或环状低聚胺,可用作惰性反应介质或作为液压液体,通过电氟化在无水HF中制备的六氟丙烯或四氟乙烯之间形成的加成产物和具有被烷氧基取代的氮原子的直链或环状低聚胺。
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公开(公告)号:US3882182A
公开(公告)日:1975-05-06
申请号:US38685773
申请日:1973-08-09
Applicant: HOECHST AG
Inventor: BENNINGER SIEGFRIED , MARTINI THOMAS
IPC: A61K31/13 , A61P7/08 , C07C67/00 , C07C213/00 , C07C217/26 , C09K5/08 , C10M105/60 , C10N30/02 , C10N30/10 , C10N70/00 , C25B3/08 , G21C15/28 , H01B1/12 , H01B3/24 , C07C93/02
Abstract: Perfluorinated hydrogen-free amines having side chains which contain ether bonds are formed by the electrolysis, carried out in anhydrous hydrofluoric acid, of the products of addition of hexafluoropropene to amino alcohols.
Abstract translation: 具有含有醚键的侧链的全氟化无氢胺通过在无水氢氟酸中向氨基醇加成六氟丙烯的产物进行电解而形成。
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公开(公告)号:NO161615C
公开(公告)日:1989-09-06
申请号:NO831837
申请日:1983-05-24
Applicant: HOECHST AG
Inventor: HANNESEN KURT , KRAHL FRITZ , STEINROETTER HEINZ , BENNINGER SIEGFRIED
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公开(公告)号:FI72901B
公开(公告)日:1987-04-30
申请号:FI831830
申请日:1983-05-23
Applicant: HOECHST AG
Inventor: HANNESEN KURT , KRAHL FRITZ , STEINROETTER HEINZ , BENNINGER SIEGFRIED
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公开(公告)号:ZA8303722B
公开(公告)日:1985-01-30
申请号:ZA8303722
申请日:1983-05-24
Applicant: HOECHST AG
Inventor: HANNESEN KURT , KRAHL FRITZ , STEINROETTER HEINZ , BENNINGER SIEGFRIED
IPC: C01D1/44 , B01J2/02 , B01J2/04 , B01J19/02 , B05B1/00 , B05B1/14 , B05B3/10 , C01D1/42 , B08B , B05B
CPC classification number: B05B3/1057 , B01J2/04 , B01J19/02 , B01J2219/0204 , B01J2219/0227 , B05B1/14 , B05B3/1021 , C01D1/42
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公开(公告)号:NO831837A
公开(公告)日:1983-11-28
申请号:NO831837
申请日:1983-05-24
Applicant: HOECHST AG
Inventor: HENNESEN KURT , KRAHL FRITZ , STEINROETTER HEINZ , BENNINGER SIEGFRIED
CPC classification number: B05B3/1057 , B01J2/04 , B01J19/02 , B01J2219/0204 , B01J2219/0227 , B05B1/14 , B05B3/1021 , C01D1/42
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公开(公告)号:FI72901C
公开(公告)日:1987-08-10
申请号:FI831830
申请日:1983-05-23
Applicant: HOECHST AG
Inventor: HANNESEN KURT , KRAHL FRITZ , STEINROETTER HEINZ , BENNINGER SIEGFRIED
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公开(公告)号:ZA833722B
公开(公告)日:1985-01-30
申请号:ZA833722
申请日:1983-05-24
Applicant: HOECHST AG
Inventor: HANNESEN KURT , KRAHL FRITZ , STEINROETTER HEINZ , BENNINGER SIEGFRIED
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公开(公告)号:FI64554B
公开(公告)日:1983-08-31
申请号:FI810673
申请日:1981-03-04
Applicant: HOECHST AG
Inventor: BENNINGER SIEGFRIED , REINING KARL , KRASEL WERNER
Abstract: The invention relates to an open dissolving chamber for rock salt and to an apparatus for the production, free from vapors, of concentrated, aqueous sodium chloride crude brine by continuously dissolving rock salt in this dissolving chamber. The dissolving chamber contains a heap of rock salt with which the brine which is unsaturated in respect of salt comes into contact. The brine thereby becomes saturated with sodium chloride and then passes out of the dissolving chamber. In the present apparatus, the unsaturated brine enters at the base of the dissolving chamber. The saturated crude brine is removed from the rock salt through at least one vertical or inclined screen which largely holds back suspended rock salt particles. The liquid level of the saturated crude brine in the dissolving chamber should not reach the surface of the heap of rock salt, and the side of the screen facing the interior of the dissolving chamber should be completely covered with a mixture of saturated crude brine and rock salt.
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