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1. 发明申请

WO2017223338A1 PROCESS FOR THE DEHYDROCHLORINATION OF A CHLOROALKANE 审中-公开
标题翻译：氯代烷的脱氢氯化方法
公开(公告)号：WO2017223338A1
公开(公告)日：2017-12-28
申请号：PCT/US2017/038792
申请日：2017-06-22
申请人： BLUE CUBE IP LLC
发明人： MYERS, John D. , TIRTOWIDJOJO, Max
IPC分类号： C07C17/04 , C07C17/25 , C07C19/01 , C07C21/04 , C07C21/073 , C07C21/10
CPC分类号： C07C17/25 , B01J27/10 , C07C17/04 , Y02P20/127 , C07C21/04
摘要： A process for the production of a chloroalkene that includes contacting a liquid phase chloroalkane with a solid catalyst, a catalyst deposited on a solid substrate, or combinations thereof, thereby causing the dehydrochlorination of the chloroalkane to produce a chloroalkene product and HCl. Processes for the production of 1,1,2,3-tetrachloropropene and 1,1,1,2,3-pentachloropropane are further provided.
摘要翻译：生产氯代烯烃的方法，其包括使液相氯代烷烃与固体催化剂，沉积在固体基质上的催化剂或其组合接触，由此引起氯代烷烃脱氯化氢以产生氯烯烃产物和HCl。进一步提供了生产1,1,2,3-四氯丙烯和1,1,1,2,3-五氯丙烷的方法。

2. 发明申请

WO02049957A1 HYDROGEN GENERATING SYSTEM AND HYDRODEHALOGENATION METHOD 审中-公开
标题翻译：氢发生系统和氢化方法
公开(公告)号：WO02049957A1
公开(公告)日：2002-06-27
申请号：PCT/FR2001/004171
申请日：2001-12-21
IPC分类号： A62D3/37 , A62D101/22 , B01J23/42 , C01B3/08 , C07B35/02 , C07B35/06 , C07C21/10
CPC分类号： A62D3/37 , A62D2101/22 , C01B3/08 , Y02E60/36
摘要： The invention concerns a hydrogen generating system, characterised in that it combines a water-corrodible metal, an inorganic material, said material having a specific surface capable of fixing the oxide and/or hydroxide form(s) of said metals generated during corrosion. The invention also concerns a method for generating hydrogen and its uses, in particular in a hydrodehalogenation process of halogenated organic compounds present in aqueous media to be purified.
摘要翻译：本发明涉及一种氢气发生系统，其特征在于它结合了水可腐蚀金属，无机材料，所述材料具有能够固化在腐蚀过程中产生的所述金属的氧化物和/或氢氧化物形式的比表面。本发明还涉及产生氢气的方法及其用途，特别是在待纯化的水性介质中存在的卤代有机化合物的加氢脱卤过程中。

3. 发明申请

WO2012121876A3 AZEOTROPE AND AZEOTROPE-LIKE COMPOSITIONS USEFUL FOR THE PRODUCTION OF HALOOLEFINS 审中-公开
公开(公告)号：WO2012121876A3
公开(公告)日：2012-09-13
申请号：PCT/US2012/025908
申请日：2012-02-21
申请人： HONEYWELL INTERNATIONAL INC. , HULSE, Ryan , PHAM, Hang T. , TUNG, Hsueh Sung , POKROVSKI, Konstantin A. , MERKEL, Daniel C.
发明人： HULSE, Ryan , PHAM, Hang T. , TUNG, Hsueh Sung , POKROVSKI, Konstantin A. , MERKEL, Daniel C.
IPC分类号： C01B7/19 , C07C21/18 , C07C21/10 , C07C19/08
摘要： The present invention pertains to ternary azeotrope and azeotrope-like composition including 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf), HF, and either 1,1,2,3-tetrachloropropene (TCP) or 1,1,1,2,2-pentafluoropropane (HFC-245cb). The present invention also relates to binary azeotropes of 2,3,3,3-tetrachloropropene and HF. Such azeotropic and azeotrope-like compositions are useful as intermediates in the production of 2,3,3,3- tetrafluoropropene (HFO-1234yf).

4. 发明申请

WO2007094965A1 INTEGRATED PROCESS FOR PRODUCING 1,2-DICHLOROETHYLENE 审中-公开
标题翻译：用于生产1,2-二氯乙烯的一体化方法
公开(公告)号：WO2007094965A1
公开(公告)日：2007-08-23
申请号：PCT/US2007/002582
申请日：2007-01-30
申请人： PPG INDUSTRIES OHIO, INC.
发明人： SCROGGINS, Jonathan W.
IPC分类号： C07C17/154 , C07C21/073 , C07C17/25 , C07C21/10 , C07C21/12 , C07C4/04
CPC分类号： C07C21/08 , C07C17/158 , C07C17/25 , Y02P20/125
摘要： Describes an integrated process for preparing 1,2-dichloroethylenes. In the described process organic feed material, e.g., C2 - C4 aliphatic hydrocarbons and/or chlorinated derivatives of such aliphatic hydrocarbons, is introduced into a first reaction zone 10, e.g., a chlorination zone such as an oxychlorination zone, or a thermal cracking zone; first product effluent from the first reaction zone is forwarded to a second reaction zone 9; trichloroethane is introduced into the second reaction zone and into heat exchange contact with the first product effluent from the first reaction zone, which has a heat content sufficient to cause thermal dehydrochlorination of trichloroethane in the second reaction zone; and second product effluent is removed from the second reaction zone. 1,2-dichloroethylene is recovered by conventional distillation recovery methods from the second product effluent.
摘要翻译：描述了制备1,2-二氯乙烯的综合方法。在所述方法中，将有机原料（例如C 2 -C 4脂族烃和/或这些脂族烃的氯化衍生物）引入第一反应区10，例如氯化区如氧氯化区或热裂解区 ; 来自第一反应区的第一产物流出物被转送到第二反应区9; 将三氯乙烷引入第二反应区并与来自第一反应区的第一产物流出物进行热交换接触，第一反应区的热含量足以在第二反应区引起三氯乙烷的热脱氯化氢; 并且从第二反应区域除去第二产物流出物。通过常规蒸馏回收方法从第二产物流出物回收1,2-二氯乙烯。

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