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Ethene;tetrachloromethane | 25398-31-6

中文名称
——
中文别名
——
英文名称
Ethene;tetrachloromethane
英文别名
ethene;tetrachloromethane
Ethene;tetrachloromethane化学式
CAS
25398-31-6
化学式
C3H4Cl4
mdl
——
分子量
181.9
InChiKey
VITOTSNEZSJYFI-UHFFFAOYSA-N
BEILSTEIN
——
EINECS
——
  • 物化性质
  • 计算性质
  • ADMET
  • 安全信息
  • SDS
  • 制备方法与用途
  • 上下游信息
  • 反应信息
  • 文献信息
  • 表征谱图
  • 同类化合物
  • 相关功能分类
  • 相关结构分类

计算性质

  • 辛醇/水分配系数(LogP):
    3.36
  • 重原子数:
    7
  • 可旋转键数:
    0
  • 环数:
    0.0
  • sp3杂化的碳原子比例:
    0.33
  • 拓扑面积:
    0
  • 氢给体数:
    0
  • 氢受体数:
    0

文献信息

  • METHODS OF MAKING CHLORINATED HYDROCARBONS
    申请人:Wilson Richard L.
    公开号:US20090216055A1
    公开(公告)日:2009-08-27
    Methods for the manufacture of 1,1,1,2,3-pentachloropropane from 1,1,1,3-tetrachloropropane and chlorine are disclosed. Improved methods are provided for the manufacture of 1,1,2,3-tetrachloropropene from 1,1,1,2,3-pentachloropropane. Methods are also disclosed for the manufacture of 1,1,2,3-tetrachloropropene from 1,1,1,3-tetrachloropropane and chlorine and for the manufacture of 1,1,2,3-tetrachloropropene from carbon tetrachloride ethylene, and chlorine.
    揭示了从1,1,1,3-四氯丙烷和氯制备1,1,1,2,3-五氯丙烷的制造方法。提供了改进的方法,用于从1,1,1,2,3-五氯丙烷制备1,1,2,3-四氯丙烯。还揭示了从1,1,1,3-四氯丙烷和氯制备1,1,2,3-四氯丙烯的制造方法,以及从四氯化碳、乙烯和氯制备1,1,2,3-四氯丙烯的制造方法。
  • Highly pure 1,1,1,2,3-pentachloropropane composition
    申请人:SPOLEK PRO CHEMICKOU A HUTNI VYROBU A.S.
    公开号:US10611707B2
    公开(公告)日:2020-04-07
    Disclosed is a process for preparing a highly pure 1,1,1,2,3-pentachloropropane product, comprising 1-a) providing a reaction mixture comprising ethylene, carbon tetrachloride and a catalyst in a principal alkylation zone to produce 1,1,1,3-tetrachloropropane in the reaction mixture, and 1-b) treating the reaction mixture obtained in step 1-a) to obtain a 1,1,1,3-tetrachloropropane feedstock; 2-a) contacting the 1,1,1,3-tetrachloropropane feedstock with a catalyst in a dehydrochlorination zone to produce a reaction mixture comprising 1,1,1,3-tetrachloropropane and 1,1,3-trichloropropene, and 2-b) treating the reaction mixture obtained in step 2-a) to obtain a 1,1,3-trichloropropene feedstock; 3-a) contacting the 1,1,3-trichloropropene feedstock with chlorine in a reaction zone to produce a reaction mixture containing 1,1,1,2,3-pentachloropropane and 1,1,3-trichloropropene, the reaction zone being different from the dehydrochlorination zone, and 3-b) treating the reaction mixture obtained in step 3-a) to obtain the highly pure 1,1,1,2,3-pentachloropropane product.
    本发明公开了一种制备高纯度 1,1,1,2,3-五氯丙烷产品的工艺,包括 1-a) 在主烷基化区提供由乙烯、四氯化碳和催化剂组成的反应混合物,在反应混合物中生成 1,1,1,3-四氯丙烷,以及 1-b) 处理步骤 1-a) 中得到的反应混合物,以获得 1,1,1,3-四氯丙烷原料; 2-a) 将 1,1,1,3- 四氯丙烷原料与脱氢氯化区中的催化剂接触,生成包含 1,1,1,3- 四氯丙烷和 1,1,3- 三氯丙烯的反应混合物,以及 2-b) 处理步骤 2-a) 中得到的反应混合物,以获得 1,1,3-三氯丙烯原料; 3-a) 在反应区将 1,1,3-三氯丙烯原料与氯接触,生成含有 1,1,1,2,3-五氯丙烷和 1,1,3-三氯丙烯的反应混合物,该反应区不同于脱氢氯化区,以及 3-b) 处理在步骤 3-a) 中获得的反应混合物,以获得高纯度的 1,1,1,2,3- 五氯丙烷产品。
  • PROCESSES FOR PRODUCING VERY HIGH PURITY 1,1,1,2,3-PENTACHLOROPROPANE
    申请人:SPOLEK PRO CHEMICKOU A HUTNI VYROBU A.S.
    公开号:US20160107956A1
    公开(公告)日:2016-04-21
    Disclosed is a process for preparing a highly pure 1,1,1,2,3-pentachloropropane product, comprising 1-a) providing a reaction mixture comprising ethylene, carbon tetrachloride and a catalyst in a principal alkylation zone to produce 1,1,1,3-tetrachloropropane in the reaction mixture, and 1-b) treating the reaction mixture obtained in step 1-a) to obtain a 1,1,1,3-tetrachloropropane feedstock; 2-a) contacting the 1,1,1,3-tetrachloropropane feedstock with a catalyst in a dehydrochlorination zone to produce a reaction mixture comprising 1,1,1,3-tetrachloropropane and 1,1,3-trichloropropene, and 2-b) treating the reaction mixture obtained in step 2-a) to obtain a 1,1,3-trichloropropene feedstock; 3-a) contacting the 1,1,3-trichloropropene feedstock with chlorine in a reaction zone to produce a reaction mixture containing 1,1,1,2,3-pentachloropropane and 1,1,3-trichloropropene, the reaction zone being different from the dehydrochlorination zone, and 3-b) treating the reaction mixture obtained in step 3-a) to obtain the highly pure 1,1,1,2,3-pentachloropropane product.
  • PROCESSES FOR PRODUCING VERY HIGH PURITY 1,1,1,2,3- PENTACHLOROPROPANE
    申请人:SPOLEK PRO CHEMICKOU A HUTNI VYROBU A.S.
    公开号:US20180118641A1
    公开(公告)日:2018-05-03
    Disclosed is a process for preparing a highly pure 1,1,1,2,3-pentachloropropane product, comprising 1-a) providing a reaction mixture comprising ethylene, carbon tetrachloride and a catalyst in a principal alkylation zone to produce 1,1,1,3-tetrachloropropane in the reaction mixture, and 1-b) treating the reaction mixture obtained in step 1-a) to obtain a 1,1,1,3-tetrachloropropane feedstock; 2-a) contacting the 1,1,1,3-tetrachloropropane feedstock with a catalyst in a dehydrochlorination zone to produce a reaction mixture comprising 1,1,1,3-tetrachloropropane and 1,1,3-trichloropropene, and 2-b) treating the reaction mixture obtained in step 2-a) to obtain a 1,1,3-trichloropropene feedstock; 3-a) contacting the 1,1,3-trichloropropene feedstock with chlorine in a reaction zone to produce a reaction mixture containing 1,1,1,2,3-pentachloropropane and 1,1,3-trichloropropene, the reaction zone being different from the dehydrochlorination zone, and 3-b) treating the reaction mixture obtained in step 3-a) to obtain the highly pure 1,1,1,2,3-pentachloropropane product.
  • PROCESS FOR THE MANUFACTURE OF 2,3,3,3-TETRAFLUOROPROPENE
    申请人:ARKEMA FRANCE
    公开号:US20190127303A1
    公开(公告)日:2019-05-02
    The present invention provides a process of manufacture of 2,3,3,3-tetrafluoropropene by fluorination of very high purity 1,1,1,2,3-pentachloropropane (HCC-240db) into product 2,3,3,3-tetrafluoropropene (HFO-1234yf), the process comprising the following steps: —step 3 of chlorination of 1,1,3-trichloropropene to produce 1,1,1,2,3-pentachloropropane, comprising: 3-a) contacting the 1,1,3-trichloropropene feedstock with chlorine in a reaction zone to produce a reaction mixture containing 1,1,1,2,3-pentachloropropane and 1,1,3-trichloropropene, the reaction zone being different from the dehydrochlorination zone, and 3-b) treating the reaction mixture obtained in step 3-a) to obtain a 1,1,1,2,3-pentachloropropane (HCC-240db) feedstock; —step 4 of producing 2,3,3,3-tetrafluoropropene (HFO-1234yf), comprising: 4-a) reacting the 1,1,1,2,3-pentachloropropane (HCC-240db) feedstock with HF in the presence or absence of catalyst to produce a reaction mixture comprising at least one compound chosen from HCI, HF, 1,1,1,2,2-pentafluoropropane (HFC-245cb), 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf) and 2,3,3,3-tetrafluoropropene (HFO-1234yf).
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