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2,2,4,4-tetrafluoro-3-methylpentane | 86154-58-7

中文名称
——
中文别名
——
英文名称
2,2,4,4-tetrafluoro-3-methylpentane
英文别名
——
2,2,4,4-tetrafluoro-3-methylpentane化学式
CAS
86154-58-7
化学式
C6H10F4
mdl
——
分子量
158.139
InChiKey
LYKAXDYIHLTYDX-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):
    2.93
  • 重原子数:
    10.0
  • 可旋转键数:
    2.0
  • 环数:
    0.0
  • sp3杂化的碳原子比例:
    1.0
  • 拓扑面积:
    0.0
  • 氢给体数:
    0.0
  • 氢受体数:
    0.0

反应信息

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文献信息

  • STEPANOV, I. V.;BURMAKOV, A. I.;KUNSHENKO, B. V.;ALEKSEEVA, L. A.;YAGUPOL+, ZH. ORGAN. XIMII, 1983, 19, N 2, 273-279
    作者:STEPANOV, I. V.、BURMAKOV, A. I.、KUNSHENKO, B. V.、ALEKSEEVA, L. A.、YAGUPOL+
    DOI:——
    日期:——
  • [EN] NEW INDUSTRIAL PROCESS FOR MANUFACTURING OF PERFLUOROPENTANE (PFP)<br/>[FR] NOUVEAU PROCÉDÉ INDUSTRIEL DE FABRICATION DE PERFLUOROPENTANE (PFP)
    申请人:[en]FUJIAN YONGJING TECHNOLOGY CO., LTD
    公开号:WO2022160762A1
    公开(公告)日:2022-08-04
    Provided are a new industrial process for manufacturing of perfluoropentane (PFP) and the manufacture of a novel intermediate compound thereof, as well as a novel intermediate compound itself and the use thereof in the process for manufacturing of perfluoropentane (PFP). Accordingly, provided are a process for the manufacture of the compound PFP (perfluoropentane), and/or of the compound perfluorinated 4-methylbutyrolactone, i.e., the precursor or intermediate compound of PFP (perfluoropentane), characterized in that the process comprises direct fluorination reaction with F2gas as the fluorination agent, and/or from the fluorination reaction with SF4as the fluorination agent. Herein provides an efficient and simplified new industrial process for manufacturing of perfluoropentane (PFP) and/or of the compound perfluorinated 4-methylbutyrolactone, and preferably enabling large-scale and/or industrial production of perfluoropentane (PFP) and/or of the compound perfluorinated 4-methylbutyrolactone by means of special equipment and special reactor design. The process, for example, is carried out in an autoclave, in a (closed) column reactor, a counter-current reactor system, in particular in a loop reactor system, or in a counter-current (loop) system ("inverse gas scrubber system"), in a tube reactor system, a continuous flow reactor system, in a coil reactor system or in a microreactor system, preferably in a counter-current reactor system or in a microreactor.
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