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acetic acid-(2-chloro-3-hydroxy-propyl ester) | 859053-78-4

中文名称
——
中文别名
——
英文名称
acetic acid-(2-chloro-3-hydroxy-propyl ester)
英文别名
Essigsaeure-(2-chlor-3-hydroxy-propylester);(2-Chloro-3-hydroxypropyl) acetate
acetic acid-(2-chloro-3-hydroxy-propyl ester)化学式
CAS
859053-78-4
化学式
C5H9ClO3
mdl
——
分子量
152.578
InChiKey
PXTGSZCVWLPUAR-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):
    0.1
  • 重原子数:
    9
  • 可旋转键数:
    4
  • 环数:
    0.0
  • sp3杂化的碳原子比例:
    0.8
  • 拓扑面积:
    46.5
  • 氢给体数:
    1
  • 氢受体数:
    3

反应信息

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文献信息

  • Wegscheider; Zmerzlikar, Monatshefte fur Chemie, 1913, vol. 34, p. 1066
    作者:Wegscheider、Zmerzlikar
    DOI:——
    日期:——
  • Bigot, Annales de Chimie (Cachan, France), 1891, vol. <6> 22, p. 482
    作者:Bigot
    DOI:——
    日期:——
  • Batch, semi-continuous or continuous hydrochlorination of glycerin with reduced volatile chlorinated hydrocarbon by-products and chloracetone levels
    申请人:Kruper J. William
    公开号:US20080015369A1
    公开(公告)日:2008-01-17
    The present invention relates to a process for converting a multihydroxylated-aliphatic hydrocarbon or ester thereof to a chlorohydrin, by contacting the multihydroxylated-aliphatic hydrocarbon or ester thereof starting material with a source of hydrogen chloride at superatmospheric, atmospheric and subatmospheric pressure conditions for a sufficient time and at a sufficient temperature, preferably wherein such contracting step is carried out without substantial removal of water, to produce the desired chlorohydrin product; wherein the desired product or products can be made in high yield without substantial formation of undesired overchlorinated byproducts; said process carried out without a step undertaken to specifically remove volatile chlorinated hydrocarbon by-products or chloroacetone, wherein the combined concentration of volatile chlorinated hydrocarbon by-products and chloroacetone is less than 2000 ppm throughout any stage of the said process.
  • Method for Making Chlorohydrin in Liquid Phase in the Presence of Heavy Compounds
    申请人:Gilbeau Patrick
    公开号:US20080194884A1
    公开(公告)日:2008-08-14
    Process for preparing a chlorohydrin, wherein a polyhydroxylated aliphatic hydrocarbon, an ester of a polyhydroxylated aliphatic hydrocarbon or a mixture thereof is subjected to reaction with a chlorinating agent in the presence of a liquid phase comprising heavy compounds other than the polyhydroxylated aliphatic hydrocarbon and having a boiling temperature under a pressure of 1 bar absolute which is at least 15° C. greater than the boiling temperature of the chlorohydrin under a pressure of 1 bar absolute.
  • BATCH, SEMI-CONTINUOUS OR CONTINUOUS HYDROCHLORINATIONOF GLYCERIN WITH REDUCED VOLATILE CHLORINATED HYDROCARBON BY-PRODUCTS AND CHLOROACETONE LEVELS
    申请人:Kruper William J.
    公开号:US20110124890A1
    公开(公告)日:2011-05-26
    The present invention relates to a process for converting a multihydroxylated-aliphatic hydrocarbon or ester thereof to a chlorohydrin, by contacting the multihydroxylated-aliphatic hydrocarbon or ester thereof starting material with a source of hydrogen chloride at superatmospheric, atmospheric and subatmospheric pressure conditions for a sufficient time and at a sufficient temperature, preferably wherein such contracting step is carried out without substantial removal of water, to produce the desired chlorohydrin product; wherein the desired product or products can be made in high yield without substantial formation of undesired overchlorinated byproducts; said process carried out without a step undertaken to specifically remove volatile chlorinated hydrocarbon by-products or chloroacetone, wherein the combined concentration of volatile chlorinated hydrocarbon by-products and chloroacetone is less than 2000 ppm throughout any stage of the said process.
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