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Pentanoic acid, 2-chlorophenyl ester

中文名称
——
中文别名
——
英文名称
Pentanoic acid, 2-chlorophenyl ester
英文别名
(2-chlorophenyl) pentanoate
Pentanoic acid, 2-chlorophenyl ester化学式
CAS
——
化学式
C11H13ClO2
mdl
——
分子量
212.67
InChiKey
NZWAAPTYGPJWPO-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):
    3.5
  • 重原子数:
    14
  • 可旋转键数:
    5
  • 环数:
    1.0
  • sp3杂化的碳原子比例:
    0.36
  • 拓扑面积:
    26.3
  • 氢给体数:
    0
  • 氢受体数:
    2

文献信息

  • Process for the preparation of copolymers of ethylene with at least one other 1-alkene
    申请人:STAMICARBON B.V.
    公开号:EP0044119A2
    公开(公告)日:1982-01-20
    Process for the preparation of copolymers consisting of 25-85% by wt. of ethylene, 15-75% by wt. of at least one other 1-alkene and optionally up to 20% by wt. of a polyunsaturated compound with application of a catalyst system containing a compound of a metal from sub-groups IV-VI of the periodic system and a compound of a metal from groups I-III of the periodic system, in which at least one hydrocarbon group is bound directly to the metal atom via a carbon atom, the polymerization being carried out in the presence of a halogen-containing compound of the general formula where A is a phenyl group which may contain one or two substituent halogen atoms or alkyl groups, or is a thienyl, furyl, pyrollyl, N-alkylpyrollyl or pyridyl group, which group is bound to the carbon atom directly or via a carbonyl group, X is a chlorine or bromine atom, Y is a chlorine, bromine or hydrogen atom or a hydrocarbon group with 1-8 carbon atoms, and Z is a nitrile group, a carboxyl group, an ester group, a hydrocarbyloxyalkylcarboxyl group, an carboxylic acid halide group, an amide group, a benzoyl group, a carboxyphenyl group or a carboxylhydrocarbylphenyl group.
    制备由 25-85%(重量百分比)乙烯、15-75%(重量百分比)至少一种其他 1-烯烃和(任选)最多 20%(重量百分比)多不饱和化合物组成的共聚物的工艺,其中催化剂体系含有周期系第Ⅳ-Ⅵ亚族金属化合物和周期系第Ⅰ-Ⅲ族金属化合物。聚合反应是在通式如下的含卤素化合物存在下进行的 其中 A 是苯基,可含有一个或两个取代卤素原子或烷基,或者是噻吩基、呋喃基、吡咯基、 N-烷基吡咯基或吡啶基,该基团直接或通过羰基与碳原子结合;X 是氯原子或溴原子;Y 是氯、Z 为腈基、羧基、酯基、烃基羧基、羧酸卤化基、酰胺基、苯甲酰基、羧基苯基或羧基氢羧基苯基。
  • PROCESS FOR PRODUCING POLYCARBONATE RESIN
    申请人:TEIJIN LIMITED
    公开号:EP0976772A1
    公开(公告)日:2000-02-02
    The purpose of this invention is to produce a stabilized terminal-blocked polycarbonate resin with a limited number of the terminal hydroxy groups having excellent thermal stability, color stability and hydrolysis resistance by an industrially advantageous method using a terminal blocking agent. In the production of a polycarbonate by the melt-polycondensation of an aromatic dihydroxy compound with an aromatic carbonic acid diester in the presence of a polycondensation catalyst, a terminal blocking agent expressed by the following formula (1) [in the formula, R1 is chlorine atom, methoxycarbonyl group or ethoxycarbonyl group; R2 is an alkyl group having a carbon number of 1 to 30, an alkoxy group having a carbon number of 1 to 30, an aryl group having a carbon number of 6 to 30 or an aryloxy group having a carbon number of 6-30] is added after the melt-polycondensation to the system in an amount of 0.3 to 4 mol-equivalent based on the hydroxy terminal group amount of the polycarbonate at 200 to 350°C under a pressure of 1,013 hPa (760 mmHg) or below for 0.1 second or longer and, thereafter, a stabilizer is added and kneaded into the system at 200 to 350°C under a pressure of 1.333 × 105 hPa (105 mmHg) or below for 0.1 second or longer.
    本发明的目的是通过一种具有工业优势的方法,使用一种末端封端剂,生产一种稳定的末端封端聚碳酸酯树脂,该树脂具有数量有限的末端羟基,具有优异的热稳定性、颜色稳定性和耐水解性。 在缩聚催化剂存在下,通过芳香族二羟基化合物与芳香族碳酸二酯的熔融缩聚反应生产聚碳酸酯时,使用下式(1)表示的末端封端剂 [式中,R1 为氯原子、甲氧基羰基或乙氧基羰基;R2 为碳原子数为 1 至 30 的烷基、碳原子数为 1 至 30 的烷氧基、碳原子数为 6 至 30 的芳基或碳原子数为 6 至 30 的芳氧基]在熔融缩聚后加入到体系中,加入量为 0.在 200 至 350°C、1,013 hPa(760 mmHg)或以下的压力下,在 0.1 秒或更长的时间内,以聚碳酸酯的羟基末端基团量为基准,添加 3 至 4 摩尔当量的稳定剂,然后在 200 至 350°C、1.333 × 105 hPa(105 mmHg)或以下的压力下,在 0.1 秒或更长的时间内,将稳定剂加入并捏合到体系中。
  • STABILIZED AROMATIC POLYCARBONATE
    申请人:TEIJIN LIMITED
    公开号:EP0985696A1
    公开(公告)日:2000-03-15
    The relative intensity of fluorescent light of a melt-polycondensed aromatic polycarbonate produced by the transesterification process (melt polymerization process) of an aromatic dihydroxy compound and a carbonic acid diester in the presence of a catalyst comprising a basic nitrogen compound and/or a basic phosphorus compound in combination with an alkali metal compound is suppressed to 4.0×10-3 or below at a wavelength of 465 nm based on a standard substance in a fluorescent light spectrum obtained by the excitation wavelength of 320 nm. An aromatic polycarbonate having good color stability, especially good stability to the deterioration of the chip color during storage of the chip in air at room temperature can be produced by the present invention..
    通过芳香族二羟基化合物和碳酸二酯在由碱性氮化合物和/或碱性磷化合物与碱金属化合物组合而成的催化剂存在下的酯化过程(熔融聚合过程)制得的熔融聚合芳香族聚碳酸酯,其荧光的相对强度在波长465 nm处被抑制到4.0×10-3或以下,该波长是基于由320 nm激发波长获得的荧光光谱中的标准物质。 通过本发明可以生产出一种具有良好颜色稳定性的芳香族聚碳酸酯,特别是在室温空气中储存芯片时对芯片颜色劣化具有良好的稳定性。
  • Process for preparing polycarbonate and apparatus for preparing polycarbonate
    申请人:General Electric Company
    公开号:US20030088051A1
    公开(公告)日:2003-05-08
    A process for preparing an end-capped polycarbonate comprises melt reacting an aromatic dihydroxy compound, a carbonic acid diester, and optionally a catalyst in a prepolymerization vessel to form a polycarbonate product; transferring the polycarbonate product from the prepolymerization vessel; mixing the polycarbonate product with an end-capping agent under hermetic seal at a pressure of at least about 760 mm Hg; and transferring the polycarbonate product and end-capping agent mixture to a postpolymerization vessel to endcap the polycarbonate product. An apparatus for preparing an end-capped polycarbonate comprises a prepolymerization vessel having and inlet and an outlet; a postpolymerization vessel having an inlet and an outlet; a mixer in fluid communication with the outlet of the prepolymerization vessel and the inlet of the postpolymerization vessel; and a charging port through which an end-capping agent is charged to the mixer, wherein the mixer is hermetically sealed at greater than or equal to 760 mm Hg.
    一种制备封端聚碳酸酯的工艺包括:在预聚合容器中熔融反应芳香族二羟基化合物、碳酸二酯和催化剂,形成聚碳酸酯产品;将聚碳酸酯产品从预聚合容器中转移出来;在至少约 760 毫米汞柱的压力下,在密封条件下将聚碳酸酯产品与封端剂混合;以及将聚碳酸酯产品和封端剂混合物转移到后聚合容器中,对聚碳酸酯产品进行封端。一种用于制备端盖聚碳酸酯的设备包括:一个具有入口和出口的预聚合容器;一个具有入口和出口的后聚合容器;一个与预聚合容器的出口和后聚合容器的入口流体相通的混合器;以及一个将端盖剂装入混合器的装料口,其中混合器在大于或等于 760 毫米汞柱的压力下密封。
  • PROCESS FOR THE PREPARATION OF LOW MOLECULAR WEIGHT COPOLYMERS OF ETHYLENE WITH AT LEAST ONE OTHER 1-ALKENE
    申请人:DSM N.V.
    公开号:EP0705284A1
    公开(公告)日:1996-04-10
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