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3-hydroxy-2,2,4-trimethylpentyl butyrate

中文名称
——
中文别名
——
英文名称
3-hydroxy-2,2,4-trimethylpentyl butyrate
英文别名
(3-Hydroxy-2,2,4-trimethylpentyl) butanoate
3-hydroxy-2,2,4-trimethylpentyl butyrate化学式
CAS
——
化学式
C12H24O3
mdl
——
分子量
216.321
InChiKey
QRDOXFIFMGYVHO-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):
    2.8
  • 重原子数:
    15
  • 可旋转键数:
    7
  • 环数:
    0.0
  • sp3杂化的碳原子比例:
    0.92
  • 拓扑面积:
    46.5
  • 氢给体数:
    1
  • 氢受体数:
    3

反应信息

  • 作为产物:
    参考文献:
    名称:
    ジオールモノエステル化合物、造膜助剤、および塗料用組成物
    摘要:
    提供具有高造膜效果和高沸点的化合物、造膜助剂,以及含有该造膜助剂的涂料用组合物。通过将由具有1至6个碳原子的烷基的羧酸酯化的式1表示的二醇化合物,总碳原子数为10至24的二醇单酯。此外,使用这些化合物,将其作为在大气压下沸点超过260°C的造膜助剂。(在式1中,R1代表氢,具有1至10个碳原子的直链烷基,或具有4至10个碳原子的支链烷基,R2和R3独立地代表氢,具有1至3个碳原子的直链烷基,或具有3个碳原子的支链烷基。)【选择图】无
    公开号:
    JP2019077650A
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文献信息

  • Synthetic method of glycol diesters from reaction of glycol monoesters and linear aliphatic carboxylic acids
    申请人:Ko Donghyun
    公开号:US20070049764A1
    公开(公告)日:2007-03-01
    A method of synthesizing glycol diester by reacting a linear aliphatic carboxylic acid and a glycol monoester in the presence of a Lewis acid type catalyst is provided. In the method, after introducing the glycol monoester, the linear aliphatic carboxylic acid and the Lewis acid type catalyst into a reactor, the reaction occurs to produce reaction products and water in the reactor; an excess of the linear aliphatic carboxylic acid forms an azeotrope with water during the reaction to be sent to a condenser through a distillation column; the linear aliphatic carboxylic acid and water passed through the condenser are divided into an organic layer and an aqueous layer in an oil water separator; and the organic layer is returned to the distillation column through a material cycling line and water in the aqueous layer is removed through a water removal line. By utilizing reactive distillation technique, water produced during the reaction is rapidly removed, and thus the reaction time can be significantly reduced and the yield of the glycol diester can be maximized.
    提供一种通过在Lewis酸型催化剂存在下,通过将线性脂肪族羧酸和甘醇单酯反应合成乙二醇二酯的方法。在该方法中,将甘醇单酯、线性脂肪族羧酸和Lewis酸型催化剂引入反应器后,在反应器中发生反应产生反应产物和水;在反应过程中,过量的线性脂肪族羧酸与水形成共沸物,通过蒸馏塔被送入冷凝器;通过冷凝器传递的线性脂肪族羧酸和水在油水分离器中分为有机层和水层;有机层通过物料循环管返回至蒸馏塔,水层中的水则通过水去除管道去除。通过利用反应蒸馏技术,可以快速去除反应过程中产生的水,从而显著减少反应时间,最大限度地提高乙二醇二酯的产量。
  • METHOD FOR FRACTIONATING STEREOISOMERIC COMPOUNDS
    申请人:Jakel Christoph
    公开号:US20090030235A1
    公开(公告)日:2009-01-29
    The present invention relates to a method for fractionating stereoisomeric compounds which have at least one alcohol and/or amino group.
    本发明涉及一种用于分离具有至少一种醇和/或氨基团的立体异构化合物的方法。
  • Levulinic acid ester derivatives as reactive plasticizers and coalescent solvents
    申请人:Bloom Paul D.
    公开号:US20100216915A1
    公开(公告)日:2010-08-26
    The present invention is directed to ester derivatives of levulinic acid that are useful as plasticizers and/or coalescent solvents in polymer compositions, compositions comprising the ester derivatives, methods of making the derivatives and the compositions, and the use of the derivatives as additives in polymer compositions.
    本发明涉及丙酮酸酯衍生物,其可用作聚合物组合物中的增塑剂和/或凝聚溶剂,包含该酯衍生物的组合物,制备该衍生物和组合物的方法以及将该衍生物用作聚合物组合物中的添加剂。
  • Thermoplastic elastomer composition
    申请人:Riken Technos Corporation
    公开号:EP1566405A1
    公开(公告)日:2005-08-24
    The invention provides a thermoplastic elastomer composition comprising: (a) 100 parts by weight of a hydrogenated block copolymer; (b) 0.01 to 3 parts by weight of an organic peroxide; and (c) 1 to 80 parts by weight of a carboxylated liquid polybutadiene. Also disclosed is a thermoplastic resin composition comprising the thermoplastic elastomer composition.
    本发明提供了一种热塑性弹性体组合物,其成分包括:(a) 100 份(重量)氢化嵌段共聚物;(b) 0.01 至 3 份(重量)有机过氧化物;(c) 1 至 80 份(重量)羧化液态聚丁二烯。还公开了一种热塑性树脂组合物,其中包含热塑性弹性体组合物。
  • Hydroformylation method for the large-scale production of aldehydes and/or alcohols
    申请人:BASF SE
    公开号:US11014863B2
    公开(公告)日:2021-05-25
    A process for preparing C4 to C13 monohydroxy compounds from a bottom fraction arising in the distillation of a crude mixture of C4 to C13 oxo-process aldehydes from cobalt-catalyzed or rhodium-catalyzed hydroformylation, or in the distillation of a crude mixture of C4 to C13 oxo-process alcohols, which comprises contacting the bottom fraction in the presence of hydrogen with a catalyst comprising copper oxide and aluminum oxide, at a temperature of 150° C. to 300° C. and a pressure of 20 bar to 300 bar and subjecting the resulting crude hydrogenation product to distillation, and the amount of C4 to C13 monohydroxy compounds present in the crude hydrogenation product after the hydrogenation being greater than the amount of C4 to C13 monohydroxy compounds given stoichiometrically from the hydrogenation of the ester and aldehyde compounds present in the bottom fraction, including the C4 to C13 monohydroxy compounds still present in the bottom fraction before the hydrogenation.
    一种从钴催化或铑催化加氢甲酰化产生的 C4 至 C13 氧化过程醛粗混合物的蒸馏过程中或 C4 至 C13 氧化过程醇粗混合物的蒸馏过程中产生的底馏物中制备 C4 至 C13 单羟基化合物的工艺,该工艺包括在氢气存在下,在 150 摄氏度至 300 摄氏度的温度和 20 巴至 300 巴的压力下,使底馏物与由氧化铜和氧化铝组成的催化剂接触,并将得到的粗加氢产物进行蒸馏,加氢后粗加氢产物中的 C4 至 C13 单羟基化合物的含量为 0.1%至 0.2%。和 20 巴至 300 巴的压力下接触,并将得到的粗加氢产物进行蒸馏,加氢后粗加氢产物中存在的 C4 至 C13 单羟基化合物的量大于底馏分中存在的酯和醛化合物加氢后按化学计量得到的 C4 至 C13 单羟基化合物的量,包括加氢前底馏分中仍存在的 C4 至 C13 单羟基化合物。
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