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Terephthalic acid, pentyl undecyl ester

中文名称
——
中文别名
——
英文名称
Terephthalic acid, pentyl undecyl ester
英文别名
1-O-pentyl 4-O-undecyl benzene-1,4-dicarboxylate
Terephthalic acid, pentyl undecyl ester化学式
CAS
——
化学式
C24H38O4
mdl
——
分子量
390.6
InChiKey
RFNOWHWPVCGIPL-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):
    9
  • 重原子数:
    28
  • 可旋转键数:
    18
  • 环数:
    1.0
  • sp3杂化的碳原子比例:
    0.67
  • 拓扑面积:
    52.6
  • 氢给体数:
    0
  • 氢受体数:
    4

文献信息

  • INDUSTRIAL PREPARATION METHOD FOR ZIEGLER-NATTA CATALYST
    申请人:CHINA ENERGY GROUP NINGXIA COAL INDUSTRY CO., LTD.
    公开号:EP3770183A1
    公开(公告)日:2021-01-27
    The present invention relates to the technical field of catalyst preparation, and discloses a preparation method of a Ziegler-Natta catalyst. The method includes the following steps: subjecting magnesium halide, alcohol and an electron donor to a first contact reaction in the presence of an inert solvent to obtain a magnesium halide alcoholate and performing first cooling; subjecting titanium halide to second cooling; subjecting the cooled titanium halide, the cooled product containing the magnesium halide alcoholate and an electron donor to a second contact reaction; filtering the product of the second contact reaction to obtain the Ziegler-Natta catalyst; and subjecting the Ziegler-Natta catalyst and the heated titanium halide to a third contact reaction. The method has the advantages such as short cycle, high efficiency, etc., being suitable to industrial production.
    本发明涉及催化剂制备技术领域,公开了一种齐格勒-纳塔催化剂的制备方法。该方法包括以下步骤:在惰性溶剂存在下,将卤化镁、醇和电子供体进行第一次接触反应,得到卤化镁醇酸酯,并进行第一次冷却;将卤化钛进行第二次冷却;将冷却后的卤化钛、含有卤化镁醇酸酯和电子供体的冷却产物进行第二次接触反应;过滤第二次接触反应的产物,得到齐格勒-纳塔催化剂;将齐格勒-纳塔催化剂和加热后的卤化钛进行第三次接触反应。该方法具有周期短、效率高等优点,适用于工业生产。
  • Solid catalyst component for use in olefin polymerisation, catalyst, and application thereof
    申请人:BEIJING LIHE TECHNOLOGY LTD
    公开号:US11136421B2
    公开(公告)日:2021-10-05
    Provided in the present invention is a solid catalyst component for use in olefin polymerisation, comprising Mg, Ti, a halogen, and at least one electron donor, the electron donor being a 2-substituted amino-phenyl ester compound selected from general formula (I). Also disclosed in the present invention are a catalyst comprising the solid catalyst component, and an application for the catalyst in olefin polymerisation, particularly in propylene polymerization. Also provided in the present invention is a high activity catalyst, said catalyst being able to obtain polypropylene of high isotacticity and wide molecular weight distribution, and not requiring an external electron donor to obtain high isotacticity polypropylene; during polymerization, Al/Ti and Al/Si are reduced, the polymerization time is lengthened, and high activity can still be maintained, suitable for producing low-ash polymers.
    本发明提供了一种用于烯烃聚合的固体催化剂组分,包括 Mg、Ti、卤素和至少一种电子供体,电子供体为选自通式 (I) 的 2-取代氨基苯基酯化合物。本发明还公开了一种包含固体催化剂组分的催化剂,以及该催化剂在烯烃聚合,特别是丙烯聚合中的应用。本发明还提供了一种高活性催化剂,所述催化剂能够获得高同素异形度和宽分子量分布的聚丙烯,并且不需要外部电子供体即可获得高同素异形度聚丙烯;在聚合过程中,Al/Ti 和 Al/Si 降低,聚合时间延长,仍可保持高活性,适用于生产低灰分聚合物。
  • OLEFIN POLYMERIZATION CATALYST CARRIER, SOLID CATALYST COMPONENT AND USE THEREOF
    申请人:Renqiu Lihe Technology Ltd.
    公开号:US20170355792A1
    公开(公告)日:2017-12-14
    Provided is an olefin polymerization catalyst carrier with a general structure formula of Mg(OR I ) n (OR II ) 2-n , wherein: 0≦n≦2, and R I and R II can be the same or different and are each independently selected from a C 1 -C 20 hydrocarbon group. In the X-ray diffraction pattern of the catalyst carrier, there are a set of diffraction peaks in the range of a 2θ diffraction angle of 5°-15°, and the set of diffraction peaks contain 1-4 main diffraction peaks. Also disclosed is an olefin polymerization solid catalyst component which is prepared from the carrier Mg(OR I ) n (OR II ) 2-n , a titanium compound, and at least one electron donor compound. In addition, also disclosed is an olefin polymerization catalyst containing the solid catalyst component, at least one organic aluminum compound, and optionally, an external electron donor compound.
  • SOLID CATALYST COMPONENT FOR USE IN OLEFIN POLYMERISATION, CATALYST, AND APPLICATION THEREOF
    申请人:BEIJING LIHE TECHNOLOGY LTD
    公开号:US20200071430A1
    公开(公告)日:2020-03-05
    Provided in the present invention is a solid catalyst component for use in olefin polymerisation, comprising Mg, Ti, a halogen, and at least one electron donor, the electron donor being a 2-substituted amino-phenyl ester compound selected from general formula (I). Also disclosed in the present invention are a catalyst comprising the solid catalyst component, and an application for the catalyst in olefin polymerisation, particularly in propylene polymerization. Also provided in the present invention is a high activity catalyst, said catalyst being able to obtain polypropylene of high isotacticity and wide molecular weight distribution, and not requiring an external electron donor to obtain high isotacticity polypropylene; during polymerization, Al/Ti and Al/Si are reduced, the polymerization time is lengthened, and high activity can still be maintained, suitable for producing low-ash polymers.
  • INDUSTRIAL PREPARATION METHOD OF ZIEGLER-NATTA CATALYST
    申请人:China Energy Group Ningxia Coal Industry Co., Ltd.
    公开号:US20210403614A1
    公开(公告)日:2021-12-30
    The present invention relates to the technical field of catalyst preparation, and discloses a preparation method of a Ziegler-Natta catalyst. The method includes the following steps: subjecting magnesium halide, alcohol and an electron donor to a first contact reaction in the presence of an inert solvent to obtain a magnesium halide alcoholate and performing first cooling; subjecting titanium halide to second cooling; subjecting the cooled titanium halide, the cooled product containing the magnesium halide alcoholate and an electron donor to a second contact reaction; filtering the product of the second contact reaction to obtain the Ziegler-Natta catalyst; and subjecting the Ziegler-Natta catalyst and the heated titanium halide to a third contact reaction. The method has the advantages such as short cycle, high efficiency, etc., being suitable to industrial production.
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