cyclohex-1-ene-1,2,4,5-tetracarboxylic acid

• 分子结构分类: 有机化合物 - 有机酸及其衍生物 - 羧酸及其衍生物
• 英文名称: cyclohex-1-ene-1,2,4,5-tetracarboxylic acid
• 英文别名: Cyclohex-1-en-1,2,4,5-tetracarbonsaeure；1,2,4,5-cyclohexene tetracarboxylic acid；Cyclohexene-1,2,4,5-tetracarboxylic acid
• 化学式: C₁₀H₁₀O₈
• 分子量: 258.185
• InChiKey: LSTXEOMYRWXAOY-UHFFFAOYSA-N

计算性质

• 辛醇/水分配系数(LogP)：
  -1.1
• 重原子数：
  18
• 可旋转键数：
  4
• 环数：
  1.0
• sp3杂化的碳原子比例：
  0.4
• 拓扑面积：
  149
• 氢给体数：
  4
• 氢受体数：
  8

反应信息

• 作为反应物：
  描述：

  cyclohex-1-ene-1,2,4,5-tetracarboxylic acid 生成 alkaline earth salt of/the/ methylsulfuric acid
  参考文献：
  名称：

  Baeyer, Justus Liebigs Annalen der Chemie, 1873, vol. 166, p. 338,346

  摘要：

  DOI：
• 作为产物：
  描述：

  均苯四甲酸 在 sodium amalgam 作用下， 生成 cyclohex-1-ene-1,2,4,5-tetracarboxylic acid 、 alkaline earth salt of/the/ methylsulfuric acid
  参考文献：
  名称：

  Baeyer, Justus Liebigs Annalen der Chemie, 1873, vol. 166, p. 338,346

  摘要：

  DOI：

文献信息

• COLORED POLYMER THIN FILM, COLOR FILTER, AND LIQUID CRYSTAL DISPLAY
  申请人：TORAY INDUSTRIES, INC.

  公开号：EP1026193A1

  公开（公告）日：2000-08-09

  An object of the present invention is to provide a liquid crystal display exhibiting excellent display performance. The object of the present invention is achieved by a colored polymer thin film having an average refractive index of 1.60 to 1.90, and an absolute value of birefringence of 0.01 or less, and a color filter and a liquid crystal display using the colored polymer thin film. The color filter using the colored polymer thin film of the present invention exhibits reduced retardation, and can thus provide a liquid crystal display exhibiting excellent display performance.

  本发明的目的是提供一种显示性能优异的液晶显示器。 本发明的目的是通过一种平均折射率为 1.60 至 1.90、双折射绝对值为 0.01 或以下的彩色聚合物薄膜，以及使用该彩色聚合物薄膜的彩色滤光片和液晶显示器来实现的。 使用本发明彩色聚合物薄膜的彩色滤光片具有较低的延迟，因此可以提供显示性能优异的液晶显示器。
• STABLE DISPERSANT AND APPLICATION THEREOF IN PREPARING COPOLYMER POLYOLS
  申请人：Wanhua Chemical Group Co., Ltd.

  公开号：EP3901189A1

  公开（公告）日：2021-10-27

  Provided by the present invention are a stable dispersant and an application thereof in preparing copolymer polyols, the preparation method for the stable dispersant comprising: 1) contacting a polyol with a dianhydride compound for reaction so as to prepare an adduct; 2) performing a ring-opening addition reaction on the adduct obtained in step 1) and an epoxy compound to prepare a stable dispersant; the dianhydride compound does not contain a double bond that may copolymerize with an olefinically unsaturated monomer, while the epoxy compound contains a double bond that may copolymerize with an olefinically unsaturated monomer, the polyol is a polyester polyol and/or a polyether polyol, preferably being a polyether polyol. The stable dispersant obtained by means of the described preparation method has a multi-active site anchoring function, and is applied to the synthesis of copolymer polyols to obtain copolymer polyols having relatively uniform particle size.

  本发明提供了一种稳定分散剂及其在制备共聚多元醇中的应用，该稳定分散剂的制备方法包括：1）将多元醇与二酐化合物接触反应，以制备加合物；2）对步骤 1）中获得的加合物和环氧化合物进行开环加成反应，以制备稳定的分散剂；二酐化合物不含有可与烯烃不饱和单体共聚的双键，而环氧化合物含有可与烯烃不饱和单体共聚的双键，多元醇是聚酯多元醇和/或聚醚多元醇，最好是聚醚多元醇。通过所述制备方法获得的稳定分散剂具有多活性位点锚定功能，应用于共聚多元醇的合成，可获得粒径相对均匀的共聚多元醇。
• METHOD FOR THE PRODUCTION OF TETRAHYDROFURAN
  申请人：——

  公开号：US20040039214A1

  公开（公告）日：2004-02-26

  Unsubstituted or alkyl-substituted THF is obtained by catalytic hydrogenation in the gas phase of C 4 -dicarboxylic acids and/or their derivatives using a catalyst comprising <80% by weight, preferably <70% by weight, in particular from 10 to 65% by weight, of CuO and >20% by weight, preferably >30% by weight, in particular from 35 to 90% by weight, of an oxidic support having acid centers, at a hot spot temperature of from 240 to 310° C., preferably from 240 to 280° C., and a WHSV over the catalyst of from 0.01 to 1.0, preferably from 0.02 to 1, in particular from 0.05 to 0.5, kg of starting material/l of catalyst×hour.

  未取代或烷基取代的四氢呋喃是在气相中通过催化氢化 C 4 -二羧酸和/或其衍生物，催化剂的重量百分比为 20%，优选大于 30%，特别是 35% 至 90%，具有酸中心的氧化性载体，热点温度为 240 至 310°C，优选 240 至 280°C，催化剂上的 WHSV 为 0.01 至 1.0，优选 0.02 至 1，特别是 0.05 至 0.5（公斤起始原料/升催化剂×小时）。
• US6231782B1
  申请人：——

  公开号：US6231782B1

  公开（公告）日：2001-05-15
• US6455208B1
  申请人：——

  公开号：US6455208B1

  公开（公告）日：2002-09-24