biphenyl-2,4′,5-tricarboxylic acid | 34196-40-2

• 分子结构分类: 有机化合物 - 苯类化合物 - 苯和取代衍生物
• 英文名称: biphenyl-2,4′,5-tricarboxylic acid
• 英文别名: 2-(4-Carboxyphenyl)terephthalic acid
• CAS: 34196-40-2
• 化学式: C₁₅H₁₀O₆
• 分子量: 286.241
• InChiKey: KNSIQMPBRNAYMV-UHFFFAOYSA-N

物化性质

• 沸点：
  559.0±50.0 °C(Predicted)
• 密度：
  1.488±0.06 g/cm3(Predicted)

计算性质

• 辛醇/水分配系数(LogP)：
  2.1
• 重原子数：
  21
• 可旋转键数：
  4
• 环数：
  2.0
• sp3杂化的碳原子比例：
  0.0
• 拓扑面积：
  112
• 氢给体数：
  3
• 氢受体数：
  6

反应信息

• 作为反应物：
  描述：

  biphenyl-2,4′,5-tricarboxylic acid 在 硫酸 作用下， 以95%的产率得到fluorenone-2,6-dicarboxylic acid
  参考文献：
  名称：

  A Practical Synthesis of 2,6-Dicarboxyfluorenone

  摘要：

  在此，我们报告了一种新的高效方法，用于大规模合成2,6-二甲基荧光酮5，产率达95%。该方法使用0.01摩尔%的双（三苯基膦）钯(II)氯化物[(PPh3)2 PdCl2]作为催化剂，反应以2,5-二甲基溴苯与4-溴甲苯反应生成2,4,5-三甲基联苯3，随后进行氧化和环化。

  DOI：

  10.1039/a805065a
• 作为产物：
  描述：

  1,4-二甲基-2-(4-甲基苯基)苯 在 potassium dichromate 作用下， 反应 48.0h， 以80%的产率得到biphenyl-2,4′,5-tricarboxylic acid
  参考文献：
  名称：

  A Practical Synthesis of 2,6-Dicarboxyfluorenone

  摘要：

  在此，我们报告了一种新的高效方法，用于大规模合成2,6-二甲基荧光酮5，产率达95%。该方法使用0.01摩尔%的双（三苯基膦）钯(II)氯化物[(PPh3)2 PdCl2]作为催化剂，反应以2,5-二甲基溴苯与4-溴甲苯反应生成2,4,5-三甲基联苯3，随后进行氧化和环化。

  DOI：

  10.1039/a805065a

文献信息

• Synthesis, structures, luminescent and magnetic properties of four coordination polymers based on biphenyl-2,4′,5-tricarboxylic acid and different N -donor ligands
  作者：Xuzhao Liao、Wujuan Sun、Dandan Zhai、Xiaoling Wang、Jiemin Dong、Xuwu Yang

  DOI：10.1016/j.inoche.2016.05.010

  日期：2016.8

  Abstract Four new coordination polymers [Zn(HL)(bibp)]n (1: H3L = biphenyl-2,4′,5-tricarboxylic acid, bibp = 4,4′-bis(imidazolyl)biphenyl), [Co(HL)(bibp)]n (2), [Co(HL)(bib)]n·4nH2O (3: bib = 1,4-bis(1-imidazoly)-benzene), [Co1.5(L)(bib)1.5(H2O)]n·3nH2O (4), have been synthesized under solvo/hydrothermal conditions, and have been fully characterized by single-crystal X-ray diffraction, powder X-ray

  摘要 四种新型配位聚合物 [Zn(HL)(bibp)]n (1: H3L = 联苯-2,4',5-三羧酸, bibp = 4,4'-双(咪唑基)联苯), [Co(HL) )(bibp)]n (2), [Co(HL)(bib)]n·4nH2O (3: bib = 1,4-bis(1-imidazoly)-benzo), [Co1.5(L)(bib )1.5(H2O)]n·3nH2O (4)，已在溶剂/水热条件下合成，并已通过单晶 X 射线衍射、粉末 X 射线衍射 (PXRD)、红外光谱、元素分析进行​​充分表征和热重分析 (TGA)。结构分析表明，1 和 2 都显示了 4 重互穿框架。复合体 3 拥有一个 2D (4,4) 网络。复合体 4 展示了一个 3D 框架，点符号为 32·4·67}232·610·72·8}。此外，还详细研究了 1 的光致发光特性和 2-4 的磁特性。
• Process and Catalyst for Oxidizing Aromatic Compounds
  申请人：Gong William H.

  公开号：US20090069594A1

  公开（公告）日：2009-03-12

  Catalytic compositions for conversion of substituted aromatic feed materials to oxidized products comprising aromatic carboxylic acid derivatives of the substituted aromatic feed materials comprise at least two metal or metalloid elements, at least one of which is palladium, platinum, vanadium or titanium, and at least one of which is a Group 5, 6, 14 or 15 metal or metalloid. A process for oxidizing substituted aromatic feed materials comprises contacting the feed material with oxygen in the presence of such a catalytic composition in a liquid reaction mixture.

  用于将取代芳香族原料转化为含取代芳香族羧酸衍生物的氧化产物的催化组合物至少包含两种金属或金属元素，其中至少一种是钯、铂、钒或钛，而至少一种是第5、6、14或15组金属或金属元素。一种氧化取代芳香族原料的方法包括在液体反应混合物中，在存在这样的催化组合物的情况下，将原料与氧接触。
• Optimized liquid-phase oxidation
  申请人：Wonders George Alan

  公开号：US20060047145A1

  公开（公告）日：2006-03-02

  Disclosed is an optimized process and apparatus for more efficiently and economically carrying out the liquid-phase oxidation of an oxidizable compound. Such liquid-phase oxidation is carried out in a bubble column reactor that provides for a highly efficient reaction at relatively low temperatures. When the oxidized compound is para-xylene and the product from the oxidation reaction is crude terephthalic acid (CTA), such CTA product can be purified and separated by more economical techniques than could be employed if the CTA were formed by a conventional high-temperature oxidation process.

  公开了一种优化的工艺和装置，用于更有效和经济地进行可氧化化合物的液相氧化。这种液相氧化是在气泡柱反应器中进行的，可以在相对较低的温度下提供高效的反应。当被氧化的化合物是对二甲苯，氧化反应的产物是粗对苯二甲酸（CTA）时，这种CTA产物可以通过比传统高温氧化工艺更经济的技术进行纯化和分离。
• Processes for producing terephthalic acid
  申请人：Sumner Edwan Charles

  公开号：US20060205977A1

  公开（公告）日：2006-09-14

  Processes for producing terephthalic acid are disclosed, the processes comprising combining in a reaction medium p-xylene, a solvent comprising water and one or more saturated organic acids having from 2-4 carbon atoms, and an oxygen-containing gas, at a temperature from about 135° C. to about 165° C., in the presence of a catalyst composition comprising cobalt atoms and manganese atoms, with bromine atoms provided as a promoter. The amount of cobalt used may be from about 1,800 ppm to about 6,000 ppm, with respect to the total weight of the liquid in the reaction medium, and the weight ratio of cobalt to manganese may be from about 40 to about 400. The processes according to the invention produce terephthalic acid as a precipitated reaction product, with typically no more than about 10 ppm 2,6-dicarboxyfluorenone produced, with respect to the weight of the terephthalic acid produced, or no more than about 20 ppm 2,6-dicarboxyfluorenone, with respect to the total weight of the reaction medium, per batch or upon one pass through a reactor. The terephthalic acid so produced may be further purified by one or more additional oxidation reactions, without the need for expensive hydrogenation purification processes.

  公开了生产对苯二甲酸的工艺，该工艺包括在反应介质中混合p-二甲苯、包含水和一个或多个具有2-4个碳原子的饱和有机酸的溶剂以及含氧气体，在存在钴原子和锰原子的催化剂组合物的情况下，以溴原子作为促进剂，在温度约为135℃至165℃之间进行。使用的钴量可以是相对于反应介质中液体的总重量约为1,800 ppm至6,000 ppm，而钴与锰的重量比可以是约40至400。本发明的工艺产生沉淀的对苯二甲酸作为反应产物，通常不会产生超过约10 ppm的2,6-二羧基芴酮，相对于所产生的对苯二甲酸的重量，或不超过约20 ppm的2,6-二羧基芴酮，相对于反应介质的总重量，每批次或通过反应器的一次通行。因此生产的对苯二甲酸可以通过一个或多个附加的氧化反应进一步纯化，而无需昂贵的氢化纯化工艺。
• [EN] PRODUCTION OF AROMATIC CARBOXYLIC ACIDS<br/>[FR] PRODUCTION D'ACIDES CARBOXYLIQUES AROMATIQUES
  申请人：DU PONT

  公开号：WO2002006201A1

  公开（公告）日：2002-01-24

  A process for the production of an aromatic carboxylic acid comprising contacting in the presence of a catalyst, within a continuous flow reactor, one or more precursors of the aromatic carboxylic acid with an oxidant, such contact being effected with said precursor(s) and the oxidant in an aqueous solvent comprising water under supercritical conditions or near supercritical conditions close to the supercritical point such that said one or more precursors, oxidant and aqueous solvent constitute a substantially single homogeneous phase in the reaction zone, wherein the contact of at least part of said precursor with said oxidant is contemporaneous with contact of said catalyst with at least part of said oxidant.

  一种生产芳香羧酸的工艺，包括在连续流反应器中，在催化剂的存在下，将一种或多种芳香羧酸前体物与氧化剂接触，所述接触是在水的超临界条件或接近超临界条件的水溶剂中进行的，使得所述一种或多种前体物、氧化剂和水溶剂在反应区域中构成一个基本单一的均相相位，其中至少部分前体物与氧化剂的接触与至少部分催化剂与氧化剂的接触同时发生。