首页> 外国专利> RECOVERY OF TRIMELLITIC ACID FROM PSEUDOCUMENE LIQUID PHASE OXIDATION EFFLUENT

RECOVERY OF TRIMELLITIC ACID FROM PSEUDOCUMENE LIQUID PHASE OXIDATION EFFLUENT

机译:伪十二碳烯液相液相氧化废水中三聚乙酸的回收

摘要

Enhanced recovery of trimellitic acid from liquid phase oxidation effluent that contains a substantial portion of the acid product as solute in acetic acid solvent by concentrating the effluent by use of heat values in the effluent to precipitate a first crop of acid product, displacing and replacing mother liquor with fresh acetic acid of low water content to a first slurry of 60 to 70 percent solids and 40 to 30 percent liquid, further concentrating displaced effluent mother liquor by removal of 80 to 90 percent of its solvent content, displacing and replacing the remaining 20 to 10 percent of solvent with fresh acetic acid of low water content to a second slurry of 60 to 70 percent solids and 40 to 30 percent liquid, combining and removing solvent from the first and second slurries. Advantageously by the use of those steps heat is not wasted, conventional crystallization is avoided and apparatus is minimized by the practice of that combination of procedural steps. The recovered trimellitic acid product can be converted to its intramolecular anhydride or inter- and intra-bis-anhydride.
机译:通过利用废水中的热值对废水进行浓缩以沉淀出第一批酸产品,从而置换并替换母体,从而提高了从液相氧化废水中回收偏苯三酸的能力,该液相氧化废水中的大部分酸产物为溶质,在乙酸溶剂中含低水含量新鲜乙酸的纯白液体,形成固体含量为60%至70%,液体含量为40%至30%的第一浆液,通过去除80%至90%的溶剂含量进一步浓缩置换后的废水母液,置换并替换剩余的20种含10%的溶剂和低水含量的新鲜乙酸,制成固体含量为60%至70%,液体含量为40%至30%的第二种浆料,合并并从第一种和第二种浆料中除去溶剂。有利的是,通过使用这些步骤,不浪费热量,避免了常规的结晶,并且通过该过程步骤的组合的实践使设备最小化。回收的偏苯三酸产物可转化为其分子内酸酐或间和间双酸酐。

著录项

  • 公开/公告号US3853924A

    专利类型

  • 公开/公告日1974-12-10

    原文格式PDF

  • 申请/专利权人 STANDARD OIL COUS;

    申请/专利号US19700100817

  • 发明设计人 MEYER DUS;JOHNSTON GUS;

    申请日1970-12-22

  • 分类号C07C63/32;

  • 国家 US

  • 入库时间 2022-08-23 03:35:21

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