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Improvements in and relating to the concentration of aqueous acetic acid solutions by distillation

机译:蒸馏法中乙酸水溶液浓度的改进及其相关

摘要

PICT:0699358/III/1 Aqueous solutions of acetic acid are concentrated by distilling them in the presence of one of the following solvents: - methoxy triglycol acetate, diglycol diacetate, methoxy diglycol acetate, ethoxy triglycol acetate, dimethoxy triglycol, dimethoxy diglycol. Water is obtained as distillate leaving a mixture of solvent and concentrated acid, which is then separated by fractional distillation, preferably under reduced pressure. The molecular ratio of solvent to the water present in the solution is preferably within the range from 1:1 to 5:1. The process is particularly applicable to the concentration of aqueous solutions containing up to 15 per cent of acetic acid where the usual azeotropic distillation processes are uneconomical. A 10 per cent aqueous acetic acid solution was passed continuously through pipe 3 into distillation column 1 heated by boiler 2 and diglycol diacetate (1 part by weight per part of aqueous acid) was introduced into the upper part of the column through pipe 4. The boiler 2 was maintained at a temperature of 120 DEG C, and the top of the column at 100 DEG C. The vapours from the head of the column were p passed to condenser 6, and water containing only 0.2 per cent of acetic acid was obtained as condensate. A mixture containing 9.2 per cent acetic acid, 89.4 per cent diglycol diacetate and 1.4 per cent water collected in boiler 2, and was passed through pipe 8 into column 9. The boiler 10 of column 9 was maintained at 160 DEG C, and the pressure within the column was maintained at 25 mm. Hg. by vacuum pump 14. A mixture containing 87 per cent of acetic acid and 13 per cent water was condensed in condenser 12, and collected in receiver 15. A mixture of 99.5 per cent of diglycol acetate and 0.5 per cent of acetic acid collected in boiler 10, and was returned to column 1 via pipe 4. The second Provisional Specification also refers to the use of diethoxy triglycol as solvent. Specifications 652,844, [Group IV(a)], and 670,751 are referred to.
机译:通过在以下溶剂之一的存在下进行蒸馏来浓缩乙酸的水溶液:-甲氧基乙酸三乙二醇酯,二乙酸二乙二醇酯,乙酸甲氧基甘油二酯,乙氧基乙酸三乙二醇酯,二甲氧基三乙二醇,二甲氧基二乙二醇。获得水作为馏出物,留下溶剂和浓酸的混合物,然后优选通过在减压下通过分馏进行分离。溶液中存在的溶剂与水的分子比优选在1∶1至5∶1的范围内。该方法特别适用于浓缩至多含15%乙酸的水溶液,而通常的共沸蒸馏方法不经济。使10%的乙酸水溶液连续通过管道3进入由锅炉2加热的蒸馏塔1中,并将二乙酸二甘醇酯(每份酸水溶液1重量份)通过管道4引入到塔的上部。锅炉2的温度保持在120℃,塔顶保持在100℃。将来自塔顶的蒸气p通入冷凝器6,得到的水仅含0.2%的乙酸。作为冷凝物。在锅炉2中收集到的混合物中含有9.2%的乙酸,89.4%的二乙酸二乙二醇酯和1.4%的水,并通过管道8进入塔9。将塔9的锅炉10保持在160℃,压力柱内的压力保持在25mm。汞通过真空泵14。将含有87%的乙酸和13%的水的混合物在冷凝器12中冷凝,并收集到接收器15中。在锅炉中收集到99.5%的乙酸二甘醇和0.5%的乙酸的混合物10,并通过管道4返回到第1列。第二临时规范还涉及使用二乙氧基三甘醇作为溶剂。参考规格652,844,[IV(a)组]和670,751。

著录项

  • 公开/公告号ES201799A1

    专利类型

  • 公开/公告日1954-02-01

    原文格式PDF

  • 申请/专利权人 COURTAULDS LIMITED;

    申请/专利号ES19520201799

  • 发明设计人

    申请日1952-02-08

  • 分类号1B01A;

  • 国家 ES

  • 入库时间 2022-08-24 00:12:29

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