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Continuous production of ethyl lactate by esterifying lactic acid with ethanol, comprises using a flash column and distillation column for product recovery

机译:通过用乙醇将乳酸酯化来连续生产乳酸乙酯,包括使用闪蒸塔和蒸馏塔进行产品回收

摘要

Continuous production of ethyl lactate comprises esterifying lactic acid with ethanol until the lactic acid conversion is 80% or less, distilling the reaction mixture in a flash column, recycling the bottoms stream from the flash column to the esterification reactor, and distilling the overhead stream from the flash column to produce and overhead stream of ethanol and water and a bottoms stream of ethyl lactate. Continuous production of ethyl lactate comprises esterifying lactic acid with ethanol in an initial ethanol/lactic acid molar ratio of at least 2.5 in the presence of a catalyst at 50-90 degrees C and atmospheric pressure until the lactic acid conversion is 80% or less, distilling the reaction mixture in a flash column at 80-90 degrees C and up to 65 mbar, recycling the bottoms stream from the flash column to the esterification reactor, and distilling the overhead stream from the flash column at atmospheric pressure to produce and overhead stream of ethanol and water and a bottoms stream of ethyl lactate with a water content allowing subsequent purification. An Independent claim is also included for ethyl lactate produced as above with a water content of 0.3% or less.
机译:乳酸乙酯的连续生产包括用乙醇将乳酸酯化,直到乳酸转化率为80%或更低;将反应混合物在闪蒸塔中蒸馏;将塔底物流从闪蒸塔再循环到酯化反应器;以及将塔顶物流从闪蒸塔产生乙醇和水的塔顶物流和乳酸乙酯的塔底物流。乳酸乙酯的连续生产包括在催化剂存在下,在50-90摄氏度和大气压下,以乙醇/乳酸的初始摩尔比至少为2.5与乙醇酯化乳酸,直到乳酸转化率为80%或更低,将反应混合物在80-90摄氏度,最高65 mbar的闪蒸塔中蒸馏,将塔底物流从闪蒸塔再循环到酯化反应器中,并在大气压下蒸馏来自闪蒸塔的塔顶物流以生产出塔顶物流乙醇和水,以及含水的乳酸乙酯塔底物流,可进行后续纯化。对于如上生产的水含量为0.3%或更少的乳酸乙酯也包括独立权利要求。

著录项

  • 公开/公告号FR2848209A1

    专利类型

  • 公开/公告日2004-06-11

    原文格式PDF

  • 申请/专利权人 ATOFINA;

    申请/专利号FR20020015348

  • 发明设计人 TRETJAK SERGE;BURTIN ELIE;TEISSIER REMY;

    申请日2002-12-05

  • 分类号C07C69/68;C07C67/48;

  • 国家 FR

  • 入库时间 2022-08-21 22:39:18

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