首页> 外国专利> Hydrogenation of fatty acid methyl ester in fatty alcohols using fixed bed reactor, comprises producing fatty acid methyl ester using auxiliary reactors, and regenerating a catalyst charge of auxiliary reactor

Hydrogenation of fatty acid methyl ester in fatty alcohols using fixed bed reactor, comprises producing fatty acid methyl ester using auxiliary reactors, and regenerating a catalyst charge of auxiliary reactor

机译:使用固定床反应器将脂肪醇中的脂肪酸甲酯氢化,包括使用辅助反应器生产脂肪酸甲酯,并再生辅助反应器的催化剂装料

摘要

The hydrogenation of fatty acid methyl ester in fatty alcohols using fixed bed reactor, comprises producing fatty acid methyl ester using auxiliary reactors, regenerating a catalyst charge of auxiliary reactor arranged in pre- and post- reactors, repeating the fatty acid methyl ester production, treating a pure and less pure of fatty acid methyl ester product at the same time, and introducing a pure and a less pure fatty acid methyl ester product in principal reactors with/without the pre-reactor. The principal reactor contains large and small quantity of catalyst. The hydrogenation of fatty acid methyl ester in fatty alcohols using fixed bed reactor, comprises producing fatty acid methyl ester using auxiliary reactors, regenerating a catalyst charge of auxiliary reactor arranged in pre- and post- reactors, repeating the fatty acid methyl ester production, treating a pure and less pure of fatty acid methyl ester product at the same time, and introducing a pure and a less pure fatty acid methyl ester product in principal reactors with/without the pre-reactor. The principal reactor contains large and small quantity of catalyst. The auxiliary reactor is arranged in an upstream and downstream of the principle reactor. A maximum liquid flow is used in the fatty acid methyl ester production and in the auxiliary reactor with the catalyst charge in post reactor. A minimum liquid flow is used in the catalyst charge regeneration in pre- and post- reactors. Long chain of 12-14C fatty acid methyl ester is used as the pure product, and long chain of 12-22C, 12-18C, 16-22C or 16-18C fatty acid methyl ester is used as the less pure product. The less pure product is treated in the pre-reactor and pure product is treated in the post-reactor. The auxiliary reactors are designed in a form of tank and principal reactors are designed as a tubular beam in the form of tank.
机译:使用固定床反应器氢化脂肪醇中的脂肪酸甲酯,包括使用辅助反应器生产脂肪酸甲酯,再生布置在前反应器和后反应器中的辅助反应器的催化剂装料,重复脂肪酸甲酯的生产,处理同时获得纯和不太纯的脂肪酸甲酯产品,并在有/没有预反应器的主要反应器中引入纯和不太纯的脂肪酸甲酯产品。主反应器包含大量和少量的催化剂。使用固定床反应器氢化脂肪醇中的脂肪酸甲酯,包括使用辅助反应器生产脂肪酸甲酯,再生布置在前反应器和后反应器中的辅助反应器的催化剂装料,重复脂肪酸甲酯的生产,处理同时获得纯和不太纯的脂肪酸甲酯产品,并在有/没有预反应器的主要反应器中引入纯和不太纯的脂肪酸甲酯产品。主反应器包含大量和少量的催化剂。辅助反应器布置在主反应器的上游和下游。在脂肪酸甲酯生产中和在辅助反应器中使用最大液体流量,而在后反应器中加入催化剂。在前反应器和后反应器中的催化剂装料再生中使用最小的液体流量。纯产物使用12-14C脂肪酸甲酯的长链,纯净度较低的产物使用12-22C,12-18C,16-22C或16-18C脂肪酸甲酯的长链。纯度较低的产物在前反应器中处理,而纯度较高的产物在后反应器中处理。辅助反应器设计为储罐形式,主反应器设计为储罐形式的管状梁。

著录项

  • 公开/公告号DE102006004743A1

    专利类型

  • 公开/公告日2007-08-09

    原文格式PDF

  • 申请/专利权人 COGNIS IP MANAGEMENT GMBH;

    申请/专利号DE20061004743

  • 发明设计人 WUERKERT STEPHAN;GUTSCHE BERNHARD;

    申请日2006-02-02

  • 分类号C07C29/149;C07B31/00;

  • 国家 DE

  • 入库时间 2022-08-21 20:29:29

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