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1,4-丁二醇连续加氢反应过程的开发

STUDY ON PROCESS DEVELOPMENT OF CONTINUOUS HYDROGENATION REACTION OF 1,4-BUTANEDIOL

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【作者】 毛之侯许志美汤惠芳张濂朱海东何祖楹胡维庭莫新强施立才党铭伟

【Author】 Mao Zhihou,Xu Zhimei, Tang Huifang,Zhang Lian & Zhu Haidong (UNILAB Research Center of Chemical Reaction Engineering, East China Institute of Chemical Technology Branch) He Zuying,Hu Weiting & Mo Xingqiang (Shanghai Wu Song Chemical Works) Shi Licai & Dang Mingwei (UNILAB Research Center of Chemical Reaction Engineering,Design Department,Shanghai)

【机构】 华东化工学院联合化学反应工程研究所上海吴淞化工厂上海医药设计院上海医药设计院

【摘要】 本文以镍系催化剂催化加氢制取1,4-丁二醇为研究对象,应用工业反应过程开发方法的基本原则,进行连续加氢反应过程的开发研究,就确定优选工艺条件、加氢反应器形式的选择及反应器主要结构尺寸等进行了论述,考察了反应放大时几何尺寸的影响,并对出现的工程问题提出相应的对策。

【Abstract】 Studied on hydrogenation synthesis of 1,4-butanediol by use of Raney nickel catalyst,the continuous hydrogenating reaction process is developed based on the principle of the development method of industrial reaction. The determination of optimizing process condition ,the selection of type of the reactor, and main structure dimension of the reactor are discussed. Effect of geometric size on reactor scaleup is investigated and a method for resolving the reactor engineering problem is proposed in this paper.

【关键词】 1,4-丁二醇加氢反应开发和放大淤浆床
  • 【文献出处】 化学工程 ,Chemical Engineering(China) , 编辑部邮箱 ,1992年06期
  • 【被引频次】5
  • 【下载频次】968
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