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酯化釜体压力间歇性突升的处理
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作者 马金凤 王云华 +2 位作者 周士强 管宗 贾晓新 《聚酯工业》 CAS 2017年第1期39-41,共3页
通过对酯化釜及工艺塔原理探究和对酯化EG固含量化验分析,判断出酯化压力间歇性突升的可能原因,并对现场流程进行改造。经过对工艺塔盘的冲洗和工艺塔回流水的自控,有效解决酯化压力间歇性突升的问题。
关键词 PET 酯化压力 处理
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Simulation of Continuous Esterification Process of Polyester Polyols 被引量:2
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作者 陈礼科 奚桢浩 +2 位作者 秦榛 赵玲 袁渭康 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2013年第3期246-252,共7页
Based on the kinetic and thermodynamic equations, a comprehensive mathematical model for the con- tinuous esterification process of polyester polyols was developed, which was carried out in an innovational bub- bling ... Based on the kinetic and thermodynamic equations, a comprehensive mathematical model for the con- tinuous esterification process of polyester polyols was developed, which was carried out in an innovational bub- bling reactive distillation tower (BRDT) at atmospheric pressure. In this new type of reactor, direct esterification between ethylene glycol and adipic acid was accomplished efficiently and rapidly. A bench BRDT with the height of 2 m was applied for the esteriflcation process of l^oly (ethylene adlpate) (P'EA). In the continuous operation, Hn- ear oligomers were discharged from the bottom of the column, while water passed a few column trays and a pack- ing section as a condensation byproduct. The influence of major operating conditions on reactor performance was also simulated. Simulation results were in good agreement with experimental data, providing a strategy for devel- oping and optimizing this process. 展开更多
关键词 poly (ethylene adipate) ESTERIFICATION continuous operation mathematical model reactive distillation
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