期刊文献+

苯乙烯本体聚合工艺模拟与分析 被引量:1

Simulation and analysis of bulk polystyrene reaction process
原文传递
导出
摘要 利用Aspen Tech Inc.的polymer plus建立了本体聚苯乙烯聚合反应过程模型,利用其灵敏度分析方法对影响产品产量和分子量的引发剂浓度、反应温度等因素进行分析,得出了引发剂量的增加可以提高产量同时分子量下降;链转移剂量的增加使产量和分子量均下降;在首釜温度115℃和107℃出现Mn和Mw的最大值. The steady process simulation models of bulk polystyrene unit process were developed by the polymer process simulation software Polymer Plus of Aspen Tech Inc. The effect of changing of initiator, temperature, etc. on the product and Mn Mw were discussed by the sensitivity analysis. The result shows that higher concentration of initiator leads to higher production rate but the lower Mn and the higher flow rate of chain agent cause the lower product ion rate and Mn, Mn Mw reach the maximum at 115 ℃ and 107 ℃ of first reactor.
出处 《计算机与应用化学》 CAS CSCD 北大核心 2007年第6期789-793,共5页 Computers and Applied Chemistry
关键词 POLYMER PLUS 苯乙烯 聚合 流程模拟 polymer plus, styrene, polymerization, flow simulation
  • 相关文献

参考文献6

  • 1Aspen Tech Co. Polymer Plus Reference. Massachusetts, 2003.
  • 2Beijing Yanshan Chemical Corp. No.1 Chemical Factory. Process and Technical Specifications for A 50000 tons per year Polystyrene Unit. Beijing: 2003.
  • 3Louie BM, et al. J Appl Polym Sci, 1985, 30: 3985.
  • 4Chemical week. 1998, (17): 34.
  • 5Pan Zuren. Polymer Chemistry. Beijing: Chemical Industry Press, 1997.
  • 6Shi Zijin. Polymerization Reaction Engineering Basis. Hangzhou: Zhejiang University Press, 1991 : 186-190.

同被引文献4

引证文献1

二级引证文献2

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部