期刊文献+

萃取精馏生产高纯度环氧丙烷的工艺研究 被引量:9

Extractive refining process for production of propylene oxide with high purification
下载PDF
导出
摘要 丙烯环氧化反应获得的粗环氧丙烷(PO)中含有乙醛、甲醇、甲酸甲酯和水等杂质,由于这些杂质与PO相对挥发度接近于1,普通精馏难以提纯PO;同时,分离过程中PO易发生水解生成1,2-丙二醇(PG),而PG又导致萃取剂萃取性能下降。据此,结合萃取精馏和液液萃取技术,同时考虑PO水解反应,开发了水洗回收PO和侧线采出共沸物脱除PG流程,在有效脱除杂质的同时,提高了PO的回收率和萃取剂的萃取效率,获得了高纯度PO产品。采用流程模拟软件Aspen Plus对上述流程进行了全流程模拟计算,借助NRTL热力学方法,分析了萃取精馏塔的溶剂比、理论塔板数、原料进料位置、溶剂进料温度等主要工艺参数对分离过程的影响。结果表明该工艺流程合理、可靠,经济性优于现有工艺,可指导工业过程设计和操作优化。 Crude propylene oxide(PO)produced from propylene epoxidation contains contaminations such as acetaldehyde,methanol,methyl formate,water and so on.It is difficult to remove them by using simple distillation because the relative volatilities of these components to PO are close to 1.Meanwhile,the PO is easy to react with water and 1,2-propanediol(PG)that will affect the extractive efficiency is then produced.Therefore,a process flowsheet combined extractive distillation and liquid-liquid extraction is proposed here to effectively remove these contaminations and improve PO product yield,in which the PO hydrolysis reaction(non-catalytic reactive distillation)and the processes of water washing for PO recover and side-drawing for the removal of PG are considered.The whole process is then simulated by using process simulation software Aspen Plus,in which the NRTL thermodynamic model is employed to character the thermodynamic properties.The effects of major design parameters of the separation process,such as the solvent ratio,the theoretical stage number of extractive distillation column,the location of feed,and the temperature of solvent,are investigated.The results show that the process is reasonable,reliable,and economical superior to existing processes,which can guide industrial process design and operation optimization.
作者 胡松 李进龙 李木金 杨卫胜 HU Song;LI Jinlong;LI Mujin;YANG Weisheng(State Key Laboratory of Green Chemical Engineering and Industrial Catalysis,SINOPEC Shanghai Research Institute of Petrochemical Technology,Shanghai 201208,China;School of Petrochemical Engineering,Changzhou University,Changzhou 213164,Jiangsu,China)
出处 《化工学报》 EI CAS CSCD 北大核心 2019年第2期670-677,共8页 CIESC Journal
基金 国家自然科学基金项目(21878025)
关键词 环氧丙烷 萃取精馏 共沸混合物 分离 优化设计 propyleneoxide extractive distillation azeotrope separation optimal design
  • 相关文献

参考文献4

二级参考文献43

  • 1马书启,李钢,王祥生.TS-1催化1-丁烯环氧化合成1,2-环氧丁烷[J].石油化工,2004,33(z1):1614-1616. 被引量:3
  • 2崔志娱,李志伟,高正虹,张瑞玲,李竞庆.水—1,2-丙二醇二元体系在101.325kPa下的汽液平衡[J].高校化学工程学报,1994,8(4):374-378. 被引量:4
  • 3王惠媛,许松林.常压精馏分离环氧丙烷-甲醇的工艺模拟[J].精细石油化工,2005,22(5):45-47. 被引量:7
  • 4Clericia M G, Bellussia G, Romanob U. Synthesis of propylene oxide from propylene and hydrogen peroxide catalyzed by titanium silicalite [J]. Journal of Catalysis, 1991,129(1 ) :159 - 167.
  • 5Hans-Georg Gobbel, I-Ienning Schultz, Peter Schultz, et al. Separation of propylene oxide from a mixture comprising propylcne and metha- nol: US,7323579 [ P]. 2008 - 01 - 29.
  • 6Aspen技术公司.AspenPluslO.0单元操作模型[Z].Aspen技术公司,2007.
  • 7qDoherty M F, Fidkowski Z T, Malone M F, et al. Perry's chemical engineers' handbook Section 13: Distillation [ M ]. New York: McGraw-Hill ,2008.
  • 8宁波镇海炼化利安德化学有限公司.Q/SH 3065 015—2010工业用环氧丙烷[S]. 2010.
  • 9Halcon International Inc. Separation of Propylene Oxide fromOther Hydrocarbons; US, 3843488 [P] .1974-10-22.
  • 10Arco Chemical Technology L P. Lower Alkylene Oxide Purifica-tion: US, 5133839[P]. 1992-07-28.

共引文献17

同被引文献88

引证文献9

二级引证文献16

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