期刊文献+

具有完全热集成和水集成的合成甲醇精制工艺 被引量:9

Novel purification process of synthetic methanol with full integration of heat and water
下载PDF
导出
摘要 A novel process of three-column(pre-distillation,low-pressure,and high-pressure)distillation was proposed for the purification of synthetic methanol.In the new process with double-effect distillation,the reboiler duties of both pre-column and low-pressure column were provided by the vapor distillate of the high-pressure column,which achieved complete heat-integration of heating steam to reduce the total heat consumption of the whole distillation process.At the same time,the soft water from the bottom of the low-pressure column and part of the salt water from the bottom of the high-pressure column were recycled to the pre-column as the extracting water,which achieved complete integration of soft water in the process and eliminated the consumption of fresh soft water and reduced the amount of waste water.A comparative case study by steady-state simulation was carried out for the present Lurgi process,the W-C process in literature and this Z-W process.The result showed that the Z-W process reduced the heat consumption by 21.4 % of the Lurgi process or by 11.7 % of the W-C process,reduced the waster water by 81.4 % of the Lurgi process or by 68.5 % of the W-C process and eliminated the soft-water consumption by 100 % of both Lurgi process and W-C process. A novel process of three-column(pre-distillation,low-pressure,and high-pressure)distillation was proposed for the purification of synthetic methanol.In the new process with double-effect distillation,the reboiler duties of both pre-column and low-pressure column were provided by the vapor distillate of the high-pressure column,which achieved complete heat-integration of heating steam to reduce the total heat consumption of the whole distillation process.At the same time,the soft water from the bottom of the low-pressure column and part of the salt water from the bottom of the high-pressure column were recycled to the pre-column as the extracting water,which achieved complete integration of soft water in the process and eliminated the consumption of fresh soft water and reduced the amount of waste water.A comparative case study by steady-state simulation was carried out for the present Lurgi process,the W-C process in literature and this Z-W process.The result showed that the Z-W process reduced the heat consumption by 21.4 % of the Lurgi process or by 11.7 % of the W-C process,reduced the waster water by 81.4 % of the Lurgi process or by 68.5 % of the W-C process and eliminated the soft-water consumption by 100 % of both Lurgi process and W-C process.
作者 周志超 吴嘉
出处 《化工学报》 EI CAS CSCD 北大核心 2007年第12期3210-3214,共5页 CIESC Journal
关键词 甲醇精馏 热集成 水集成 过程模拟 methanol distillation heat-integration water-integration process simulation
  • 相关文献

参考文献15

  • 1Tijm P J A, Waller F J, Brown D M. Methanol technology developments for the new millennium. Applied Catalysis A: General, 2001, 221 (1/2): 275-282.
  • 2Ohsaki K, Shojj K, Okuda O. A large scale methanol plant based on ICI process. CEER, 1985, 17 (5): 31-38.
  • 3Song Weiduan(宋维端),Xiao Renjian(肖任坚),Fang Dingye(房鼎业).Methanol Tcchnics(甲醇工学).Beijing:Chemical Industry Press,1991:278-279.
  • 4吴嘉,陈露.具有热集成和水集成的甲醇精馏新工艺及其模拟[J].化工学报,2005,56(3):477-481. 被引量:30
  • 5赵瑞红,赵焕祺,张向京.UNIFAC法在甲醇精馏过程模拟计算中的应用[J].化学工程,2000,28(1):48-51. 被引量:13
  • 6许波.粗甲醇的双塔精馏与三塔精馏[J].化工催化剂及甲醇技术,2002(1):22-24. 被引量:3
  • 7Myungwan Han, Sunwon Park. Multivariable control of double-effect distillation configurations. Journal of Process Control, 1996, 6 (4): 247-253.
  • 8Pohlmeier J, Rix A. Interactive plant and control design of a double effect distillation column. Computers &. Chemical Engineering, 1996, 20 (4): 395-400.
  • 9Bansal V, Ross R, Perkins J D, Pistikopoulos E N. The interactions of design and control: double effect distillation. Journal of Process Control, 2000, 10 (2,/3) : 219-227.
  • 10Zou 1.aixi, Wu Jia. The apply of distribute parallel genetic algorithms in optimizing the strong coupling separation system Proceedings of International Forum on Green Chemical Science & Engineering and Process Systems Engineering 2006. Tianjin: Chemical Industry and Engineering Society of China, 2006, 3:1752-1757.

二级参考文献11

  • 1冯元琦.联醇生产[M].北京:化学工业出版社,1995..
  • 2宋维端.甲醇工学[M].化学工业出版社,1991..
  • 3冯元琦,联醇生产,1995年
  • 4郭天民,多元汽、液平衡和精馏,1983年
  • 5赵焕祺,第一届全国小联醇会议,1977年
  • 6Hilde K Engelien, Truls Larsson,Sisurd Skogestad.Simulation and optimization of heat integrated distillation columns.In:SIMS (Scandinavian Simulation Society) conference.Porsgrunn, Norway:2001.
  • 7Tijm P J A,Waller F J,Brown D M.Methanol technology developments for the new millennium.Europe Chemical News,1998,69(1795):35.
  • 8Ohsaki K,Shojj K,Okuda O.A large-scale methanol plant based on ICI process.CEER,1985,17(5):31-38.
  • 9Lurgi A G.In:Lurgi Gas & Coal Technologies Symposium.Beijing:1994.201-233.
  • 10赵瑞红,赵焕祺,张向京.UNIFAC法在甲醇精馏过程模拟计算中的应用[J].化学工程,2000,28(1):48-51. 被引量:13

共引文献38

同被引文献35

引证文献9

二级引证文献38

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