期刊文献+

一种费托合成尾气的分离方法 被引量:4

下载PDF
导出
摘要 为有效利用费托合成尾气,提高煤间接液化装置的经济性,开发了一种费托合成尾气深冷分离的新工艺。应用PRO/II流程模拟软件对该分离工艺进行了全流程模拟,并对关键工艺参数进行了优化。
出处 《化工进展》 EI CAS CSCD 北大核心 2010年第S1期477-480,共4页 Chemical Industry and Engineering Progress
  • 相关文献

参考文献7

  • 1高军虎,赵璐琦,郝栩,崔富梅,董根全,徐元源,曹立仁,李永旺.煤基费托合成尾气流向变换自热式转化制合成气[J].天然气化工—C1化学与化工,2008,33(3):1-7. 被引量:3
  • 2Charles B Benham,Mark S Bohn,Dennis LYakobson.Process for the production ofhydrocarbons. US,5324335 . 1994
  • 3Charles B Benham,Mark S Bohn,Dennis LYakobson.Process for the production ofhydrocarbons. US,5763716 . 1998
  • 4Walter Schramm.Economic recoveryof ethylene and/or propylene from low concentration feeds. US,4401450 . 1983
  • 5John W Rich,Jr.Integrated electric power and synthetic fuel plant. US,6711903 . 2004
  • 6Ricard O Sheppard,Dennis L,Yakobson.Integrated fischer-Tropsch and power productionplant with low CO2 emissions. US,6976362 . 2005
  • 7Federal Energy Technology Center,U.S Department of Energy.Baseline design/economics for advanced fischer-tropsch technology. . 1998

二级参考文献12

  • 1刘镜远.合成气生产工艺与设计手册[M].北京:化学工业出版社.2001.244-476.
  • 2唐宏青.碳-化工新技术概论[M].成都:《氮肥与甲醇》编辑部,2006.76-93.
  • 3Wilhelm D J, et al. Syngas production for gas-to-liquids applications: technologies, issues and outlook[J].Fuel Process Technol, 2001,71: 139-148.
  • 4Aasberg-Peterson K, et al. Recent developments in autothermal reforming and pre-reforming for synthesis gas production in GTL applications[J]. Fuel Process Technol, 2003, 83: 253-261.
  • 5Kolios G, Frauhammer J, Eigenberger G.Autothermal fixed-bed reactor concepts[J].Chem Eng Sci,2000,55:5945 -5967.
  • 6Matros Y S. Forced unsteady-state processes in heterogeneous catalytic reactors[J]. Can J Chem Eng, 1996,74: 566- 579.
  • 7Matros Y S, Bunimovich G A. Reverse-flow operation in fixed bed catalytic reactors[J]. Catal Rev - Sci Eng, 1996, 38:1-68.
  • 8Eigenberger G, Kolios G, Nieken U. Thermal pattern formarion and process intensification in chemical reaction engineering[J]. Chem Eng Sci, 2007,62: 4825-4841.
  • 9Abdel-aal H K, et al. Simulation of the direct production of synthesis gas from sour natural gas by noncatalytic partial oxidation (NCPO): Thermodynamics and stoichiometry[J]. Ind Eng Chem Res, 1999,35: 1069-1074.
  • 10Khoshnoodi M, Lim Y S. Simulation of partial oxidation of natural gas to synthesis gas using ASPEN PLUS [J]. Fuel Process Technol, 1997,50: 275-289.

共引文献2

同被引文献52

引证文献4

二级引证文献9

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