期刊文献+

抽提蒸馏中溶剂再生塔常见问题解析

Analysis on Common Problems of Solvent Regeneration Tower in Extractive Distillation
下载PDF
导出
摘要 通过对溶剂再生塔开工过程中出现问题的探究,给出了芳烃抽提装置再生塔开工运行常见问题的分析方法,同时给出了判断贫溶剂汽提水换热器出现内漏的判断依据,并指出了再生塔运行对改善溶剂质量、从而减缓溶剂系统管线腐蚀的重要性,以及如何降低溶剂的降解速度、提高装置的运行周期。 By means of analyzing and discussing the problems happened in the solvent regeneration tower during starting running, the common analysis method for regeneration tower running problems was put forward. At the same time, the judgment basis was presented to estimate if there is leakage in the heat exchanger between lean solvent and stripping water.Furtherly the importance of regeneration tower for improving solvent quality and relaxing the pipes' corrosion of solvent system was discussed, how to reduce solvent degradation speed and to increase running period of installation was analyzed.
机构地区 沈阳化工集团
出处 《辽宁化工》 CAS 2016年第3期316-317,共2页 Liaoning Chemical Industry
关键词 再生塔 溶剂 汽提水 regeneration tower solvent stripping water
  • 相关文献

参考文献5

二级参考文献23

  • 1赵国雄.芳烃抽提装置溶剂环丁砜劣化因素探讨[J].石油炼制与化工,1994,25(5):44-48. 被引量:39
  • 2袁忠勋.几种芳烃抽提工艺技术的分析对比[J].石油炼制与化工,1994,25(6):35-41. 被引量:28
  • 3张静轩.环丁砜的改质及其在芳烃抽提装置上的应用[J].石油炼制与化工,1994,25(11):26-29. 被引量:9
  • 4任佳,苏宏业,褚健.分类模糊关联规则挖掘模型及其在芳烃抽提中的应用[J].化工学报,2005,56(11):2137-2141. 被引量:2
  • 5Messac A, Mattson C A. Generating well-distributed sets of Pareto points for engineering design using physical programming [J]. Optim. Eng., 2002, 3: 431-450.
  • 6Das I, Dennis J E. A closer look at drawbacks of minimizing weighted sums of objectives for Pareto set generation in multicriteria optimization problems [J]. Struct: Optim., 1997, 14: 63-69.
  • 7Kim I Y, de Weck 0 L. Adaptive weighted-sum method for bi-objective optimization: Pareto front generation [J]. Struct. Multidisc. Optim., 2005, 29: 149-158.
  • 8Kim I Y, de Week 0 L. Adaptive weighted sum method for multiobjective optimization: a new method for Pareto front generation [J]. Struct. Multidisc. Optim., 2006, 31: 105-116.
  • 9Yu J Choi , Ki W Cho , Byung W Cho , et al. Optimization of the sulfolane extraction plant based on modeling and simulation [J]. Ind. Eng. Chem. Res., 2002, 41 (22): 5504-5509.
  • 10Jafar Mahmoudi , Mohammad Nader Lotfollahi. (Liquid + liquid) equilibria of (sulfolane + benzene + n-hexane), (N-formylmorpholine + benzene + n-hexane), and (sulfolane + N-formylmorpholine + benzene + n-hexane) at temperatures ranging from 298. 15 to 318. 15 K: experimental results and correlation [J]. J. Chem. Thermodynamics, 2010, 42: 466-471.

共引文献110

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