SINGLE-DROP MASS TRANSFER COEFFICIENTS IN MULTICOMPONENT SYSTEMS 被引量：2

SINGLE-DROP MASS TRANSFER COEFFICIENTS IN MULTICOMPONENT SYSTEMS

下载PDF

导出

作者魏海国费维扬朱慎林

出处《化工学报》 EI CAS CSCD 北大核心 2002年第7期665-666,共2页 CIESC Journal

基金 supportedbytheNationalNaturalScienceFoundationofChina (No .2 983 613 0 )andTsinghuaUniversityBasicResearchFund (No.JZ2 0 0 0 0 0 8)

关键词多组分体系单液滴传质系数传质过程化工过程 multi-component system,mass transfer coefficient,single-drop,aromatics extraction,sulfolane

分类号 TQ021.4 [化学工程]

引文网络
相关文献

参考文献6

1魏海国,费维扬,WEI Hai-guo,FEI Wei-yang.非平衡级模型及其在化工分离过程中的应用[J].石油化工,2001,30(6):486-490. 被引量：7
2Clift R,Grace J R,Weber M E.Bubbles, Drops and Particles[]..1978
3Slater M J,Baird H I,Liang T- B. Chemical Engineering Science . 1988
4Steiner L. Chemical Engineering Science . 1986
5Kirshna R,Standart G L. Chemical Engineering Communications . 1979
6Kirshnamurthy R,Taylor R. American Institute of Chemical Engineers Journal . 1985

二级参考文献3

1许锡恩,郑宇翔,李家玲,董为毅.催化蒸馏合成乙二醇乙醚的过程模拟[J].化工学报,1993,44(3):269-276. 被引量：22
2朱建华,沈复.反应精馏过程的非平衡级模型初探[J].计算机与应用化学,1994,11(3):167-173. 被引量：8
3秦永胜,徐用懋,方崇智,唐杰.多元精馏塔非平衡级模型与仿真──Ⅰ．模型的建立与求解[J].石油炼制与化工,1996,27(3):35-39. 被引量：2

共引文献6

1魏海国.多组分体系液滴群的传质因数[J].金山油化纤,2004,23(2):11-13. 被引量：1
2晋正茂,王维德.反应精馏及其研究进展[J].化学工业与工程技术,2006,27(3):10-14. 被引量：16
3杨亭,王东岩,关威,张双双,常虹,张述伟.基于非平衡级速率模型的低温甲醇洗吸收塔模拟研究[J].大氮肥,2010,33(5):297-301.
4凌鸿钰,顾正桂,曹晓艳.从LCO中提取三甲基萘的模拟及试验研究[J].计算机与应用化学,2019,36(6):652-658.
5魏海国,费维扬,朱慎林.环丁砜芳烃抽提体系界面性质的研究[J].高校化学工程学报,2003,17(1):6-12. 被引量：1
6秦建华.反应精馏技术的关键问题分析[J].扬州工业职业技术学院论丛,2008,0(2):1-7.

同被引文献12

1罗耀明,张秋香,陈晓祥.液液传质界面扰动现象的全息实时记录[J].高校化学工程学报,1995,9(2):149-154. 被引量：6
2Pratt A.J.F. In T. C. Lo et al. eds. Handbook of solvent extraction[ M ]. New York :John Wiley&Sons Ltd, 1983:91-121.
3Slater M. J. Baird H. I. , Liang T - B Drop Mass transfer coefficients for liquil - liquid Systems and the lnflenee of Packings. Chem. Eng.Sci. , 1988,43 (2) :233 - 245.
4Steiner L. Mass Transfer from Single Drops and Drop Swarms.Chem. Eng. Sei. , 1986,41(7) :1979- 1986.
5Toor H. L. Diffusion in Three Component Gas Mixtures. AIChE J. ,1957,3 ( 1 ) : 198 - 201.
6Taylor R., Kirshna R. Multicomponent Mass Transfer [ M ]. New York,Wiley & Sons, 1993.
7陈晓祥,高浩其.液液传质界面扰动的实验研究[J].厦门大学学报（自然科学版）,1998,37(2):233-238. 被引量：2
8沙勇,李樟云,林芬芬,吐松,肖宗源,叶李艺.气液传质界面湍动现象投影观察[J].化工学报,2010,61(4):844-847. 被引量：14
9魏海国,费维扬,WEI Hai-guo,FEI Wei-yang.非平衡级模型及其在化工分离过程中的应用[J].石油化工,2001,30(6):486-490. 被引量：7
10沙勇,成弘,余国琮.质量、热量传递过程中的Marangoni效应[J].化学进展,2003,15(1):9-17. 被引量：22

引证文献2

1魏海国.多组分体系液滴群的传质因数[J].金山油化纤,2004,23(2):11-13. 被引量：1
2邱挺,洪素芬,郭川,吕远炬.乙酸仲丁酯-乙酸-水萃取体系的传质行为[J].化工学报,2011,62(11):3171-3178. 被引量：2

二级引证文献3

1马力,仇性启,王健,郑志伟,易志勇,阎红巧.单液滴蒸发影响因素实验研究[J].现代化工,2013,33(1):103-106. 被引量：20
2吕建华,高梦璠,李品,殷明海.水萃取氯丙醇的传质性能[J].化学工程,2015,43(8):27-32.
3黄智贤,林毅雄,王红星,叶长燊,李玲.高密度差体系中单液滴运动的数值模拟[J].化工进展,2016,35(B11):61-67.

1阎恭喜,朱自强,关怡新,韩兆熊.Measurement of Mass Transfer Coefficients and Their Modelling of Continuous Counter-Current Aqueous Two-Phase System in a Packed Extraction Column[J].Chinese Journal of Chemical Engineering,1999,7(3):196-204. 被引量：1
2Rubber prices may drop 22 percent by the end of 2010[J].橡塑机械时代,2010,22(5):9-9.
3Shi Mingxian, Jin Youhai, Wu Xiaolin, Chen Jianyi, Liu Junren (United Research Institute of Applied Chemistry and Chemical Engineering, University of Petroleum, Beijing 100083).Research on High-Efficiency Cyclone Separators and Their Optimum Design[J].石油学报（石油加工）,1997,13(S1):19-27. 被引量：1
4MA QingLan,CHEN GuangJin.Prediction of vapor-liquid-liquid-hydrate phase equilibrium for multicomponent systems containing tetrahydrofuran[J].Science China Chemistry,2013,56(12):1800-1810. 被引量：2
5Gabriel Zarca,Inmaculada Ortiz,Ane Urtiaga.Recovery of carbon monoxide from flue gases by reactive absorption in ionic liquid imidazolium chlorocuprate(I): Mass transfer coefficients[J].Chinese Journal of Chemical Engineering,2015,23(5):769-774. 被引量：2
6WANG JianFeng,YANG Chao,MAO ZaiSha.Numerical simulation of Marangoni effects of single drops induced by interphase mass transfer in liquid-liquid extraction systems by the level set method[J].Science China Chemistry,2008,51(7):684-694. 被引量：4
7Mehdi Asadollahzadeh,Ahad Ghaemi,Meisam Torab-Mostaedi,Shahrokh Shahhosseini.Experimental mass transfer coefficients in a pilot plant multistage column extractor[J].Chinese Journal of Chemical Engineering,2016,24(8):989-999. 被引量：3
8李玉安,赵培,刘吉,张杰旭,路秀林.Directed Valve Trays[J].Chinese Journal of Chemical Engineering,1998,6(1):95-98.
9屈一新,汪文川,Lee,Y.Y.,Chung,K.Y.,Lee,Y.W..A G^E/Equation of State Mixing Rule for Vapor-Liquid Equilibria[J].Chinese Journal of Chemical Engineering,1998,6(3):14-28.
10鲍晓军,陈家镛.GRAVITY SETTLING OF DISPERSED PHASE DROP SWARMS IN EXTRACTION COLUMNS IN ABSENCE OF MASS TRANSFER[J].Chinese Journal of Chemical Engineering,1994,2(1):11-22.

化工学报

2002年第7期

浏览历史

内容加载中请稍等...