[1] Bravo J L,Rocha J A,Fair J R. Mass transfer in gauze packings[J]. Hydrocarbon Processing,1985,64(1):91-95.[2] Bravo J L,Rocha J A,Fair J R. Pressure drop in structured packings[J]. Hydrocarbon Processing,1986,65(3):45-49.[3] Rocha J A,Bravo J L,Fair J F. Distillation columns containing structured packings:A comprehensive model for their performance. Ⅰ. Hydraulic models[J]. Ind. Eng. Chem. Res.,1993,32(4):641-651.[4] Rocha J A,Bravo J L,Fair J F. Distillation columns containing structured packings:A comprehensive model for their performance. Ⅱ. Mass-transfer model[J]. Ind. Eng. Chem. Res.,1996,35(5):1660-1667.[5] Gualito J J,Cerino F J,Cardenas J C. Design method for distillation columns filled with metallic,ceramic,or plastic structured packings[J]. Industrial & Engineering Chemistry Research,1997,36(5):1747-1757.[6] Billet R,Schultes M. Prediction of mass transfer columns with dumped and arranged packings - Updated summary of the calculation method of Billet and Schultes[J]. Chemical Engineering Research & Design,1999,77(A6):498-504.[7] Tsai R E,Schultheiss P,Kettner A. Influence of surface tension on effective packing area[J]. Ind. Eng. Chem. Res.,2008,47(4):1253-1260.[8] Tsai R E,Seibert A F,Eldridge R B. Influence of viscosity and surface tension on the effective mass transfer area of structured packing[J]. Energy Procedia,2009,1(1):1197-1204.[9] Tsai R E,Seibert A F,Eldridge R B. A dimensionless model for predicting the mass-transfer area of structured packing[J]. AIChE Journal,2011,57(5):1173-1184.[10] Hanley B,Chen C. New mass-transfer correlations for packed towers[J]. AIChE Journal,2012,58(1):132-152.[11] Zuiderweg F J,Harmens A. The influence of surface phenomena on the performance of distillation columns[J]. Chem. Eng. Sci.,1958,9(2):89-103.[12] Moens F P. The effect of composition and driving force on the performance of packed distillation columns -I[J]. Chem. Eng. Sci.,1972,27(2):275-283.[13] Moens F P. The effect of composition and driving force on the performance of packed distillation columns - II[J]. Chem. Eng. Sci.,1972,27(2):285-293.[14] Patberg W B,Koers A.Effectiveness of mass transfer in a packed distillation column in relation to surface tension gradients[J]. Chem. Eng. Sci.,1983,38(6):917-923.[15] Kolev N,Semkov K. On the evaluation of the interfacial turbulence (the Marangoni Effect) in gas (vapour)-liquid mass transfer:Part II. Modelling of packed columns accounting for axial mixing and Marangoni effects[J]. Chemical Engineering and Processing:Process Intensification,1991,29(2):83-91.[16] Proctor S J,Biddulph M W,Krishnamurthy K R. Effects of Marangoni surface tension forces on modern distillation packings[J]. AIChE Journal,1998,44(4):831-835.[17] Xu Z P,Afacan A,Chuang K T. Predicting mass transfer in packed columns containing structured packings[J]. Chemical Engineering Research & Design,2000,8(A1):91-98.[18] 耿皎,洪梅,肖剑. 规整填料塔精馏的 Marangoni 效应[J]. 化工学报,2002,53(6):600-606.[19] 刘光启,马连湘,刘杰.化学化工物性数据手册有机卷[M]. 北京:化学工业出版社,2002:134-135.[20] 王树楹. 现代填料塔技术指南[M]. 北京:中国石化出版社,1998:11-12.[21] Basden M,Eldridge R B,Farone J,et al. Liquid holdup profiles in structured packing determined via neutron radiography[J]. Industrial &Engineering Chemistry Research,2013,52(48):17263-17269. |