参考文献
[1] 余国琮,黄洁.大型塔板的模拟与板效率的研究(Ⅰ)——不均匀速度场的涡流扩散模型[J].化工学报,1981,32(1):11-19.
[2] YU K T,HUANG J,KU F J.Mathematical modeling of large distillation tray[C].Philadelphia:Paper Presented at the AIChE 88th National Meeting,1980.
[3] 王晓玲.精馏塔板上流体三维流场及传质的模拟[D].天津:天津大学,2002.
[4] WANG X L,LIU C J,YUAN X G,et al.Computational fluid dynamics simulation of three-dimensional liquid flow and mass transfer on distillation column trays[J].Industrial and Engineering Chemistry Research,2004,43(10):2556-2567.
[5] 刘伯潭.流体力学传质计算新模型的研究和在塔板上的应用[D].天津:天津大学,2003.
[6] NAGANO Y,KIH C A.A two-equation model for heat transfer in wallturbulent shear flows[J].Journal of Heat Transfer,1988,110(3):583-589.
[7] 张兆顺.湍流[M].北京:国防工业出版社,2002.
[8] COLIN O,BENKENID A.A new scalar fluctuation model to predict mixing in evaporating two-phase flows[J].Combustion and Flame,2003,134(3):207-227.
[9] 孙志民.化工计算传质学的研究及其在精馏塔中的应用[D].天津:天津大学,2005.
[10] 孙志民,刘春江,袁希钢,等.筛孔塔板浓度场的测量与模拟[J].化工学报,2006,57(8):1878-1883.
[11] SUN Z M,YU K T,YUAN X G,et al.A modified model of computational mass transfer for distillation column[J].Chemical Engineering Science,2007,62:1839-1850.
[12] SUN Z M,LIU B T,YUAN X G,et al.New turbulent model for computational mass transfer and its application to a commercial-scale distillation column[J].Industrial and Engineering Chemistry Research,2005,44(12):4427-4434.
[13] SUN Z M,YU K T,YUAN X G,et al.Prediction of distillation column performance by computational mass transfer method[J].Chinese J Chem Eng,2011,19(5):833-844.
[14] 刘国标.计算传递学及其在填料床与反应过程中的应用[D].天津:天津大学,2006.
[15] LIU G B,YU K T,YUAN X G,et al.A numerical method for predicting the performance of a randomly packed distillation column[J].International Journal of Heat and Mass Transfer,2009,52:5330-5338.
[16] LI W B,LIU B T,YU K T,et al.A new model for simulating distillation column[J].Chinese J Chem Eng,2011,19(5):717-725.
[17] LOCKETT M J.Distillation Fundamentals[M].New York:Cambridge,1986.
[18] COCKX A,DO-QUANG Z,LINE A,et al.Use of Computational fluid dynamics for simulating hydrodynamics and mass transfer in industry ozonation towers[J].Chemical Engineering Science,1999,54:5085-5090.
[19] YU K T,YUAN X G,YOU X Y,et al.Computational fluid-dynamics and experimental verification of two-phase two-dimensional flow on a sieve column tray[J].Chemical Engineering Research and Design,Transactions of the Institute of Chemical Engineers,Part A,1999,77(6):554-560.
[20] 王忠诚.塔板流体力学性能研究——清液层高度、压力降和液相性能的比较和分析[D].天津:天津大学,1989.
[21] NALLASAMY M.Turbulence models and their applications to the prediction of internal flows:A review[J].Computers & Fluids,1987,15(2):151-194.
[22] BELL R L,SOLARI R B.Effect of nonuniform velocity fields and retrograde flow on distillation tray efficiency[J].AICHE Journal,1974,20(4):688-695.
[23] 张敏卿.精馏塔板上液相流速场及温度场的研究[D].天津:天津大学,1990.
[24] ZHANG M Q,YU K T.Simulation of two dimensional liquid phase flow on a distillation tray[J].Chinese Journal of Chemical Engineering,1994,2(1):63-71.
[25] KRISHNA R,VAN BATEN J M.ELLENBERGER J,et al.CFD simulations of sieve tray hydrodynamics[J].Chemical Engineering Research & Design.Transactions of the Institute of Chemical Engineers,Part A,1999,77:639-646.
[26] ZHANG S Q.Chemical Engineering Handbook[M].Jinan:Shandong Science and Technology Press,1986.
[27] Committee.AIChE Research.Bubble Tray Design Manual[M].New York:AIChE,1958.
[28] LEBOEUF F,HUANG G P,KULISA P,et al.Model and computation of discrete jets in crossflow[J].European Journal of Mechanics,B/Fluids,1991,10(6):629-650.
[29] 戴干策,陈敏恒.化工流体力学[M].北京:化学工业出版社,1988.
[30] ZUIDERWEG F J,HOFHOIS P A M,KUZMAIR J.Flow regimes on sieve trays[J].Chem Eng Res Des,1984,62:39.
[31] LAUNDER B E,SPALDING D B.Numerical computation of turbulent flows[J].Computer Methods in Applied Mechanics and Engineering,1974,3(2):269-289.
[32] FLUENT INC.FLUENT User’s Guide[CP].2003.
[33] FERCHICHI M,TAVOULARIS S.Scalar probability density function and fine structure in uniformly sheared turbulence[J].Journal of Fluid Mechanics,2002,461:155-182.
[34] KRISHNA R,VAN BATEN J M,ELLENBERGER J,et al.CFD simulations of sieve tray hydrodynamics[J].Chem Eng Res Des,Trans Inst Chem Eng Part A,1999,77:639-646.
[35] LI W B,LIU B T,YU K T,et al.A new model for the simulation of distillation column[J].Chinese J Chem Eng,2011,19(5):717-725.
[36] LI W B.Theory and application of computational mass transfer for chemical engineering processes.[D].Tianjin:Tianjin University,2012.
[37] SUN Z M.Study on computational mass transfer in chemical engineering[D].Tianjin:Tianjin University,2005.
[38] SUN Z M,LIU B T,YUAN X G,et al.New turbulent model for computational mass transfer and its application to a commercial-scale distillation column[J].Ind Eng Chem Res,2005,44(12):4427-4434.
[39] MURPHREE E V.Rectifying column calculations[J].Ind Eng Chem,1925,17(7):747-750.
[40] HAUSEN H.A definition of exchange efficiency of rectifying plates for binary and ternary mixtures[J].Chem Ind Tech,1953,25:595.
[41] STANDARD G.Studies on distillation-V:Generalized definition of a theoretical plate or stage of contacting equipment[J].Chem Eng Sci,1965,20(6):611-622.
[42] HOLLAND C D,MCMAHON K S.Comparison of vaporization efficiencies with Murphree-type efficiencies in distillation-I[J].Chem Eng Sci,1970,25(3):431-436.
[43] OLDERSHAW C.Perforated plate columns for analytical batch distillations[J].Ind Eng Chem Analytical Edition,1941,13(4):65-268.
[44] SHARMA M M,GUPTA R K.Mass transfer characteristics of plate columns without downcomer[J].Trans Inst Chem Engrs,1967,45(1):T169-T175.
[45] KALBASSI M A,BIDDULPH M W.A modified oldershaw column for distillation efficiency measurements[J].Ind Eng Chem Res,1987,26(6):1 127-1 132.
[46] WANG Z C.Non-ideal multi-component mass transfer and point efficiency on a sieve tray[D].Tianjin:Tianjin University,1997.
[47] HAI N T.Hydrodynamics of sieve trays[D].New South Wales:The University of New South Wales,1980.
[48] Calderbank P H,Moo-Young M.The mass transfer efficiency of distillation and gas absorption plate columns.Part 2[J].Inst Chem Eng Symp Ser,1960,6:59.
[49] GEARY N W,RICE R G.Bubble size prediction for rigid and flexible spargers[J].AIChE J,1991,37(2):161-168.
[50] HESKETH R P,FRASER RUSSELL T W,ETCHELLS A W.Bubble size in horizontal pipelines[J].AIChE J,1987,33(4):663-667.
[51] RAPER J A,KEARNEY M S,BURGESS J M,et al.The structure of industrial sieve tray froths[J].Chem Eng Sci,1982,37(4):501-506.
[52] ZARITSKY N E,CALVELO A.Internal mass transfer coefficient within single bubbles.Theory and experiment[J].Can J Chem Eng,1979,57:58-64.
[53] PRADO M,FAIR J R.Fundamental model for the prediction of sieve tray efficiency[J].Ind Eng Chem Res,1990,29(6):1031-1042.
[54] LIU G B,YU K T,YUAN X G,et al.A numerical method for predicting the performance of a randomly packed distillation column[J].Int J Heat Mass Tran,2009,52:5330-5338.
[55] SHARIAT A,KUNESH J G.Packing efficiency testing on a commercial scale with good(and not so good)reflux distribution[J].Ind Eng Chem Res,1995,24(4):1273-1279.
[56] ENGEL V,STICHMAIR J,GEIPEL W.A new model to predict liquid holdup in packed columns-using data based on capacitance measurement techniques[J].Inst Chem Eng Symp Ser,1997,4:939-947.
[57] STICHLMAIR J,BRAVO J L,FAIR J R.General model for prediction of pressure drop and capacity of countercurrent gas/liquid packed columns[J].Gas Separation and Purification,1989,3(3):19-28.
[58] WAGNER I,STICHLMAIR J,FAIR J R.Mass transfer in beds of modern,high-efficiency random packings[J].Industrial Engineering Chemistry Research,1997,36:227-237.
[59] KHALIL E E,SPALDING D B,WHITELAW J H.Calculation oflocal flow properties in 2-dimensional furnaces[J].International Journal of Heat and Mass Transfer,1975,18(6):775-791.
[60] 王绍亭,陈树章,李春利.填料塔液相轴向混合的几种参数估计方法[J].化学工程,1988,16(5):46-51.
[61] MICHELL R W,FURZER I A.Mixing in trickle flow through packed beds[J].The Chemical Engineering Journal,1972,4(1):53-63.
[62] EARL A,EBACH R R W.Mixing of fluids flowing through beds of packed solids[J].AIChE Journal,1958,4(2):161-169.
[63] CHOE D K,LEE W L.Liquid phase dispersion in a packed column with countercurrent two-phase flow[J].Chemical Engineering Communication,1985,34:295.
[64] STRANG D,GEANKOPLIS C.Longitudinal diffusivity of liquids in packed beds[J].Industrial & Engineering Chemistry,1958,50(9):1305-1308.
[65] OTAKE T,KUNUGITA E.Mixing characteristics of irrigated packed towers[J].Journal of Chemical Engineering of Japan,1958,22:144.
[66] LION D,TAN C S.Axial dispersion of supercritical carbon dioxide in packed bed[J].Ind Eng Chem Res,1989,28(8):1246-1250.