The Development In Packed Tower Research

Abstract The development in packed tower research till the end of 1991 is briefly reviewed with certain accent to recent investigation and domestic works. The present status of research and results in correlation about the performance of packed bed are presented. With respect to mass transfer, not only important results are included but also the probable cause of wide deviation in correlations by different authors is discussed in some detail

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Keywords�� packed tower tower packing fluid flow mass transfer

Received 1993-01-15; published 1993-01-15

Cite this article:

Mai Benxi .The Development In Packed Tower Research[J] Chemcial Industry and Engineering, 1993,V10(1): 16-27

[1]	Eckert J S. How tower packings behave. Chem Eng, 1975, 82(8) : 70��76
[2]	�Ͼ��ѧԺ.��ѧ��(��)--��Һ��ʱ��ѹ��.��ѧ��,1977,(4) :43��59
[3]	�Ͼ��ѧԺ.��ѧ��(��)--��ڵ�Һ��.��ѧ��,1977,(6) :55��65
[4]	��.��ϵ��ѧ��ܹ��.��ѧ��,1981,(6) :41��50
[5]	�°�.��Һ��ٶȵľ��ģ��.��ѧ��,1983,(6) :61��65
[6]	��־�.��Һ��ٶȼ��ʽ.��ѧ��,1987,(2) :26��30
[7]	��,��,��.��Һ��ٶȹ��ʽ�ĸĽ�,ʯ�ͻ��,1989,18(6) :371��373
[8]	��Դ.�Ҷ��ϲ�ѹ��뾭��ͨ�ù��ʽ.��ѧ��,1982,(3) :26��37
[9]	��Դ.��ͨ�ù��ͼ.��ѧ��,1988,39(2) :232��238
[10]	��Դ.��Һ��ʽ[J].��ѧ��ҵ�빤��.1989,6(3):16-26 ��
[11]	��Զƽ,�ܴ��.��ѹ��Һ��ʽ.��ѧ��,1990,18(3) :41��43
[12]	�Ĳ��,��,Ī��.��Һ��ͺ�ѹ��.��ѧ��,1991,19(5) :60��65
[13]	Bemer G G, Kalis G A J. A new method to predict hold-up and pressure drop in packed columns. Tran Inst them Engrs, 1978, 56(3) : 200��204
[14]	Takanaski T, Akagi Y, Ueyama K. A new correlation for pressure drop of packed columns[J].Journ Chem Eng Jpn.1979, 12(5):341-346
[15]	Bravo J L, Rocha J A, Fair J R. Pressure drop in structure packings. Hydto Carbon Proc, 1986, (3) : 45��49
[16]	Fair J R, Bravo J L. Distillation containing structure Packings. Chem Eng Prog, 1990, 86(1) : 19��29
[17]	Kister H Z, Gill D R. Predict flood point and pressure drop for modern random packings. Chem Eng Prog, 1991, 87(2) : 32��42
[18]	Robins L A. Improve pressure drop prediction with a new correlation. Chem Eng Prog, 1991, 87(5) : 87��91
[19]	Shulman H L, Ullrich C F, Wells N. Performance of packed columns,��-Total, static and operating holdups[J].AIChE Journ.1955, 1(2):87-91
[20]	Billet R, Schultes M. Determination of liquid hold-up in gas-liquid two-phase countercurrent mass transfer columns �� Chem Symp Series, 1987, No. 104,A: 159��170
[21]	١��,Ī��.��Һ��о�(��)--�ص��µĳ�Һ��.��ѧ��,1983,(6) :17��21
[22]	١��,Ī��.��Һ��о�(��)--��µĳ�Һ��.��ѧ��,1984,(1) :21��25
[23]	��ʩ��,Ī��.��Һ��о�(��)--�ص㵽��֮��ĳ�Һ��.��ѧ��,1986,(3) :1��4
[24]	��ʩ��,Ī��.��Һ��о�(��)--��Һ��ѹ��Ӱ��.��ѧ��,1986,(4) :7��12
[25]	�Ĳ��,��,Ī��.��Һ��²��ĳ�Һ��.��ѧ��,1989,(6) :15��21
[26]	��,��ε֮.��Һ��ĳ�Һ��.��ѧ��,1990,18(4) :41��49
[27]	Porter K E. Liquid flow in packed columns Pt. �� The spread of liquid over random packings. Tran Inst Chem Engrs. 1968, 46(3) : T69��73, T74��85
[28]	Porter K E. Liquid flow in packed columns Pt. ��-Wall flow. Tran Inst Chem Engrs, 1968, 46(3) : T86��94
[29]	Patwardhan V S, Pataskar S G. The influence of wettability on the equilibrium wall flow of liquid in Packed Columns[J].Chem Eng Journ.1982, 23(2):145-149
[30]	Hoek P J, Wsselingh J A, Zuiderwig F J. Small scale and large scale liquid mildistribution in packed columns. Chem Eng Res Des, 1986, 64 (6) : 431��449
[31]	Chila Z, Schmidt O. Coll Czech Chem Eng Comm, 1957, 22: 896
[32]	Kolar V, Stanonek V. Coll Czech Chem Eng Comm, 1965, 30: 1045
[33]	Datkai E, Ruckenstein E. Liquid distribution in packed columns[J].Chem Eng Sci.1968, 23:1365-1373
[34]	Bemer G G, Zuiderweg F J. Radial liquid spread and maldistribution in packed columns under different wetting conditions. Chem Eng Sci, 1987, 33(12) : 1637��1643
[35]	Furzer I A. L quid dispersion in packed columns ��-the Dutkai-Ruckenstein model; ��-the Gunn model[J].Chem Eng Sci.1984,39(7/8):1283-1300
[36]	��ͥ,��,��.��ģ��Һ��ֲ�.��ѧ��,1988,39(2) :162��169
[37]	��ͥ,��,��.��Һ��ϵ��о�(��)--��һά��ɢģ��.��ѧ��,1988,39(3) :285��298
[38]	��ͥ,��,��.��Һ��ϵ��о�(��)--��ά��ɢ��ģ��.��ѧ��,1988,39(3) :292��298
[39]	ԬТ��,���,��.��Һ��ֲ�״̬��о�.��ѧ��,1989,40(6) :686��692
[40]	ԬТ��,��.��岨��Һ��ģ��о�.��ѧ��,1987,(6) :45��54
[41]	��,¥��,��Ȫ.��岨��Һ��е��о�.��ѧ��,1986,(4) :402��411
[42]	��,�컦��.��Ȫ.��Һ��ֲ��о�.��ѧ��,1986,(4) :13��19
[43]	Stockar U, Cevey P F. Influence of the physical properties of the liquid on axial despersion in packed columns[J].Ind Eng Chem Proc Des Dev.1984, 23(4):717-724
[44]	��ͤ,��,��ƽ,��.��Һ��Һ��ϵ��о�.��ѧ��,1985,(6) :35��42
[45]	��ͤ,��,��ƽ.��Һ��Һ��ϵ��о�.��ѧ��,1985,(4) :475��483
[46]	Shi M G, Mersmann A. Effective interfacial area in packed columns. Ger Chem Eng, 1985, 8(2) : 87��96
[47]	½��ά.��ϵ��ʪ.��,1986,(1/2) :1��6
[48]	Linek V, Stoy V, Machon V, Krivsky Z. Increasing the effective interfacial area in plastic packed absorption columns Chem Eng Sci. 1974, 29(9) : 1955��1960
[49]	Linek V, Petricek P, Braun R. Effective interfacial area and liquid side mass transfer coefficients in absorption columns packed with hydrophilised and untreated plastic packings. Chem Eng Res Des, 1984, 62(1) : 13��21
[50]	��ռƽ,�ﴺ��,��.�۱�ϩ��ϱ��ˮ��о�.��ѧ��,1988,16(5) :26��29
[51]	�辴��.�۱�ϩ��ϵ��ʪ�ͱ��洦��.��ѧ��,1991,19(1) :33��36
[52]	½��ά,�ﴺ��,��.�۱�ϩ��ϵı��Լ��ѧ�ʹ��ʵ�Ӱ��.ʯ�ͻ��豸.1991,20(2) :22��25
[53]	Shulman H L, Ullrich C F, Proulx A Z, Zimmerman J O. Performance of packed columns. Wetted and effective interfacial areas, gas and liquid phase mass transfer rates. AIChE Journ, 1955, 1 (2) : 253��258
[54]	Echarte R, Campana H, Brignole E A. Effective areas and liquid film mass transfer coefficients in packed columns. Ind Eng Chem Proc Des Dev, 1984, 23 (2) : 249��254
[55]	Danckwerts P V. Gas liquid rections. Mc Graw-Hill, 1970, chapter 9
[56]	Sharma M M, Danckwerts P V. Chemical methods for measuring interfacial area and mass transfer coefficient in two-liquid system. Brit Chem Eng, 1970, 15(4) : 522��528
[57]	Onda K, Takeuchi H, Okumotov Y. Mass transfer coefficients between gas and liquid phases in packed columns[J].Journ Chem Eng Jpn.1968, 1(1):56-62
[58]	Puranik S S, Vogelpohl A. Effective interfacial area in irrigated columns[J].Chem Eng Sci.1974, 29(2):501-507
[59]	��,��,��Դ.��ֿ��ϵ��о�(��)--��Ч��.��ѧ��,1989,17(1) :21��25
[60]	Charpentier J C, Recent progress in two Phase gas-liquid mass transfer in Packed beds. Chem Eng Journ, 1976, 11(3) : 161��181
[61]	Ponter A B, Au-Yeung P H. Estimation of liquid film mass transfer coefficient for randomly Packed absorption columns. Canad Journ Chem Eng, 1983, 61(4) : 481��493
[62]	Connel D, KnaPP W G, Fair J R. Mass transfer in Packed columns-Pt 1�� Chem Eng Prog, 1960, 56(7) : 68��74
[63]	Connel D, KnaPP W G, Fair J R. Mass transfer in Packed columns--Pt 2�� Chem Eng Prog, 1960, 56(8) : 48��53
[64]	Bolles W L, Fair J R. Performance and design of Packed distillation Columns. �� Ch E SymP Series, 1979, No. 56, 3�� 3/3�� 5-89
[65]	Bolles W L, Fair J R. ImProved mass transfer model enhances Packed column design. Chem Eng, 1982, 89(14) : 109��116
[66]	Davidson J F. The hold uP and liquid film coefficient of Packed towers Pt ��: Static models of the random Packing. Tran Inst Chem Eng, 1959, 37: 131��136
[67]	Porter K E, Mc Jones. Liquid and gas distribution in the scale uP of Packed columns. �� Ch E SymP Series, 1987, No. 104: A245��254
[68]	��Դ,̸��,���.��ֿ��ϴ��ܵ��о�.��ѧ��,1980,(4) :375��386
[69]	��.��ֿ��ϵ��о�(��)--��ϵ��ʽ.��ѧ��,1986,(4) :1��6
[70]	Bravo J L, Rocha J A, Fair J R. Mas transfer in gauze Packings. Hydrocarbon Proc, 1985, 64(1) : 91��95
[71]	Nawrocki P A, Xu Z P, Chuang K T. Mass transfer in structure corrugated Packing[J].Canad Journ Chem Eng.1991, 69(12):1336-1343
[72]	�ܽ��,��,��Դ.��ֿ��ϵ��о�(��)--��Һ��ڵĲ��.��ѧ��,1987,(6) :1��6
[73]	Billet R. Performance of low Pressure droP Packings[J].Chem Eng Comm.1987, 54(1/6):93-118
[74]	Billet R, Mackowiak J. APPlication of modern Packings in thermal seperation Processes[J].Chem Eng Technol.1988, 11 (1/6):213-227