[1] | BEENACKERS A A C M,VAN SWAAIJ W P M.Masstransfer in gas-liquid slurry reactors[J].Chem Eng Sci,1993,48:3 109-3 139. |
[2] | ���,����.���Ϲ�����������������ǿ��Һ�����о�[D].���:����ѧ,2004. |
[3] | ���֮,����,ë��ɰ.����ʽ��-Һ-Һ��Ӧ�������ɢ�ʹ�������[J].ʯ�������뻯��,2000,31(10):54-59. |
[4] | ����,��ӧ,����.��ҺҺ������ϵ�Ķ�ά�Ǿ��ഫ��ģ�������[C].���:�ڰ˽�ȫ����ѧ�������ı�������ļ�,1996. |
[5] | �ɺ�.������ϸ����ǿ��Һ���ഫ�ʵĻ����о�[D].���:����ѧ,1997. |
[6] | GOMEZPLATA A,REGAN T M.Mass transfer[J].IndEng Chem,1970,62(12):17-26. |
[7] | ��͢��,������.��������������ϳ�����������ȡ���ɹ����о�[J].�Ĵ���ѧѧ��:���̿�ѧ��,2002,34(5):102-105. |
[8] | ������,��ݰ.��-Һ-Һ���䷴Ӧ��ȡ�Ʊ���������Ĺ���[J].����ѧ��,2003,54(11):1 654-1 657. |
[9] | JOOSTEN G E H,SCHILDER J G M,JANSSEN J.Theinfluence of suspended solid material on the gas-liquid masstransfer in stirred gas-liquid contactors[J].ChemicalEngineering Science,1977,32(5):563-566. |
[10] | NIENOW A M,KONE M,BUJUSKI W.Studies on thethree-phase mixing:A review and recent results[J].ChemEng Res Des,1986,64(1):35-42. |
[11] | SCHMITZ M,STEIFF A.Gas/liquid interfacial area per unit10 and 10tric mass transfer coefficient in stirredslurry reactors[J].Chem Eng Tech.1987,10(3):204-215 |
[12] | HAMBY N,EDWARDS M F,NIENOW A W.��ҵ�еĻ�Ϲ���[M].������,��.����:�й�ʯ��������,1991. |
[13] | ���,���ɲ�,�´���.��-Һ-������������Һ�����������ܵ��о�[J].��ѧ��ҵ�빤��,1997,14(2):17-22,38. |
[14] | SHARMA M M.Perspectives in gas-liquid reactions[J].Chem Engng Sci.1983,38(5):21- |
[15] | ALPER E,OZTIIRK S.The effect of activated carbonloading on oxygen absorption into aqueous sodium sulphidesolutions in a slurry reactor[J].Chem Engng J(Lausanne.1986,32(2):127-130 |
[16] | ������.����ѭ���������е���Һ�������ʹ���ϵ��[J].����ұ��,2000,21(4):10. |
[17] | KARS R L,BEST R J,DRINKENBURG A A H.Theadsorption of propane in slurries of active carbon in water[J].Chemical Engineering Journal,1979,17(3):201-210. |
[18] | ALPER E,DECKWER W D.Comments on gas absorptionwith catalytic reaction[J].Chemical Engineering Science.1981,36:1- |
[19] | SCHMITZ M,STEIFF A,WEINSPACH P M.Gas-liquidinterfacial area per unit volume and volumetric mass transfercoefficient in stirred slurry reactors[J].Chem EngngTechnol,1987,10(3):204-215. |
[20] | ������.������ϵ��ϸ������ǿ��Һ�����о�[D].���:����ѧ,2003. |
[21] | �ɺ�.������ϸ����ǿ��Һ���ഫ��(��)����[J].����ѧ��,1999,50(6):12. |
[22] | LI Yiao-ping.Gas-liquid mass transfer in multiphasemechanically stirred airlift reactor[J].Journal of NanjingUniversity of Chemical Technology,1998,20(3):51-55. |
[23] | MILLS D B,RAPHAEL B,KIIRWAN D J.Effect of solidson oxygen transfer in agitated three-phase system[J].AIChE Journal.1987,33(9):1- |
[24] | �º�ѫ.��ϸ̼���������������Һ�����෴Ӧ���о�[D].���:�ӱ���ҵ��ѧ,2000. |
[25] | SADA E.Gas holdup and mass transfer characteristics in athree phase bubble column[J].Industrial&EngineeringChemistry Process Design and Development.1986,25(2):472-476 |
[26] | GODBOLE S P,SCHUMPE A,SHAH Y H.Effect of solidwettability on gas-liquid mass transfer in a slurry bubblecolumn[J].Chemical Engineering Science,1990,45(12):3 593-3 595. |
[27] | ���绪,����.�����е���跴Ӧ����Һ����[J].����ѧ��,2005,56(2):220-226. |
[28] | WIMMERS O J,FORTUIN J M H.The use of adhesion ofcatalyst particles to gas bubbles to achieve enhancement ofgas absorption in slurry reactors��.Investigation ofparticle-to-bubble adhesion using the bubble pick-up method[J]..Chemical Engineering Science.1988,43(2):303-312 |
[29] | PANDIT A B,JOSHI J B.Mass and heat transfercharacteristics of three phase sparged reactors[J].ChemicalEngineering Research&Design.1986,64(2):125-157 |
[30] | NAGARAJ N,GRAY D J.Interfacial area and coalescencefrequency in gas-slurry stirred reactors[J].AIChE Journal.1987,33(9):1- |
[31] | QUICKER G,ALPER E,DECKWER W D.Effect of fineactivated carbon particles on the rate of CO2absorption[J].AIChE Journal.1987,33(5):871-875 |
[32] | MEHRA A.Gas absorption in slurries of finite-capacitymicrophases[J].Chem Eng Sci.1990,45:1- |
[33] | Van der MEER A B,BEENACKERS A A C M,BURGHARD R,et al.Gas/liquid mass transfer in a four-phase stirred fermentor:Effects of organic phase hold-upand surfactant concentration[J].Chem Eng Sci,1992,47:2 369-2 374. |
[34] | �ֳ�,����,����.������ϸ����ǿ��Һ���ഫ��(��)ʵ��[J].����ѧ��,1999,50(4):469-476. |
[35] | �ֳ�,����,����,��.��ɢ�ڶ�Һ�����ǿ��Һ���ʵ�Ӱ��[J].��ѧ����,2000,28(2):23-33. |
[36] | BRUINING W J,JOOSTEN G E H,BEENACKER A A CM,et al.Enhancement of gas-liquid mass transfer by adispersed second liquid phase[J].Chem Eng Sci.1986,41:1- |
[37] | BRUINING W J,JOOSTEN G E H,BEENACKERS A A CM,et al.Enhancement of gas-liquid mass transfer by adisperse second liquid phase[J].Chem Eng Sci.1986,41(7):1- |
[38] | CENTS A H G,BRILMAN D W F,VERSTEEG G F.Gasabsorption in an agitate gas-liquid-liquid system[J].ChemEng Sci,2001,56:1 075-1 083. |
[39] | DECKWER W D,NGUYEN-TIEN K,KELKAR B G.Applicability of axial dispersion model to analyze masstransfer measurements in bubble columns[J].AIChEJournal,1983,6(29):915-921. |
[40] | ���֮,����,ë��ɰ.����ʽ��-Һ-Һ��Ӧ�������ɢ�ʹ�������[J].ʯ�������뻯��,2000,31(10):54-59. |
[41] | HASSAN I T M,ROBINSON C W.Oxygen transfer inmechanically agitated systems containing dispersedhydrocarbon[J].Biotechnol Bioeng.1977,19:661-682 |
[42] | JANAKIRMAN B,SHARMA M M.Solid-liquid and liquid-liquid slow and fast reaction[J].Chem Engng Sci.1985,40:235-245 |
[43] | JUNKER B H,HATTON T A,WANG D I C.Oxygentransfer enhancement in aqueous/per-fluorocarbonfermentation systems��.Experimental observations[J]..Biotechnol Bioengng.1990,35:578-591 |
[44] | ROLS J L,CONDORET J S,FONADE C.Modeling ofoxygen transfer in water through emulsified organic liquids[J].Chem Engng Sci.1991,46:1- |
[45] | DUMONT E,DELMAS H.Mass transfer enhancement ofgas absorption in oil-in-water systems:A review[J].ChemEng Pro,2003,42:419-438. |
[46] | ALPER E,DECKWER W D.Some aspects of gasabsorption mechanism in slurry reactors[J].NATO ASISeries E,1983,73(2):199-224. |
[47] | YOSHIDA F,YAMANE T,MIYAMOTO Y.Oxygenabsorption into oil-in-water emulsions[J].Industrial andEngineering Chemistry:Process Design and Development.1970,9:570-577 |
[48] | LITTLE R J,VERSTEEG G F,Van SWAAIJ W P M.Physical absorption of CO2and propene into toluene/wateremulsions[J].AIChE Journal.1994,40:1- |
[49] | ROLS J L,CONDORET J S,FONADE C,et al.Mechanism of enhanced oxygen transfer in fermentationusing emulsified oxygen-vectors[J].Biotechnology andBioengineering.1990,35:427-435 |
[50] | Van EDE C J,van HOUTEN R,BEENACKERS A A C M.Enhancement of gas to water mass transfer rates by adispersed organic phase[J].Chem Engng Sci,1995,50:2 911-2 930. |
[51] | DAS T R,BANDOPADHYAY A,PARTHASARATHY R,et al.Gas-liquid interfacial area in stirred vessels:Theeffect of an immiscible liquid phase[J].Chem Eng Sci.1985,40(2):209-214 |
[52] | LINEK V,BENES P.A study of the mechanism of gasabsorption into oil-water emulsions[J].Chem Eng Sci.1976,31(11):1- |
[53] | MEHRA V D,SHARMA M M.Mass transfer inmechanically agitated gas-liquid contactors[J].Chem EngSci.1971,26:461-479 |
[54] | ROLS J L,CONDORET J S,FONADE C,et al.Mechanism of enhanced oxygen transfer in fermentationusing emulsified oxygen-vectors[J].Biotechnol Bioeng.1990,35:427-435 |
[55] | SHARMA M M,MASHELKAR R A.Absorption withreaction in bubble columns[J].Chem E Symp Series,1968,28:10-21. |
[56] | ���Ǿ�.��̬���������ȡ��������ѧ����������Ӱ����о�[D].����:��������ѧ,2005. |
[57] | KOIDE K.Gas holdup and 17tric liquid-phase masstransfer coefficient in solid-suspended bubble columns[J].Journal of Chemical Engineering of Japan.1984,17(5):459-466 |
[58] | JU L K,LEE J F,ARMIGER W B.Enhancing oxygentransfer in bioreactors by perfluorocarbon emulsions[J].Biotechnology Progress,1991,37:505. |
[59] | ���ѹ�,������,�ɺ�,��.4�ֱ�����Լ���CO2�������չ��̽�����Ũ��Ӱ����о�[J].����ѧ��,1999,50(6):776. |
[60] | DAS T R,BANDOPADHYAY A,PARTHASARAT R,etal.Gas-liquid interfacial area in stirred vessels:The effectof an immiscible liquid phase[J].Chem Eng Sci.1985,40(2):209-214 |
[61] | DAVIES J T.Turbulence Phenomena[M].New York:Accademic Press,1972. |
[62] | LIN C,ZHOU M,XU C J.Axisymmetrical two-dimensionalheterogeneous mass transfer model for the absorption of gasinto liquid-liquid dispersions[J].Chemical EngineeringScience.1999,54(3):389-399 |
[63] | RAMCHANDRAN C A,SHARMA M M.Adsorption withfast reaction in a slurry containing sparingly soluble fineparticles[J].Chemical Engineering Science.1969,24:1- |
[64] | YAGI H,HIKITA H.Gas absorption into a slurryaccompanied by chemical reaction with solute from sparinglysoluble particles[J].Chem Ertgrt,1987,36(3):169-174. |
[65] | KARVE S,JUVEKAR V A.Gas absorption into slurriescontaining fine catalyst particles[J].Chemical EngineeringScience.1990,45(3):587-596 |
[66] | HOLSTVOOGD R D,van SWAAIJ W P M,vanDIERENDONCK L.The absorption of gases in aqueousactivated carbon slurries enhanced by adsorbing or catalyticparticles[J].Chemical Engineering Science,1988,43(8):2 181-2 187. |
[67] | VINKE H,HAMERSMA P J,FORTUIN J M H.Enhancement of the gas-adsorption rate in agitated slurryreactors by gas-adsorbing particles adhering to gas bubbles[J].Chemical Engineering Science,1993,48(12):2 197-2 210. |
[68] | BRILMAN D W F,van SWAAIJ W P M,VERSTEEG G F.Heterogeneous mass transfer models for gas absorption inmultiphase systems[J].Chemical Engineering Science,2000,55(15):2 793-2 812. |
[69] | DECKWER W D,BURCKHART R,ZOLL G.Mixing andmass transfer in tall bubble columns[J].ChemicalEngineering Science,1974,29:2 177-2 188. |
[70] | �ֳ�,����,����,��.��ɢ�ڶ�Һ�����ǿ��Һ���ʵ�Ӱ��[J].��ѧ����,2000,28(2):23-33. |