[1] Woragidbumrung, K., Sae-Tang, P., Yao, H., Han, J., Chaivatcharin, S., Zhong, J.J.,
"Impact of conditioned medium on cell cultures of Panax notoginseng in an airlift
bioreactor", Process Biochem., 37, 209-213 (2001).
[2] Huang,T.K., Wang, P.M., Wu, W.T., "Cultivation of Bacillus thuringiensins in airlift
reactor with wire mesh draft tubes", Biochem. Eng. J., 7, 35-39 (2001).
[3] Gavrilescu, M., Tudose, R.Z., "Hydrodynamics of nonNewtonian liquids in external-loop
airlift bioreactors. Part I: Study of the gas holdup", Bioproc. Eng., 18, 17-26(1998).
[4] Galindez-Mayer, J., Sanchez-Teja, O., Cristiani-Urbina, E.,Ruiz-Ordaz, N., "A novel
split-cylinder airlift reactor for fed-batch cultures", Bioproc. Biosys. Eng., 24, 171-177
(2001)
[5] Bello, R.A., Robinson, C.W., Moo-young, M., "Gas holdup and overall volumetric oxygen
transfer coefficient in airlift contactors", Biotechnol. Bioeng., 27, 369-381 (1985).
[6] Sajc, L., Oberadovic, B., Vakovic, D., Bugarki, B., "Hydrodynamics and mass transfer in
a four-phase external-loop airlift bioreactor", Biotechnol. Prog., 11, 420-428 (1995).
[7] Kawase, Y., Hashimoto, N., "Gas hold-up and oxygen transfer in three-phase external-
loop airlift bioreactors:Non-Newtonian fermentation broths", J. Chem. Tech.Biotechnol., 65,
325-334 (1996).
[8] Kawase, Y., Omori, N., Tsujimura, M., "Liquid-phase mixing in external-loop airlift
bioreactors", J. Chem. Tech.Biotechnol., 61, 49-55 (1994).
[9] Fraser, R.D., Itiel, G.A., "Hydrodynamic characteristic of a spinning sparger,
external-loop airlift bioreactor", Can. J.Chem. Eng., 71, 419-425 (1993).
[10] Fraser, R.D., Ritchie, B.J., Hill, G.A., "Dynamic mixing and oxygen transfer in a
small airlift loop bioreactors:Model and experimental verification", Biotechnol. Prog.,10,
543-547 (1994).
[11] Gavrilescu, M., Tudose, R.Z., "Modeling of liquid circulation velocity in concentric
tube airlift reactors", Chem.Eng. J., 69, 85-91 (1998).
[12] Zheng, Y.G., Wang, Z., Chen, X.L., "α-Amylase production by Bacillus subtilis with
dregs in an external-loop airlift bioreactor", Biochem. Eng. J., 5, 115-121 (2000).
[13] Schorr-Galindo, S., Ghomnidh, C., Guiraud, J.P., "Insulin enrichment by fermentation
in a flocculating yeast reactor",Biotechnol. Lett., 17, 1305-1310 (1995).
[14] Chung, I.S., Kang, Y.M., Oh, J.H., "Continuous suspended cell culture of Mentha
piperita in cell-recycled airlift bioreactor", Biotechnol. Tech., 8, 789-792 (1994).
[15] Kessler, W.R., Popovic, M.K., Robinson, C.W., "Xanthan production in an external-loop
airlift fermenter", Can. J.Chem. Eng., 71, 101-106 (1993).
[16] Brandes, L., Cvu, X., Maschke, H.S., "Production of fusion protein SPA ECORI in batch
culture in a 60I airlift tower loop reactor", Biotechnol. Prog., 9, 122-127 (1993).
[17] Al-Qodah, Z., Lsfi, W., "Modeling of antibiotics production in magneto three-phase
airlift fermenter", Biochem. Eng.J., 7, 7-16 (2001).
[18] Xie, D., Liu, D., Liu, T., "Modeling of glycerol production by fermentation in
different reactor states", Process Biochem., 36, 1225-1232 (2001).
[19] Mekchuk, J.C., Siegel, M.H., "Airlift reactors in chemical and biological technology",
J. Chem. Tech. Biotechnol.,41, 105-120 (1988).
[20] Agricultural Antibiotic Group in Shanghai Pesticide Institute, "Identification of
validamycins producing organism",Ac. Microb., 15, 110-114 (1975). (in Chinese)
[21] Iwasa, T., Higashide, E., Yamanoto, H., Shibata, M.,"Studies on validamycins, a new
antibiotic Ⅱ. Production and biological properties of validamycins A and B", J. Antibiot.,
24, 107-113 (1971).
[22] Dong, H., Mahmud, T., Tornus, I., Lee, S., Floss, H.,"Biosynthesis of the
validamycins: Identification of intermediates in the biosynthesis of validamycin A by
Streptomyces hygroscopicus", J. Am. Chem. Soc., 123, 2733-2742 (2001).
[23] Iwasa, T., Yamamoto, H., Shibata, M., "Studies on validamycins new antibiotics I.
Streptomyces hygroscopicus var. Limoneusnov. var., validamycin producing organism",J.
Antibiot., 23, 595-602 (1970).
[24] Kameda, Y., Asano, N., Matsui, K., "Structures of minor components of the validamycin
complex", J. Antibiot., 41,1488-1492 (1988).
[25] Asano, N., Yamaguchi, T., Kameda, Y., Matsui, K., "Effect of validamycins on
glycohydrolases of Rhizoctionia Solani",J. Antibiot., 40, 526-532 (1987).
[26] Chen, T., Zhang, Y., Sun, S., Determination of the Biological Pesticides and Their
Principles, Agriculture Press,Beijing (1993). (in Chinese)
[27] Jia, S., Mu, G., Ren, S., "A rapid method for determination of reducing sugar, glucose
and starch in fruits and vegetables with 3,5-diatrosalycylic acid", Food Ferment. Ind.,
2,30-34 (1983). (in Chinese)
[28] Kamp, F., Wase, D.A.J., McManamey, W.J., Mendoza, O.,Thayamithy, K., "A comparison of
some methods of estimating volumetric mass-transfer coefficients in an externalloop airlift
fermenter", Biotechnol. Bioeng., 30, 179-186(1987).
[29] Stejskal, J., Potucek, F., "Oxygen transfer in liquids",Biotechnol. Bioeng., 27, 503-
508 (1985).
[30] Snape, J.B., Fialova, M., Zahradnik, J., "Hydrodynamic studies in an external-loop
airlift reactor containing aqueous electrolyte and sugar solutions", Chem. Eng. Sci.,
47,3387-3394 (1992).
[31] Snape, J.B., Zahradnik, J., Fialova, M., Thomas, N.H.,"Liquid-phase properties and
sparger design effects in an external-loop airlift reactor", Chem. Eng. Sci., 50, 3175-3186
(1995).
[32] Merchuk, J.C., "Gas holdup and liquid velocity in a twodimensional airlift reactor",
Chem. Eng. Sci., 41, 11-16(1986).
[33] Mekchuk, J.C., Stein, Y., "Local holdup and liquid velocity in airlift reactors",
AIChE J., 27, 377-388 (1981).
[34] McManamecy, W.J., Wase, D.A.J., Rayrnahasay, S.,Thayanithy, K., "The influence of gas
inlet design on gas holdup values for water and various solutions in a loop-type airlift
fermenter", J. Chem. Technol. Biotechnol., 341,151-164 (1984). |
京公网安备 11010102001995号
