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Volumn 36, Issue 3, 2000, Pages 201-207

Comparison of experimental methods for determination of the volumetric mass transfer coefficient in fermentation processes

Author keywords

[No Author keywords available]

Indexed keywords

BIOMASS; BIOREACTORS; FERMENTATION; MATHEMATICAL MODELS; METABOLISM; MICROORGANISMS; OXYGEN;

EID: 0342572576     PISSN: 00429929     EISSN: None     Source Type: Journal    
DOI: 10.1007/s002310050385     Document Type: Article
Times cited : (24)

References (13)
  • 1
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    • Siegel MH; Merchuk JC (1987) Mass transfer in a rectangular airlift reactor: effects of geometry and gas circulation. Biotechnol Bioeng 32: 1128-1137
    • (1987) Biotechnol Bioeng , vol.32 , pp. 1128-1137
    • Siegel, M.H.1    Merchuk, J.C.2
  • 2
    • 0028405849 scopus 로고
    • 2 mass balance technique in a coal desulfuration bioreactor
    • 2 mass balance technique in a coal desulfuration bioreactor. Ind Eng Chem Res 33: 950-956
    • (1994) Ind Eng Chem Res , vol.33 , pp. 950-956
    • Güell, C.1    Giralt, J.2
  • 3
    • 0024278770 scopus 로고
    • Simultaneous measurements of oxygen diffusion coefficients and solubilities in fermentation media with polarographic oxygen electrodes
    • Ju LK; Ho CS (1988) Simultaneous measurements of oxygen diffusion coefficients and solubilities in fermentation media with polarographic oxygen electrodes. Biotechnol Bioeng 31: 995-1005
    • (1988) Biotechnol Bioeng , vol.31 , pp. 995-1005
    • Ju, L.K.1    Ho, C.S.2
  • 5
    • 77957227509 scopus 로고
    • Chemical analysis of microbial cells
    • Norris JR, Ribbons DW (Eds) London, Academic Press
    • Herbert D; Phipps PJ; Strange RE (1971) Chemical analysis of microbial cells. In: Norris JR, Ribbons DW (Eds) Methods in microbiology. London, Academic Press, 5B, pp 209-344
    • (1971) Methods in Microbiology , vol.5 B , pp. 209-344
    • Herbert, D.1    Phipps, P.J.2    Strange, R.E.3
  • 6
    • 0019578923 scopus 로고
    • Differences in the behaviour of bubble columns and airlift loop reactors
    • Weiland P; Onken U (1981) Differences in the behaviour of bubble columns and airlift loop reactors. Ger Chem Eng 4: 174-181
    • (1981) Ger Chem Eng , vol.4 , pp. 174-181
    • Weiland, P.1    Onken, U.2
  • 9
    • 0030304056 scopus 로고    scopus 로고
    • Prediction of gas hold-up and liquid velocity in airlift reactors using two-phase flow friction coefficients
    • García-Calvo E; Letón P (1996) Prediction of gas hold-up and liquid velocity in airlift reactors using two-phase flow friction coefficients. J Chem Tech Biotech 67: 388-396
    • (1996) J Chem Tech Biotech , vol.67 , pp. 388-396
    • García-Calvo, E.1    Letón, P.2
  • 10
    • 0020201449 scopus 로고
    • New bioreactors for aerobic processes
    • Schügerl K (1982) New bioreactors for aerobic processes. Int Chem Eng 22(4): 591-610
    • (1982) Int Chem Eng , vol.22 , Issue.4 , pp. 591-610
    • Schügerl, K.1
  • 11
    • 0024579716 scopus 로고
    • Characteristics of a cocurrent multistage bubble column
    • Chen BH; Yang NS (1989) Characteristics of a cocurrent multistage bubble column. Ind Eng Chem Res 28: 1405-1410
    • (1989) Ind Eng Chem Res , vol.28 , pp. 1405-1410
    • Chen, B.H.1    Yang, N.S.2
  • 12
    • 0000903169 scopus 로고
    • Physical rate processes in industrial fermentation. Part I: The interfacial area in gas-liquid contacting with mechanical agitation
    • Calderbank PH (1958) Physical rate processes in industrial fermentation. Part I: the interfacial area in gas-liquid contacting with mechanical agitation. Trans Instn Chem Engrs 36: 443-463
    • (1958) Trans Instn Chem Engrs , vol.36 , pp. 443-463
    • Calderbank, P.H.1
  • 13
    • 0001995599 scopus 로고
    • Physical rate processes in industrial fermentation. Part II: Mass transfer coefficient in gas-liquid contacting with and without mechanical agitation
    • Calderbank PH (1959) Physical rate processes in industrial fermentation. Part II: mass transfer coefficient in gas-liquid contacting with and without mechanical agitation. Trans Instn Chem Engrs 37: 173-185
    • (1959) Trans Instn Chem Engrs , vol.37 , pp. 173-185
    • Calderbank, P.H.1


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.