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Information Journal Paper

Title

MODELLING AND SCALLING UP FOR SINGLE – CELL PROTEIN PRODUCTION IN CONTINUOUS BIOREACTOR

Pages

  72-78

Abstract

 Interest in searching for new sources of food has increased exponentially during the last 40 years. In this study, MODELING of continuous stirred tank bioreactor is carried out from experimental results and then a bioreactor in pilot scale is designed for production of 40 kg S.C.P. per day. For MODELING of bioreactor in constant temperature and pressure, balance equation of cell mass, methanol, oxygen and carbon dioxide are developed. After dissolving of equations by fourth order runge, the influence of both kinetic and transport parameters on dissolved oxygen, biomass and methanol concentration were studied. From comparing of experimental and theoric results optimum parameters were obtained. For designing bioreactor in pilot scale from optimum parameters, size of bioreactor and other equipments were obtained. Then other parameters from different bases for scaling up were obtained.

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    APA: Copy

    MIRNEZAMI, S.Z.. (2002). MODELLING AND SCALLING UP FOR SINGLE – CELL PROTEIN PRODUCTION IN CONTINUOUS BIOREACTOR. PAJOUHESH-VA-SAZANDEGI, 14(4 (53 IN ANIMAL & FISHRIES SCIENCES)), 72-78. SID. https://sid.ir/paper/18747/en

    Vancouver: Copy

    MIRNEZAMI S.Z.. MODELLING AND SCALLING UP FOR SINGLE – CELL PROTEIN PRODUCTION IN CONTINUOUS BIOREACTOR. PAJOUHESH-VA-SAZANDEGI[Internet]. 2002;14(4 (53 IN ANIMAL & FISHRIES SCIENCES)):72-78. Available from: https://sid.ir/paper/18747/en

    IEEE: Copy

    S.Z. MIRNEZAMI, “MODELLING AND SCALLING UP FOR SINGLE – CELL PROTEIN PRODUCTION IN CONTINUOUS BIOREACTOR,” PAJOUHESH-VA-SAZANDEGI, vol. 14, no. 4 (53 IN ANIMAL & FISHRIES SCIENCES), pp. 72–78, 2002, [Online]. Available: https://sid.ir/paper/18747/en

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