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Information Seminar Paper

Title

HYDRODYNAMIC AND MASS TRANSFER IN A SPLIT-CYLINDER AIRLIFT BIOREACTOR WITH PACKED BED

Pages

  -

Abstract

 EFFECTS OF PACKED BED IN THE RISER SECTION OF A SPLIT-CYLINDER AIRLIFT BIOREACTOR ON GAS HOLDUP, LIQUID CIRCULATION RATE, MIXING TIME AND THE GAS-LIQUID MASS TRANSFER WITH DIFFERENT GAS FLOW RATES ARE REPORTED FOR AIR–WATER. PACKING ARE ONE/TWO ROWS OF CYLINDRICAL TYPE THAT WERE SETTING HORIZONTALLY WITH A REGULAR DISTANCES. SUPERFICIAL GAS VELOCITIES WAS USED AS OPERATIONAL PARAMETER.IT WAS OBSERVED FROM EXPERIMENTAL RESULTS THAT GAS HOLD UP, OXYGEN TRANSFER AND MIXING TIME INCREASED WITH INCREASING THE NUMBER OF PACKING ROWS BUT PRESENCE OF PACKING IN THE REACTOR DECREASE THE LIQUID CIRCULATION. IN FACT PACKINGS ACT LIKE A BARRIER SO DECREASE LIQUID CIRCULATION, IN ADDTION, ACCUMULATION OF BUBBLES BEHIND THEM LEAD TO INCREASING BUBBLE COALESCENCE RATE AND INCREASING OF BOUYNCY FORCE THUS BUBBLES EXPORT FROM RECTOR WITH NOT IMPORTING TO DOWN COMER RESULT IN DECREASING OF GAS HOLD-UP IN THE DOWN COMER.

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  • Cite

    APA: Copy

    SAJJADI, BAHARAK, & KESHAVARZ MORAVEJI, MOSTAFA. (2010). HYDRODYNAMIC AND MASS TRANSFER IN A SPLIT-CYLINDER AIRLIFT BIOREACTOR WITH PACKED BED. IRANIAN NATIONAL CHEMICAL ENGINEERING CONGRESS & 1ST INTERNATIONAL REGIONAL CHEMICAL AND PETROLEUM E. SID. https://sid.ir/paper/908839/en

    Vancouver: Copy

    SAJJADI BAHARAK, KESHAVARZ MORAVEJI MOSTAFA. HYDRODYNAMIC AND MASS TRANSFER IN A SPLIT-CYLINDER AIRLIFT BIOREACTOR WITH PACKED BED. 2010. Available from: https://sid.ir/paper/908839/en

    IEEE: Copy

    BAHARAK SAJJADI, and MOSTAFA KESHAVARZ MORAVEJI, “HYDRODYNAMIC AND MASS TRANSFER IN A SPLIT-CYLINDER AIRLIFT BIOREACTOR WITH PACKED BED,” presented at the IRANIAN NATIONAL CHEMICAL ENGINEERING CONGRESS & 1ST INTERNATIONAL REGIONAL CHEMICAL AND PETROLEUM E. 2010, [Online]. Available: https://sid.ir/paper/908839/en

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