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Information Journal Paper

Title

BED VOIDAGE AND HEAT TRANSFER IN NON-NEWTONIAN LIQUID-SOLID FLUIDIZED BED

Pages

  73-79

Abstract

 The presence of particles in liquid-solid FLUIDIZED BEDs enhances the bed HEAT TRANSFER, because he movement of the particles leads to an increased turbulence in the system. Moreover, the violent movement of the particles has a positive effect on fouling of the HEAT TRANSFER surface. The aim of this investigation was to perform systematic measurements of BED VOIDAGE and HEAT TRANSFER coefficient for solid-liquid fluidization in a cylindrical tube and to study the effect of process parameters such as particle size and density, flow velocity, and liquid viscosity on these subjects. A large number of experiments were performed using different cylindrical and spherical particles fluidized in aqueous CMC solution with different concentrations. Using the experimental results, a new correlation for predicting HEAT TRANSFER coefficient in NON-NEWTONIAN liquid-solid FLUIDIZED BED heat exchanger was introduced. 

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    Cite

    APA: Copy

    EHSANI, A.H., BEHBAHANI, B.A., & JAMI ALAHMADI, M.. (2004). BED VOIDAGE AND HEAT TRANSFER IN NON-NEWTONIAN LIQUID-SOLID FLUIDIZED BED . IRANIAN JOURNAL OF CHEMISTRY AND CHEMICAL ENGINEERING (IJCCE), 23(2), 73-79. SID. https://sid.ir/paper/530494/en

    Vancouver: Copy

    EHSANI A.H., BEHBAHANI B.A., JAMI ALAHMADI M.. BED VOIDAGE AND HEAT TRANSFER IN NON-NEWTONIAN LIQUID-SOLID FLUIDIZED BED . IRANIAN JOURNAL OF CHEMISTRY AND CHEMICAL ENGINEERING (IJCCE)[Internet]. 2004;23(2):73-79. Available from: https://sid.ir/paper/530494/en

    IEEE: Copy

    A.H. EHSANI, B.A. BEHBAHANI, and M. JAMI ALAHMADI, “BED VOIDAGE AND HEAT TRANSFER IN NON-NEWTONIAN LIQUID-SOLID FLUIDIZED BED ,” IRANIAN JOURNAL OF CHEMISTRY AND CHEMICAL ENGINEERING (IJCCE), vol. 23, no. 2, pp. 73–79, 2004, [Online]. Available: https://sid.ir/paper/530494/en

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