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Information Journal Paper

Title

DYNAMIC SIMULATION OF AN INDUSTRIAL ROTARY DRYER

Pages

  68-77

Abstract

SOLID TRANSPORT phenomena drastically affect rotary drying process. A change in any solid movement variable such as particle hold up or input flow rate results in a significant variation of heat and mass transfer rates. Therefore, in this research dynamic study of these phenomena was conducted both experimentally and theoretically. Several experiments were performed employing an industrial granule dryer. The dryer length and diameter were 5 and 1 m, respectively. In each experiment one of the solid movement variables was changed and the resulting dynamic change on the process was measured. The data was used to estimate the parameters of a dynamic distributed parameter model of the system using dynamic optimization method. The data were also employed to evaluate the model. The model predictions for solid hold up and outlet flow rate were compared with those of the experimental data. The average model error for solid hold up and outlet flow rate were 5.6% and 5.4 %, respectively.

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  • Cite

    APA: Copy

    SHAHHOSSEINI, SH., SADEGHI, M.T., & GOLSEFATAN, H.R.. (2010). DYNAMIC SIMULATION OF AN INDUSTRIAL ROTARY DRYER. IRANIAN JOURNAL OF CHEMICAL ENGINEERING, 7(2), 68-77. SID. https://sid.ir/paper/298306/en

    Vancouver: Copy

    SHAHHOSSEINI SH., SADEGHI M.T., GOLSEFATAN H.R.. DYNAMIC SIMULATION OF AN INDUSTRIAL ROTARY DRYER. IRANIAN JOURNAL OF CHEMICAL ENGINEERING[Internet]. 2010;7(2):68-77. Available from: https://sid.ir/paper/298306/en

    IEEE: Copy

    SH. SHAHHOSSEINI, M.T. SADEGHI, and H.R. GOLSEFATAN, “DYNAMIC SIMULATION OF AN INDUSTRIAL ROTARY DRYER,” IRANIAN JOURNAL OF CHEMICAL ENGINEERING, vol. 7, no. 2, pp. 68–77, 2010, [Online]. Available: https://sid.ir/paper/298306/en

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