American Journal of Chemical Engineering
Volume 5, Issue 1, January 2017, Pages: 1-5
Received: Sep. 22, 2016;
Accepted: Jan. 7, 2017;
Published: Feb. 3, 2017
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Mehdi Zarifian Jenadelh, Dpartment of Chemical Engineering, Sirjan Branch, Islamic Azad University, Sirjan, Iran
Farshad Farahbod, Department of Chemical Engineering, Firoozabad Branch, Islamic Azad University, Firoozabad, Iran
The use of multistage, fluidized beds of continuous recycles reveals economically and technically attractive for both adsorption of stack gas SO2 and sequential conversion to elemental sulfur. This paper studies the adsorption process behavior of SO2 removal in one bed reactor which is filled with zinc oxide nano catalysts. The performance of catalytic bed is analyzed experimentally and theoretically by measuring the rate of mass transfer, NA, in this work. Sulfur elimination from gas is the major purpose of the handled experiments. The specific surface area (15, 20 and 25 m2/m3) as a effective parameter on mass transfer area and the particle diameter (40, 60 and 80 nm) as feed driving force on the amount of NA are evaluated.
Mehdi Zarifian Jenadelh,
Empirical Study of Treatment of Sour Gas by New Technology, American Journal of Chemical Engineering.
Vol. 5, No. 1,
2017, pp. 1-5.
Copyright © 2017 Authors retain the copyright of this article.
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