Empirical Study of Treatment of Sour Gas by New Technology

Mehdi Zarifian Jenadelh; Farshad Farahbod

doi:doi:10.11648/j.ajche.20170501.11

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Empirical Study of Treatment of Sour Gas by New Technology

Mehdi Zarifian Jenadelh, Farshad Farahbod

Published in American Journal of Chemical Engineering (Volume 5, Issue 1)

Received: 22 September 2016 Accepted: 7 January 2017 Published: 3 February 2017

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Abstract

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.

Published in	American Journal of Chemical Engineering (Volume 5, Issue 1)
DOI	10.11648/j.ajche.20170501.11
Page(s)	1-5
Creative Commons	This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.
Copyright	Copyright © The Author(s), 2017. Published by Science Publishing Group

Keywords

SO₂ Removal, Experimental and Theoretical Study, Catalytic Bed, Sulfur

References

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[7]	W. Zhou, C. S. Zhao, L. B. Duan, XP. Chen, C. Liang, Two-dimensional computational fluid dynamics simulation of nitrogen and sulfur oxides emissions in a circulating fluidized bed combustor. Chem. Eng. J., 2011; 173: 564-573.
[8]	D. Eow, S. John, Recovery of sulfur from sour acid gas: A review of the technology Environmental Progress. Americ. Institut. Chem. Eng., 2002; 21: 143-162.
[9]	D. Kunii, O. Levenspiel, Fluidization engineering. First edition. New York: Wiley; 1991.
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Mehdi Zarifian Jenadelh, Farshad Farahbod. (2017). Empirical Study of Treatment of Sour Gas by New Technology. American Journal of Chemical Engineering, 5(1), 1-5. https://doi.org/10.11648/j.ajche.20170501.11

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ACS Style

Mehdi Zarifian Jenadelh; Farshad Farahbod. Empirical Study of Treatment of Sour Gas by New Technology. Am. J. Chem. Eng. 2017, 5(1), 1-5. doi: 10.11648/j.ajche.20170501.11

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AMA Style

Mehdi Zarifian Jenadelh, Farshad Farahbod. Empirical Study of Treatment of Sour Gas by New Technology. Am J Chem Eng. 2017;5(1):1-5. doi: 10.11648/j.ajche.20170501.11

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@article{10.11648/j.ajche.20170501.11,
  author = {Mehdi Zarifian Jenadelh and Farshad Farahbod},
  title = {Empirical Study of Treatment of Sour Gas by New Technology},
  journal = {American Journal of Chemical Engineering},
  volume = {5},
  number = {1},
  pages = {1-5},
  doi = {10.11648/j.ajche.20170501.11},
  url = {https://doi.org/10.11648/j.ajche.20170501.11},
  eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajche.20170501.11},
  abstract = {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.},
 year = {2017}
}

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TY  - JOUR
T1  - Empirical Study of Treatment of Sour Gas by New Technology
AU  - Mehdi Zarifian Jenadelh
AU  - Farshad Farahbod
Y1  - 2017/02/03
PY  - 2017
N1  - https://doi.org/10.11648/j.ajche.20170501.11
DO  - 10.11648/j.ajche.20170501.11
T2  - American Journal of Chemical Engineering
JF  - American Journal of Chemical Engineering
JO  - American Journal of Chemical Engineering
SP  - 1
EP  - 5
PB  - Science Publishing Group
SN  - 2330-8613
UR  - https://doi.org/10.11648/j.ajche.20170501.11
AB  - 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.
VL  - 5
IS  - 1
ER  -

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Author Information

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

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APA Style

Mehdi Zarifian Jenadelh, Farshad Farahbod. (2017). Empirical Study of Treatment of Sour Gas by New Technology. American Journal of Chemical Engineering, 5(1), 1-5. https://doi.org/10.11648/j.ajche.20170501.11

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ACS Style

Mehdi Zarifian Jenadelh; Farshad Farahbod. Empirical Study of Treatment of Sour Gas by New Technology. Am. J. Chem. Eng. 2017, 5(1), 1-5. doi: 10.11648/j.ajche.20170501.11

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AMA Style

Mehdi Zarifian Jenadelh, Farshad Farahbod. Empirical Study of Treatment of Sour Gas by New Technology. Am J Chem Eng. 2017;5(1):1-5. doi: 10.11648/j.ajche.20170501.11

Copy | Download

@article{10.11648/j.ajche.20170501.11,
  author = {Mehdi Zarifian Jenadelh and Farshad Farahbod},
  title = {Empirical Study of Treatment of Sour Gas by New Technology},
  journal = {American Journal of Chemical Engineering},
  volume = {5},
  number = {1},
  pages = {1-5},
  doi = {10.11648/j.ajche.20170501.11},
  url = {https://doi.org/10.11648/j.ajche.20170501.11},
  eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajche.20170501.11},
  abstract = {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.},
 year = {2017}
}

Copy | Download

TY  - JOUR
T1  - Empirical Study of Treatment of Sour Gas by New Technology
AU  - Mehdi Zarifian Jenadelh
AU  - Farshad Farahbod
Y1  - 2017/02/03
PY  - 2017
N1  - https://doi.org/10.11648/j.ajche.20170501.11
DO  - 10.11648/j.ajche.20170501.11
T2  - American Journal of Chemical Engineering
JF  - American Journal of Chemical Engineering
JO  - American Journal of Chemical Engineering
SP  - 1
EP  - 5
PB  - Science Publishing Group
SN  - 2330-8613
UR  - https://doi.org/10.11648/j.ajche.20170501.11
AB  - 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.
VL  - 5
IS  - 1
ER  -

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