Hydrogen production via carbonaceous catalytic methane decomposition is a complex process with simultaneous reaction, catalyst deactivation, and carbon agglomeration. Conventional reaction and deactivation models do not predict the progress of reaction accurately. Thus, statistical modeling using the method of design of experiments (DoEs) was used to design, model, and analyze experiments of methane decomposition to determine the important factors that affect the rates of reaction and deactivation. A variety of statistical models were tested in order to identify the best one agreeing with the experimental data by analysis of variance (ANOVA). Statistical regression models for initial reaction rate, catalyst activity, deactivation rate, and carbon weight gain were developed. The results showed that a quadratic model predicted the experimental findings. The main factors affecting the dynamics of the methane decomposition reaction and the catalyst deactivation rates for this process are partial pressure of methane, reaction temperature, catalytic activity, and residence time.
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July 2018
Research-Article
Statistical Modeling of Hydrogen Production Via Carbonaceous Catalytic Methane Decomposition Available to Purchase
Vidyasagar Shilapuram,
Vidyasagar Shilapuram
Department of Chemical Engineering,
National Institute of Technology,
Warangal 506004, Telangana, India
National Institute of Technology,
Warangal 506004, Telangana, India
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Bishwadeep Bagchi,
Bishwadeep Bagchi
Department of Chemical Engineering,
National Institute of Technology,
Warangal 506004, Telangana, India
National Institute of Technology,
Warangal 506004, Telangana, India
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Nesrin Ozalp,
Nesrin Ozalp
Fellow ASME
Department of Mechanical
and Industrial Engineering,
University of Minnesota,
Duluth, MN 55812
e-mail: nozalp@d.umn.edu
Department of Mechanical
and Industrial Engineering,
University of Minnesota,
Duluth, MN 55812
e-mail: nozalp@d.umn.edu
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Richard Davis
Richard Davis
Department of Chemical Engineering,
University of Minnesota,
Duluth, MN 55812
University of Minnesota,
Duluth, MN 55812
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Vidyasagar Shilapuram
Department of Chemical Engineering,
National Institute of Technology,
Warangal 506004, Telangana, India
National Institute of Technology,
Warangal 506004, Telangana, India
Bishwadeep Bagchi
Department of Chemical Engineering,
National Institute of Technology,
Warangal 506004, Telangana, India
National Institute of Technology,
Warangal 506004, Telangana, India
Nesrin Ozalp
Fellow ASME
Department of Mechanical
and Industrial Engineering,
University of Minnesota,
Duluth, MN 55812
e-mail: nozalp@d.umn.edu
Department of Mechanical
and Industrial Engineering,
University of Minnesota,
Duluth, MN 55812
e-mail: nozalp@d.umn.edu
Richard Davis
Department of Chemical Engineering,
University of Minnesota,
Duluth, MN 55812
University of Minnesota,
Duluth, MN 55812
1Corresponding author.
Contributed by the Advanced Energy Systems Division of ASME for publication in the JOURNAL OF ENERGY RESOURCES TECHNOLOGY. Manuscript received September 29, 2017; final manuscript received January 21, 2018; published online March 20, 2018. Editor: Hameed Metghalchi.
J. Energy Resour. Technol. Jul 2018, 140(7): 072006 (8 pages)
Published Online: March 20, 2018
Article history
Received:
September 29, 2017
Revised:
January 21, 2018
Citation
Shilapuram, V., Bagchi, B., Ozalp, N., and Davis, R. (March 20, 2018). "Statistical Modeling of Hydrogen Production Via Carbonaceous Catalytic Methane Decomposition." ASME. J. Energy Resour. Technol. July 2018; 140(7): 072006. https://doi.org/10.1115/1.4039323
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