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Numerical study of effect of operating and design parameters for design of steam reforming reactor

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  • Hong, Sung Kook
  • Dong, Sang Keun
  • Han, Jeong Ok
  • Lee, Joong Seong
  • Lee, Young Chul

Abstract

A numerical study on the design of a steam reforming reactor consisting of several reforming tubes and one burner is conducted with respect to various operating and design parameters such as GHSV (gas hourly space velocity), input heat capacity, catalyst layer length, and number of tubes. The calculation of the reforming reaction rate is coupled with a three-dimensional heat and mass transfer calculation. It is shown that a large temperature gradient exists in the reforming reactor, resulting in significant variation of the gas temperature and reaction rate along the reforming tube. The reduction of the catalyst layer length induces a decrease in H2 (hydrogen) concentration as well as pressure loss. An increased number of tubes leads to better system efficiency owing to the enhanced heat transfer to the reforming tube. Consequently, to improve the system efficiency and reduce the pressure loss, an increase in heat transfer area and decrease in catalyst layer length should be essential design considerations.

Suggested Citation

  • Hong, Sung Kook & Dong, Sang Keun & Han, Jeong Ok & Lee, Joong Seong & Lee, Young Chul, 2013. "Numerical study of effect of operating and design parameters for design of steam reforming reactor," Energy, Elsevier, vol. 61(C), pages 410-418.
    • Handle: RePEc:eee:energy:v:61:y:2013:i:c:p:410-418
    DOI: 10.1016/j.energy.2013.08.035
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    3. Popov, S.K. & Svistunov, I.N. & Garyaev, A.B. & Serikov, E.A. & Temyrkanova, E.K., 2017. "The use of thermochemical recuperation in an industrial plant," Energy, Elsevier, vol. 127(C), pages 44-51.
    4. Wangsong Wu & Jiajin Liu & Shuya Guo & Zhukai Zeng & Guangyao Cui & Zhongqing Yang, 2022. "Optimization Research on Burner Arrangement of Landfill Leachate Concentrate Incinerator Based on “3T+E” Principle," Energies, MDPI, vol. 15(16), pages 1-13, August.
    5. Lesmana, Donny & Wu, Ho-Shing, 2014. "Modified oxalic acid co-precipitation method for preparing Cu/ZnO/Al2O3/Cr2O3/CeO2 catalysts for the OR (oxidative reforming) of M (methanol) to produce H2 (hydrogen) gas," Energy, Elsevier, vol. 69(C), pages 769-777.
    6. Wu, Wei & Yang, Hsiao-Tung & Hwang, Jenn-Jiang, 2014. "Conceptual design of syngas production systems with almost net-zero carbon dioxide emissions," Energy, Elsevier, vol. 74(C), pages 753-761.
    7. Ouyang, Kwan & Wu, Horng-Wen & Huang, Shun-Chieh & Wu, Sheng-Ju, 2017. "Optimum parameter design for performance of methanol steam reformer combining Taguchi method with artificial neural network and genetic algorithm," Energy, Elsevier, vol. 138(C), pages 446-458.
    8. Inbamrung, Piyanut & Sornchamni, Thana & Prapainainar, Chaiwat & Tungkamani, Sabaithip & Narataruksa, Phavanee & Jovanovic, Goran N., 2018. "Modeling of a square channel monolith reactor for methane steam reforming," Energy, Elsevier, vol. 152(C), pages 383-400.

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