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Small-scale production of hydrogen via auto-thermal reforming in an adiabatic packed bed reactor: Parametric study and reactor's optimization through response surface methodology

Small-scale production of hydrogen via auto-thermal reforming in an adiabatic packed bed reactor: Parametric study and reactor's optimization through response surface methodology
Small-scale production of hydrogen via auto-thermal reforming in an adiabatic packed bed reactor: Parametric study and reactor's optimization through response surface methodology
In this work, a two-dimensional (2-D) heterogeneous reactor model for ATR process is presented. In order to authenticate the developed reactor model outputs, literature results as well as thermodynamic findings produced by employing chemical equilibrium with applications (CEA) software were compared with the model predictions and an excellent agreement was evidenced that corroborates the model's accurate predictive capability. Response surface methodology combined with central composite design was used to investigate the significance of operational parameters on the performance of the ATR process and Parametric optimization was performed to find the optimal operating conditions. Further insights into the ATR process were obtained by studying the effect of temperature, pressure, S/C, oxygen to carbon ratio (O/C) and gas mass flow velocity (Gs) on CH4 conversion, H2 yield (wt. % of CH4) and H2 purity. It was concluded that 973 K, 1.5 bar, S/C of 3.0, O/C of 0.45 and Gs of 0.15 kg/m2s resulted in CH4 conversion and H2 purity up to 97.6% and 71.8%, respectively.
0098-1354
Tariq, Ramesha
796c6eeb-4bf0-4caf-830a-ee0bf2777eaf
Maqbool, Fahad
608013cc-6fab-45dd-b848-9f42e796bf10
Abbas, Syed Zaheer
3b02900e-fef6-40e1-acf7-96f26bfde4a8
Tariq, Ramesha
796c6eeb-4bf0-4caf-830a-ee0bf2777eaf
Maqbool, Fahad
608013cc-6fab-45dd-b848-9f42e796bf10
Abbas, Syed Zaheer
3b02900e-fef6-40e1-acf7-96f26bfde4a8

Tariq, Ramesha, Maqbool, Fahad and Abbas, Syed Zaheer (2021) Small-scale production of hydrogen via auto-thermal reforming in an adiabatic packed bed reactor: Parametric study and reactor's optimization through response surface methodology. Computers and Chemical Engineering, 145, [107192]. (doi:10.1016/j.compchemeng.2020.107192).

Record type: Article

Abstract

In this work, a two-dimensional (2-D) heterogeneous reactor model for ATR process is presented. In order to authenticate the developed reactor model outputs, literature results as well as thermodynamic findings produced by employing chemical equilibrium with applications (CEA) software were compared with the model predictions and an excellent agreement was evidenced that corroborates the model's accurate predictive capability. Response surface methodology combined with central composite design was used to investigate the significance of operational parameters on the performance of the ATR process and Parametric optimization was performed to find the optimal operating conditions. Further insights into the ATR process were obtained by studying the effect of temperature, pressure, S/C, oxygen to carbon ratio (O/C) and gas mass flow velocity (Gs) on CH4 conversion, H2 yield (wt. % of CH4) and H2 purity. It was concluded that 973 K, 1.5 bar, S/C of 3.0, O/C of 0.45 and Gs of 0.15 kg/m2s resulted in CH4 conversion and H2 purity up to 97.6% and 71.8%, respectively.

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More information

Accepted/In Press date: 6 December 2020
e-pub ahead of print date: 8 December 2020
Published date: 6 January 2021

Identifiers

Local EPrints ID: 474526
URI: http://eprints.soton.ac.uk/id/eprint/474526
ISSN: 0098-1354
PURE UUID: 618527d9-1d7c-440e-8a92-a85c849f63cb
ORCID for Syed Zaheer Abbas: ORCID iD orcid.org/0000-0002-8783-8572

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Date deposited: 23 Feb 2023 17:55
Last modified: 17 Mar 2024 04:18

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Contributors

Author: Ramesha Tariq
Author: Fahad Maqbool
Author: Syed Zaheer Abbas ORCID iD

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