Exergetic and Economic Improvement for a Steam Methane-Reforming Industrial Plant: Simulation Tool

Steam methane reforming (SMR) for hydrogen production was studied by simulating the reformer and pre-reformer sections. This simulation was validated by using available data taken from a real industrial plant, which enabled precise correlations with the real industrial process to be found. Moreover,...

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Main Authors: Francisco Jose Durán, Fernando Dorado, Luz Sanchez-Silva
Format: Article
Language:English
Published: MDPI AG 2020-07-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/13/15/3807
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spelling doaj-74de16186ddc46ff905f86029e38d8bf2020-11-25T03:51:39ZengMDPI AGEnergies1996-10732020-07-01133807380710.3390/en13153807Exergetic and Economic Improvement for a Steam Methane-Reforming Industrial Plant: Simulation ToolFrancisco Jose Durán0Fernando Dorado1Luz Sanchez-Silva2Department of Chemical Engineering, University of Castilla—La Mancha, Avda. Camilo José Cela 12, 13071 Ciudad Real, SpainDepartment of Chemical Engineering, University of Castilla—La Mancha, Avda. Camilo José Cela 12, 13071 Ciudad Real, SpainDepartment of Chemical Engineering, University of Castilla—La Mancha, Avda. Camilo José Cela 12, 13071 Ciudad Real, SpainSteam methane reforming (SMR) for hydrogen production was studied by simulating the reformer and pre-reformer sections. This simulation was validated by using available data taken from a real industrial plant, which enabled precise correlations with the real industrial process to be found. Moreover, the influence of the molar ratio between the raw materials (steam-to-carbon molar ratio, S/C) and the reformer outlet temperature (<i>T<sub>cc</sub></i>) was studied. The energy requirements for the reforming reaction increased with the S/C ratio. The energy needed for developing the reforming reaction also increased with <i>T<sub>cc</sub></i>, but the hydrogen yield when operating with a high S/C ratio and <i>T<sub>cc</sub></i> increased. In addition, an exergetic analysis was carried out to identify exergy losses in the SMR process, and most were destroyed in the chemical reactors. Increasing the combustion air flow was proposed for finding an optimum value for exergetic efficiency in the process, thereby reducing fuel consumption. Finally, there was a study into the economic viability of this investment, with a reduction of 22% in utility costs with the optimum exergetic value.https://www.mdpi.com/1996-1073/13/15/3807steam methane reformingsimulation softwarehydrogen yieldindustrial plantexergetic analysiseconomic study
collection DOAJ
language English
format Article
sources DOAJ
author Francisco Jose Durán
Fernando Dorado
Luz Sanchez-Silva
spellingShingle Francisco Jose Durán
Fernando Dorado
Luz Sanchez-Silva
Exergetic and Economic Improvement for a Steam Methane-Reforming Industrial Plant: Simulation Tool
Energies
steam methane reforming
simulation software
hydrogen yield
industrial plant
exergetic analysis
economic study
author_facet Francisco Jose Durán
Fernando Dorado
Luz Sanchez-Silva
author_sort Francisco Jose Durán
title Exergetic and Economic Improvement for a Steam Methane-Reforming Industrial Plant: Simulation Tool
title_short Exergetic and Economic Improvement for a Steam Methane-Reforming Industrial Plant: Simulation Tool
title_full Exergetic and Economic Improvement for a Steam Methane-Reforming Industrial Plant: Simulation Tool
title_fullStr Exergetic and Economic Improvement for a Steam Methane-Reforming Industrial Plant: Simulation Tool
title_full_unstemmed Exergetic and Economic Improvement for a Steam Methane-Reforming Industrial Plant: Simulation Tool
title_sort exergetic and economic improvement for a steam methane-reforming industrial plant: simulation tool
publisher MDPI AG
series Energies
issn 1996-1073
publishDate 2020-07-01
description Steam methane reforming (SMR) for hydrogen production was studied by simulating the reformer and pre-reformer sections. This simulation was validated by using available data taken from a real industrial plant, which enabled precise correlations with the real industrial process to be found. Moreover, the influence of the molar ratio between the raw materials (steam-to-carbon molar ratio, S/C) and the reformer outlet temperature (<i>T<sub>cc</sub></i>) was studied. The energy requirements for the reforming reaction increased with the S/C ratio. The energy needed for developing the reforming reaction also increased with <i>T<sub>cc</sub></i>, but the hydrogen yield when operating with a high S/C ratio and <i>T<sub>cc</sub></i> increased. In addition, an exergetic analysis was carried out to identify exergy losses in the SMR process, and most were destroyed in the chemical reactors. Increasing the combustion air flow was proposed for finding an optimum value for exergetic efficiency in the process, thereby reducing fuel consumption. Finally, there was a study into the economic viability of this investment, with a reduction of 22% in utility costs with the optimum exergetic value.
topic steam methane reforming
simulation software
hydrogen yield
industrial plant
exergetic analysis
economic study
url https://www.mdpi.com/1996-1073/13/15/3807
work_keys_str_mv AT franciscojoseduran exergeticandeconomicimprovementforasteammethanereformingindustrialplantsimulationtool
AT fernandodorado exergeticandeconomicimprovementforasteammethanereformingindustrialplantsimulationtool
AT luzsanchezsilva exergeticandeconomicimprovementforasteammethanereformingindustrialplantsimulationtool
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