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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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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