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Hydrogen production by onboard gasoline processing – Process simulation and optimization

Abstract

Highlights: • Process flow sheet for an onboard fuel processor for 100 kW fuel cell output was simulated. • Gasoline fuel requirement was found to be 30.55 kg/hr. • The fuel processor efficiency was found to be 95.98%. • An heat integrated optimum flow sheet was developed. - Abstract: Fuel cell vehicles have reached the commercialization stage and hybrid vehicles are already on the road. While hydrogen storage and infrastructure remain critical issues in stand alone commercialization of the technology, researchers are developing onboard fuel processors, which can convert a variety of fuels into hydrogen to power these fuel cell vehicles. The feasibility study of a 100 kW on board fuel processor based on gasoline fuel is carried out using process simulation. The steady state model has been developed with the help of Aspen HYSYS to analyze the fuel processor and total system performance. The components of the fuel processor are the fuel reforming unit, CO clean-up unit and auxiliary units. Optimization studies were carried out by analyzing the influence of various operating parameters such as oxygen to carbon ratio, steam to carbon ratio, temperature and pressure on the process equipments. From the steady state model optimization using Aspen HYSYS,  More>>
Publication Date:
Dec 15, 2013
Product Type:
Journal Article
Resource Relation:
Journal Name: Energy Conversion and Management; Journal Volume: 76; Other Information: Copyright (c) 2013 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.; Country of input: International Atomic Energy Agency (IAEA)
Subject:
42 ENGINEERING; 29 ENERGY PLANNING, POLICY AND ECONOMY; CARBON; CARBON MONOXIDE; COMMERCIALIZATION; CONCENTRATION RATIO; EFFICIENCY; FEASIBILITY STUDIES; FLOWSHEETS; FUEL CELLS; GASOLINE; HEAT EXCHANGERS; HYBRID ELECTRIC-POWERED VEHICLES; HYDROGEN PRODUCTION; HYDROGEN STORAGE; OPTIMIZATION; OXYGEN; SIMULATION; STEADY-STATE CONDITIONS; STEAM
OSTI ID:
22298468
Country of Origin:
United Kingdom
Language:
English
Other Identifying Numbers:
Journal ID: ISSN 0196-8904; CODEN: ECMADL; Other: PII: S0196-8904(13)00460-3; TRN: GB14R5015004640
Availability:
Available from http://dx.doi.org/10.1016/j.enconman.2013.08.006
Submitting Site:
INIS
Size:
page(s) 746-752
Announcement Date:
Jan 27, 2015

Citation Formats

Bisaria, Vega, and Smith, R.J. Byron,. Hydrogen production by onboard gasoline processing – Process simulation and optimization. United Kingdom: N. p., 2013. Web. doi:10.1016/J.ENCONMAN.2013.08.006.
Bisaria, Vega, & Smith, R.J. Byron,. Hydrogen production by onboard gasoline processing – Process simulation and optimization. United Kingdom. https://doi.org/10.1016/J.ENCONMAN.2013.08.006
Bisaria, Vega, and Smith, R.J. Byron,. 2013. "Hydrogen production by onboard gasoline processing – Process simulation and optimization." United Kingdom. https://doi.org/10.1016/J.ENCONMAN.2013.08.006.
@misc{etde_22298468,
title = {Hydrogen production by onboard gasoline processing – Process simulation and optimization}
author = {Bisaria, Vega, and Smith, R.J. Byron,}
abstractNote = {Highlights: • Process flow sheet for an onboard fuel processor for 100 kW fuel cell output was simulated. • Gasoline fuel requirement was found to be 30.55 kg/hr. • The fuel processor efficiency was found to be 95.98%. • An heat integrated optimum flow sheet was developed. - Abstract: Fuel cell vehicles have reached the commercialization stage and hybrid vehicles are already on the road. While hydrogen storage and infrastructure remain critical issues in stand alone commercialization of the technology, researchers are developing onboard fuel processors, which can convert a variety of fuels into hydrogen to power these fuel cell vehicles. The feasibility study of a 100 kW on board fuel processor based on gasoline fuel is carried out using process simulation. The steady state model has been developed with the help of Aspen HYSYS to analyze the fuel processor and total system performance. The components of the fuel processor are the fuel reforming unit, CO clean-up unit and auxiliary units. Optimization studies were carried out by analyzing the influence of various operating parameters such as oxygen to carbon ratio, steam to carbon ratio, temperature and pressure on the process equipments. From the steady state model optimization using Aspen HYSYS, an optimized reaction composition in terms of hydrogen production and carbon monoxide concentration corresponds to: oxygen to carbon ratio of 0.5 and steam to carbon ratio of 0.5. The fuel processor efficiency of 95.98% is obtained under these optimized conditions. The heat integration of the system using the composite curve, grand composite curve and utility composite curve were studied for the system. The most appropriate heat exchanger network from the generated ones was chosen and that was incorporated into the optimized flow sheet of the100 kW fuel processor. A completely heat integrated 100 kW fuel processor flow sheet using gasoline as fuel was thus successfully simulated and optimized.}
doi = {10.1016/J.ENCONMAN.2013.08.006}
journal = []
volume = {76}
journal type = {AC}
place = {United Kingdom}
year = {2013}
month = {Dec}
}