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contributor authorKyoungdoug Min
contributor authorFabian Mueller
contributor authorJohn Auckland
contributor authorSanggyu Kang
contributor authorJacob Brouwer
date accessioned2017-05-09T00:33:22Z
date available2017-05-09T00:33:22Z
date copyrightNovember, 2009
date issued2009
identifier issn2381-6872
identifier otherJFCSAU-28939#041015_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/140821
description abstractA dynamic model of a stationary proton exchange membrane (PEM) fuel cell system has been developed in MATLAB-SIMULINK ®. The system model accounts for the fuel processing system, PEM stack with coolant, humidifier with anode tail-gas oxidizer, and an enthalpy wheel for cathode air. Four reactors are modeled for the fuel processing system: (1) an autothermal reformation (ATR) reactor, (2) a high temperature shift (HTS) reactor, (3) a low temperature shift (LTS) reactor, and (4) a preferential oxidation reactor. Chemical kinetics for ATR that describe steam reformation of methane and partial oxidation of methane were simultaneously solved to accurately predict the reaction dynamics. The chemical equilibrium of CO with H2O was assumed at HTS and LTS reactor exits to calculate CO conversion corresponding to the temperature of each reactor. A quasi-one-dimensional PEM unit cell was modeled with five control volumes for solving the dynamic species and mass conservation equations and seven control volumes to solve the dynamic energy balance. The quasi-one-dimensional cell model is able to capture the details of membrane electrode assembly behavior, such as water transport, which is critical to accurately determine polarization losses. The dynamic conservation equations, primary heat transfer equations and equations of state are solved in each bulk component, and each component is linked together to represent the complete system. The model predictions well matched the observed experimental dynamic voltage, stack coolant outlet temperature, and catalytic partial oxidation (CPO) temperature responses to perturbations. The dynamic response characteristics of the current system are representative of a typical stationary PEM fuel cell system. The dynamic model is used to develop and test a proportional-integral (PI) fuel flow controller that determines the fuel flow rate to maintain the uniform system efficiency. The dynamic model is shown to be a useful tool for investigating the effects of inlet conditions, load, and fuel flow perturbations and for the development of control strategies for enhancing system performance.
publisherThe American Society of Mechanical Engineers (ASME)
titleDynamic Simulation of a Stationary Proton Exchange Membrane Fuel Cell System
typeJournal Paper
journal volume6
journal issue4
journal titleJournal of Fuel Cell Science and Technology
identifier doi10.1115/1.3008029
journal fristpage41015
identifier eissn2381-6910
keywordsFuels
keywordsSimulation
keywordsPolarization (Electricity)
keywordsCoolants
keywordsHumidifiers
keywordsFuel cells
keywordsEnthalpy
keywordsEquations
keywordsFuel processing
keywordsFlow (Dynamics)
keywordsTemperature
keywordsProton exchange membrane fuel cells
keywordsWater
keywordsWheels
keywordsSystem efficiency
keywordsElectric potential
keywordsHydrogen
keywordsAnodes
keywordsGas diffusion layers
keywordsDynamic models
keywordsMembranes
keywordsProton exchange membranes
keywordsHeat transfer
keywordsControl equipment
keywordsSteady state
keywordsoxidation AND Chemical kinetics
treeJournal of Fuel Cell Science and Technology:;2009:;volume( 006 ):;issue: 004
contenttypeFulltext


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