Performance and cost of automotive fuel cell systems with ultra-low platinum loadings

被引:59
作者
Ahluwalia, R. K. [1 ]
Wang, X.
Kwon, J.
Rousseau, A.
Kalinoski, J. [2 ]
James, B. [2 ]
Marcinkoski, J. [3 ]
机构
[1] Argonne Natl Lab, Nucl Engn Div, Argonne, IL 60439 USA
[2] Directed Technol Inc, Arlington, VA USA
[3] US DOE, Washington, DC USA
关键词
Polymer electrolyte fuel cells; Automotive fuel cell stacks; Electrocatalysts; Air management; Heat rejection; Cost and performance; VEHICLES; ECONOMY; STACKS;
D O I
10.1016/j.jpowsour.2011.01.059
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Anautomotive polymer-electrolyte fuel cell (PEFC) system with ultra-low platinum loading (0.15 mg-Pt cm(-2)) has been analyzed to determine the relationship between its design-point efficiency and the system efficiency at part loads, efficiency over drive cycles, stack and system costs, and heat rejection. The membrane electrode assemblies in the reference PEFC stack use nanostructured, thin-film ternary catalysts supported on organic whiskers and a modified perfluorosulfonic acid membrane. The analyses show that the stack Pt content can be reduced by 50% and the projected high-volume manufacturing cost by >45% for the stack and by 25% for the system, if the design-point system efficiency is lowered from 50% to 40%. The resulting penalties in performance are a <1% reduction in the system peak efficiency; a 2-4% decrease in the system efficiency on the urban, highway, and LA92 drive cycles: and a 6.3% decrease in the fuel economy of the modeled hybrid fuel-cell vehicle on the combined cycle used by EPA for emission and fuel economy certification. The stack heat load, however, increases by 50% at full power (80 kW(e)) but by only 23% at the continuous power (61.5 kW(e)) needed to propel the vehicle on a 6.5% grade at 55 mph. The reduced platinum and system cost advantages of further lowering the design-point efficiency from 40% to 35% are marginal. The analyses indicate that thermal management in the lower efficiency systems is very challenging and that the radiator becomes bulky if the stack temperature cannot be allowed to increase to 90-95 degrees C under driving conditions where heat rejection is difficult. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:4619 / 4630
页数:12
相关论文
共 21 条
[1]   Buildup of nitrogen in direct hydrogen polymer-electrolyte fuel cell stacks [J].
Ahluwalia, R. K. ;
Wang, X. .
JOURNAL OF POWER SOURCES, 2007, 171 (01) :63-71
[2]   Rapid self-start of polymer electrolyte fuel cell stacks from subfreezing temperatures [J].
Ahluwalia, R. K. ;
Wang, X. .
JOURNAL OF POWER SOURCES, 2006, 162 (01) :502-512
[3]   Fuel cell systems for transportation: Status and trends [J].
Ahluwalia, Rajesh K. ;
Wang, Xiaohua. .
JOURNAL OF POWER SOURCES, 2008, 177 (01) :167-176
[4]   Fuel economy of hybrid fuel-cell vehicles [J].
Ahluwalia, RK ;
Wang, X ;
Rousseau, A .
JOURNAL OF POWER SOURCES, 2005, 152 (01) :233-244
[5]   Direct hydrogen fuel cell systems for hybrid vehicles [J].
Ahluwalia, RK ;
Wang, X .
JOURNAL OF POWER SOURCES, 2005, 139 (1-2) :152-164
[6]   Fuel economy of hydrogen fuel cell vehicles [J].
Ahluwalia, RK ;
Wang, X ;
Rousseau, A ;
Kumar, R .
JOURNAL OF POWER SOURCES, 2004, 130 (1-2) :192-201
[7]  
AHLUWALIA RK, 2008, FUEL CELL SYSTEMS AN, P793
[8]  
AHLUWALIA RK, 2010, FUEL CELL SYSTEMS LO
[9]   Oxygen reduction activity of Pt and Pt-Mn-Co electrocatalysts sputtered on nano-structured thin film support [J].
Bonakdarpour, Arman ;
Stevens, Krystal ;
Vernstrom, George D. ;
Atanasoski, Radoslav ;
Schmoeckel, Alison K. ;
Debe, Mark K. ;
Dahn, Jeff R. .
ELECTROCHIMICA ACTA, 2007, 53 (02) :688-694
[10]   Pre-oxidized and nitrided stainless steel alloy foil for proton exchange membrane fuel cell bipolar plates: Part 1. Corrosion, interfacial contact resistance, and surface structure [J].
Brady, M. P. ;
Wang, H. ;
Turner, J. A. ;
Meyer, H. M., III ;
More, K. L. ;
Tortorelli, P. F. ;
McCarthy, B. D. .
JOURNAL OF POWER SOURCES, 2010, 195 (17) :5610-5618