Chemicals and energy co-generation from direct hydrocarbons/oxygen proton exchange membrane fuel cell

被引:26
作者
Li, WS [1 ]
Lu, DS
Luo, JL
Chuang, KT
机构
[1] S China Normal Univ, Dept Chem, Guangzhou 510631, Peoples R China
[2] Univ Alberta, Dept Chem & Mat Engn, Edmonton, AB T6G 2G6, Canada
基金
中国国家自然科学基金; 加拿大自然科学与工程研究理事会;
关键词
chemicals; energy; co-generation; hydrocarbon; proton exchange membrane; fuel cell;
D O I
10.1016/j.jpowsour.2005.01.077
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
A proton exchange membrane fuel cell for chemicals and energy co-generation was set up with hydrocarbons ethane, propane and butane as fuels, and the electrochemical performance of the cell was studied by using linear potential sweep, alternating current impedance and gas chromatography. The cell performance can be improved to a great extent by increasing the platinum load in the catalyst, by treating the membrane with phosphoric acid and by elevating temperature. The improvement of cell performance by the increase of platinum load is ascribed to the increase of reaction sites for hydrocarbon oxidation, that by phosphoric acid treatment to the increase of proton conductivity in Nafion membrane, and that by elevating temperature to the improvement in thermodynamic as well as kinetic aspects. Only a small fraction of the hydrocarbon is converted to carbon dioxide in this cell during its power generation. The current efficiency is 5% for the conversion of ethane to carbon dioxide in the ethane/oxygen fuel cell with 20% carbon-supported platinum as catalyst and phosphoric acid-treated membrane as proton exchange membrane at 0.2 V, 80 degrees C and ambient pressure. The reaction activity of hydrocarbons at the anode is in the order of propane, butane and ethane. The possible chemicals produced from the cell were hydrocarbons with more than six carbons, which are inactive at the anode under cell conditions. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:376 / 382
页数:7
相关论文
共 24 条
[1]   Status of the development of a direct methanol fuel cell [J].
Baldauf, M ;
Preidel, W .
JOURNAL OF POWER SOURCES, 1999, 84 (02) :161-166
[2]   ANODIC OXIDATION OF SATURATED HYDROCARBONS . A MECHANISTIC STUDY [J].
BOCKRIS, JOM ;
GILEADI, E ;
STONER, GE .
JOURNAL OF PHYSICAL CHEMISTRY, 1969, 73 (02) :427-&
[3]   ADSORPTION AND OXIDATION OF HYDROCARBONS ON NOBLE METAL ELECTRODES .I. PROPANE ADSORPTION ON SMOOTH PLATINUM ELECTRODES [J].
BRUMMER, SB ;
FORD, JI ;
TURNER, MJ .
JOURNAL OF PHYSICAL CHEMISTRY, 1965, 69 (10) :3424-&
[4]  
Giner, 1964, ELECTROCHIM ACTA, V9, P63
[5]  
GLEADI E, 1966, J ELECTROANAL CHEM, V11, P137
[6]   Selective oxidation of propene using an electrochemical membrane reactor with CeO2-based solid electrolyte [J].
Hamakawa, S ;
Hayakawa, T ;
York, APE ;
Tsunoda, T ;
Yoon, YS ;
Suzuki, K ;
Shimizu, M ;
Takehira, K .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1996, 143 (04) :1264-1268
[7]   A review of the state-of-the-art of the methanol crossover in direct methanol fuel cells [J].
Heinzel, A ;
Barragán, VM .
JOURNAL OF POWER SOURCES, 1999, 84 (01) :70-74
[8]   HIGH TEMPERATURE-TYPE PROTON CONDUCTIVE SOLID OXIDE FUEL-CELLS USING VARIOUS FUELS [J].
IWAHARA, H ;
UCHIDA, H ;
TANAKA, S .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1986, 16 (05) :663-668
[9]  
LARMINIE J, 2000, FUEL CELL SYSTEM EXP, P62
[10]   COMPUTER-SIMULATION STUDIES OF ETHANE PYROLYSIS IN SHOCK-TUBES AT 1206-K [J].
LEE, WM ;
YEH, CT .
JOURNAL OF PHYSICAL CHEMISTRY, 1979, 83 (07) :771-774