Ethanol membrane reformer and PEMFC system for automotive application

被引:19
作者
De Falco, Marcello [1 ,2 ]
机构
[1] Univ Campus Biomed Rome, Fac Engn, I-00128 Rome, Italy
[2] Labor Srl, I-00131 Rome, Italy
关键词
Membrane reactor; H-2 selective membrane; Reformer; PEMFC; HEAT-TRANSFER; HYDROGEN-PRODUCTION; PACKED-BEDS; FUEL-CELLS; PD-AG; STEAM; METHANE; CATALYSTS; REACTORS; PERFORMANCE;
D O I
10.1016/j.fuel.2010.09.054
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The wide diffusion of fuel cell (FC) powered Zero-Emissions Vehicles (ZEVs) is stopped by hydrogen storage technological drawbacks, as high cost and low storage volume density. This obstacle can be overcome if a fuel processor, able to produce H-2 to be fed to FC from a liquid fuel, is installed. In the present work, an innovative clean power generator for light-vehicles is presented, modelled and designed. Such a generator is realized by coupling the most market-appeal clean liquid fuel, the ethanol, and the most technologically strengthened and the only off-the-shelf fuel cell type, the PEMFC, by applying a membrane reactor (MR) for converting ethanol and separating the hydrogen produced in one single and compact device. A process scheme is described and a 4-tubes-and shell membrane reactor is modelled by means of a rigorous homogeneous 2D mathematical model, validated by experimental data. The effect of most important operating conditions, as gas mixture residence time, heating fluid temperature, steam-to-ethanol and sweeping-to ethanol ratios, operating pressure, is evaluated via simulation and optimal conditions are defined. Then, by applying the optimal conditions set, a design of ethanol MR + PEMFC system in substitution of a 4 kW Pb-battery pack for a light vehicle is proposed. Final results attest that a 1.52 m long, 0.4 m large 4-tubes-and-shell membrane reactor (total volume equal to 0.76 m(3)) is able to produce 64.7 NL/min of hydrogen, equal to the 4 kW FC feedstock requirement. The MR ethanol conversion is 98% and the percentage of H-2 recovered through the Pd-Ag selective membrane on total H-2 produced in the reactor is 67% about. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:739 / 747
页数:9
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