Preliminary Equipment Design for On-Board Hydrogen Production by Steam Reforming in Palladium Membrane Reactors

被引:6
|
作者
Holgado, Marina [1 ]
Alique, David [1 ]
机构
[1] Rey Juan Carlos Univ, Dept Chem Energy & Mech Technol, C Tulipan S-N, Mostoles 28933, Spain
关键词
hydrogen; on-board; steam reforming; ethanol; methane; membrane reactor; palladium; modeling;
D O I
10.3390/chemengineering3010006
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrogen, as an energy carrier, can take the main role in the transition to a new energy model based on renewable sources. However, its application in the transport sector is limited by its difficult storage and the lack of infrastructure for its distribution. On-board H-2 production is proposed as a possible solution to these problems, especially in the case of considering renewable feedstocks such as bio-ethanol or bio-methane. This work addresses a first approach for analyzing the viability of these alternatives by using Pd-membrane reactors in polymer electrolyte membrane fuel cell (PEM-FC) vehicles. It has been demonstrated that the use of Pd-based membrane reactors enhances hydrogen productivity and provides enough pure hydrogen to feed the PEM-FC requirements in one single step. Both alternatives seem to be feasible, although the methane-based on-board hydrogen production offers some additional advantages. For this case, it is possible to generate 1.82 kmol h(-1) of pure H-2 to feed the PEM-FC while minimizing the CO2 emissions to 71 g CO2/100 km. This value would be under the future emissions limits proposed by the European Union (EU) for year 2020. In this case, the operating conditions of the on-board reformer are T = 650 degrees C, P-ret = 10 bar and H2O/CH4 = 2.25, requiring 1 kg of catalyst load and a membrane area of 1.76 m(2).
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页码:1 / 13
页数:13
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