Partial oxidation reformer development for fuel cell vehicles

被引：1

作者：

Ahmed, S ^{[1
]}

Doshi, R ^{[1
]}

Lee, SHD ^{[1
]}

Kumar, R ^{[1
]}

Krumpelt, M ^{[1
]}

机构：

[1] Argonne Natl Lab, Electrochem Technol Program, Div Chem Technol, Argonne, IL 60439 USA

来源：

IECEC-97 - PROCEEDINGS OF THE THIRTY-SECOND INTERSOCIETY ENERGY CONVERSION ENGINEERING CONFERENCE, VOLS 1-4: VOL.1: AEROSPACE POWER SYSTEMS AND TECHNOL; VOL 2: ELECTROCHEMICAL TECHNOL, CONVERSION TECHNOL, THERMAL MANAGEMENT; VOLS 3: ENERGY SYSTEMS, RENEWABLE ENERGY RESOURCES, ENVIRONMENTAL IMPACT, POLICY IMPACTS ON ENERGY; VOL 4: POST DEADLINE PAPERS, INDEX | 1997年

关键词：

D O I：

10.1109/IECEC.1997.661878

中图分类号：

V [航空、航天];

学科分类号：

08 ; 0825 ;

摘要：

A bench-scale partial oxidation reformer that is compact (1.8 L) and light-weight has been demonstrated with methanol fuel. The hydrogen output from the reactor had a lower heating value of 12 kW. The gas contained over 50% hydrogen and less than 1% carbon monoxide. A novel class of catalyst materials has been identified which is able to convert various hydrocarbons, including gasoline, to a hydrogen-rich product gas. Tested in a microreactor with gasoline and oxygen at 760 degrees C, these catalysts yielded a product gas containing over 60% hydrogen.

引用

页码：843 / 846

页数：4