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Contaminant Resistant Intermediate Temperature Proton Exchange Membrane Fuel Cell System for Military Application

Award Information
Agency: Department of Defense
Branch: Navy
Contract: N00014-09-M-0181
Agency Tracking Number: O083-E09-4050
Amount: $100,000.00
Phase: Phase I
Program: SBIR
Solicitation Topic Code: OSD08-E09
Solicitation Number: 2008.3
Timeline
Solicitation Year: 2008
Award Year: 2009
Award Start Date (Proposal Award Date): 2009-05-11
Award End Date (Contract End Date): 2009-11-11
Small Business Information
7610 Eastmark Drive
College Station, TX 77840
United States
DUNS: 184758308
HUBZone Owned: No
Woman Owned: No
Socially and Economically Disadvantaged: No
Principal Investigator
 Jeremy Steinshnider
 Sr. Research Scientist
 (979) 693-0017
 jeremy.steinshnider@lynntech.com
Business Contact
 G. Duncan Hitchens
Title: Vice President
Phone: (979) 693-0017
Email: proposals@lynntech.com
Research Institution
N/A
Abstract

Intermediate temperature proton exchange membrane fuel cells (PEMFCs) operating directly on the reformates of logistic fuels have a great potential for simplifying the power generation systems for Army and Navy applications. However trace amounts of S and CO contaminants present in the reformate streams as well as in the air in hot battlefields, have a significant poisoning effect on PEMFC catalysts and membrane materials, thus limiting its performance and durability. In the present proposal, therefore a modular approach of PEMFC system design is attempted, to seggregate and resolve the contaminant problems for PEMFC systems separately. An intermediate temperature PEMFC system working at operating temperatures above 150 0C with reformate gas as fuel is proposed, wherein the reformate gas feed and the air feed have separate purification systems, thus eliminating the deleterious effects of contaminants on PEMFC performance and durability. Phase I will develop and demonstrate a conceptual design of a modular fuel cell system operating with reformate gas, with energy density in excess of 100 W/kg and H2 utilization efficiencies in excess of 50 %, which will form the basis of a more detailed design in Phase II.

* Information listed above is at the time of submission. *

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