Qingfeng Li

Prof. Dr. Qingfeng Li

Department of Energy Conversion and Storage, Technical University of Denmark, 2800 Lyngby, Denmark

Research Focus & Metrics

Academic Career Length

38Years (1989-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 December 2003 in Chemistry of Materials
Verified
Journal Article
Open access
Qingfeng LiQingfeng Li
Qingfeng Li
RHRonghuan He
Ronghuan He
Jens Oluf JensenJens Oluf Jensen
Jens Oluf Jensen
NBNiels J. Bjerrum
Niels J. Bjerrum
The state-of-the-art of polymer electrolyte membrane fuel cell (PEMFC) technology is based on perfluorosulfonic acid (PFSA) polymer membranes operating at a typical temperature of 80 °C. Some of the key issues and shortcomings of the PFSA-based PEMFC technology are briefly discussed. These include water management, CO poisoning, hydrogen, reformate and methanol as fuels, cooling, and heat recovery. As a means to solve these shortcomings, high-temperature polymer electrolyte membranes for operation above 100 °C are under active development. This treatise is devoted to a review of the area encompassing modified PFSA membranes, alternative sulfonated polymer and their composite membranes, and acid−base complex membranes. PFSA membranes have been modified by swelling with nonvolatile solvents and preparing composites with hydrophilic oxides and solid proton conductors. DMFC and H2/O2(air) cells based on modified PFSA membranes have been successfully operated at temperatures up to 120 °C under ambient pressure and up to 150 °C under 3−5 atm. Alternative polymers are selected from silicon- and fluorine-containing inorganic polymers or aromatic hydrocarbon polymers and functionalized by sulfonation. The sulfonated hydrocarbons and their inorganic composites are potentially promising for high-temperature operation. High conductivities have been obtained at temperatures up to 180 °C. Acid−base complex membranes constitute another class of electrolyte membranes. A high-temperature PEMFC based on H3PO4-doped PBI has been demonstrated for operation at temperatures up to 200 °C under ambient pressure. The advanced features include high CO tolerance, simple thermal and water management, and possible integration with the fuel processing unit.

1 May 2009 in Progress in Polymer Science
Verified
Journal Article
Closed access
Qingfeng LiQingfeng Li
Qingfeng Li
Jens Oluf JensenJens Oluf Jensen
Jens Oluf Jensen
RSRobert F. Savinell
Robert F. Savinell
NBNiels J. Bjerrum
Niels J. Bjerrum

19 February 2014 in Angewandte Chemie International Edition
Verified
Journal Article
Closed access
PDF file
YHYang Hu
Yang Hu
Jens Oluf JensenJens Oluf Jensen
Jens Oluf Jensen
WZWei Zhang
Wei Zhang
LCLars N. Cleemann
Lars N. Cleemann
WXWei Xing
Wei Xing
Qingfeng LiQingfeng Li
Qingfeng Li

1 July 2002 in Journal of Power Sources
Verified
Journal Article
Closed access
Qingfeng LiQingfeng Li
Qingfeng Li
NBNiels J Bjerrum
Niels J Bjerrum


1 January 2003 in Journal of the Electrochemical Society
Verified
Journal Article
Closed access
PDF file
Qingfeng LiQingfeng Li
Qingfeng Li
RHRonghuan He
Ronghuan He
JGJi-An Gao
Ji-An Gao
Jens Oluf JensenJens Oluf Jensen
Jens Oluf Jensen
NBNiels. J. Bjerrum
Niels. J. Bjerrum
The CO poisoning effect on carbon-supported platinum catalysts (at a loading of 0.5 mg <mml:math display="inline"><mml:mi mathvariant="normal">Pt</mml:mi><mml:mo>/</mml:mo><mml:msup><mml:mi mathvariant="normal">cm</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:math>Pt/cm2 per electrode) in polymer electrolyte membrane fuel cells (PEMFCs) has been investigated in a temperature range from 125 to 200°C with the phosphoric acid-doped polybenzimidazole membranes as electrolyte. The effect is very temperature-dependent and can be sufficiently suppressed at elevated temperature. By defining the CO tolerance as a voltage loss less than 10 mV, it is evaluated that 3% CO in hydrogen can be tolerated at current densities up to <mml:math display="inline"><mml:mn>0.8</mml:mn><mml:mo>A</mml:mo><mml:mo>/</mml:mo><mml:msup><mml:mi mathvariant="normal">cm</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup></mml:math>0.8A/cm2 at 200°C, while at 125°C 0.1% CO in hydrogen can be tolerated at current densities lower than <mml:math display="inline"><mml:mn>0.3</mml:mn><mml:mo>A</mml:mo><mml:mo>/</mml:mo><mml:msup><mml:mi mathvariant="normal">cm</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>.</mml:mo></mml:math>0.3A/cm2. For comparison, the tolerance is only 0.0025% CO (25 ppm) at 80°C at current densities up to <mml:math display="inline"><mml:mn>0.2</mml:mn><mml:mo>A</mml:mo><mml:mo>/</mml:mo><mml:msup><mml:mi mathvariant="normal">cm</mml:mi><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msup><mml:mo>.</mml:mo></mml:math>0.2A/cm2. The relative anode activity for hydrogen oxidation was calculated as a function of the CO concentration and temperature. The effect of <mml:math display="inline"><mml:msub><mml:mo>CO</mml:mo><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math>CO2 in hydrogen was also studied. At 175°C, 25% <mml:math display="inline"><mml:msub><mml:mo>CO</mml:mo><mml:mrow><mml:mn>2</mml:mn></mml:mrow></mml:msub></mml:math>CO2 in the fuel stream showed only the dilution effect. © 2003 The Electrochemical Society. All rights reserved.