Effect of Water Transport on the Production of Hydrogen and Sulfuric Acid in a PEM Electrolyzer
Author(s) -
John A. Staser,
John W. Weidner
Publication year - 2008
Publication title -
journal of the electrochemical society
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 1.258
H-Index - 271
eISSN - 1945-7111
pISSN - 0013-4651
DOI - 10.1149/1.3001923
Subject(s) - sulfuric acid , electrolysis , polymer electrolyte membrane electrolysis , high temperature electrolysis , chemistry , electrolysis of water , high pressure electrolysis , hydrogen production , inorganic chemistry , sulfur dioxide , hydrogen , thermochemical cycle , sulfur , chemical engineering , electrolyte , electrode , organic chemistry , engineering
The thermochemical cycle involving the interconversion between sulfur dioxide and sulfuric acid is a promising method for efficient, large-scale production of hydrogen. A key step in the process is the oxidation of sulfur dioxide to sulfuric acid in an electrolyzer. Gaseous SO2 fed to a proton exchange membrane PEM electrolyzer was previously investigated and was shown to be a promising system for the electrolysis step. A critical factor in the performance of this gas-fed electrolyzer is the management of water since it: i is needed as a reactant, ii determines the product sulfuric acid concentration, iii affects SO2 crossover rate, and iv serves to hydrate the membrane. Therefore, we present a coupled mathematical and experimental study on the effect of water on the production of sulfuric acid in a gas-phase PEM electrolyzer. The model is shown to successfully predict the concentration of sulfuric acid as a function of temperature, current density, pressure differential across the membrane, and membrane thickness.
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