An Electrochemical Claus Process for Sulfur Recovery

Electrochemical oxidation of H{sub 2}S to give sulfur and water was achieved at 900{degrees}C using fuel cells possessing the general configuration where anode electrocatalysts experimentally investigated for promoting the subject oxidation reaction included WS{sub 2} and the thiospinels CuNi{sub 2}...

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Published inJournal of the Electrochemical Society Vol. 136; no. 12; pp. 3662 - 3678
Main Authors Pujare, Nirupama U., Tsai, Kan J., Sammells, Anthony F.
Format Journal Article
LanguageEnglish
Published Pennington, NJ Electrochemical Society 01.12.1989
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Abstract Electrochemical oxidation of H{sub 2}S to give sulfur and water was achieved at 900{degrees}C using fuel cells possessing the general configuration where anode electrocatalysts experimentally investigated for promoting the subject oxidation reaction included WS{sub 2} and the thiospinels CuNi{sub 2}S{sub 4}, CuCo{sub 2}S{sub 4}, CuFe{sub 2}S{sub 4}, and NiFe{sub 2}S{sub 4}. The predominant oxidizable electroactive species present in the fuel cell anode compartment was suggested to be hydrogen originating from the initial thermal dissociation of H{sub 2}S (H{sub 2}S {r reversible} H{sub 2} + 1/2 S{sub 2}) at fuel cell operating temperatures. Rapid anode kinetics were found for the anodic reaction with the empirical trend for exchange currents (i{sub o}) per geometric area being found to be NiFe{sub 2}S{sub 4}{gt}WS{sub 2}{gt}CuCo{sub 2}S{sub 4}{gt}CuFe{sub 2}S{sub 4}{approx equal}NiCo{sub 2}S{sub 4}{gt}CuNi{sub 2}S{sub 4}.
AbstractList Electrochemical oxidation of H{sub 2}S to give sulfur and water was achieved at 900{degrees}C using fuel cells possessing the general configuration where anode electrocatalysts experimentally investigated for promoting the subject oxidation reaction included WS{sub 2} and the thiospinels CuNi{sub 2}S{sub 4}, CuCo{sub 2}S{sub 4}, CuFe{sub 2}S{sub 4}, and NiFe{sub 2}S{sub 4}. The predominant oxidizable electroactive species present in the fuel cell anode compartment was suggested to be hydrogen originating from the initial thermal dissociation of H{sub 2}S (H{sub 2}S {r reversible} H{sub 2} + 1/2 S{sub 2}) at fuel cell operating temperatures. Rapid anode kinetics were found for the anodic reaction with the empirical trend for exchange currents (i{sub o}) per geometric area being found to be NiFe{sub 2}S{sub 4}{gt}WS{sub 2}{gt}CuCo{sub 2}S{sub 4}{gt}CuFe{sub 2}S{sub 4}{approx equal}NiCo{sub 2}S{sub 4}{gt}CuNi{sub 2}S{sub 4}.
Author Tsai, Kan J.
Pujare, Nirupama U.
Sammells, Anthony F.
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  organization: Eltron Research, Incorporated, Aurora, Illinois 60504
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Snippet Electrochemical oxidation of H{sub 2}S to give sulfur and water was achieved at 900{degrees}C using fuel cells possessing the general configuration where anode...
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StartPage 3662
SubjectTerms 30 DIRECT ENERGY CONVERSION
300504 - Fuel Cells- Applications
300505 - Fuel Cells- Electrochemistry, Mass Transfer & Thermodynamics
320305 - Energy Conservation, Consumption, & Utilization- Industrial & Agricultural Processes- Industrial Waste Management
400400 - Electrochemistry
ANODES
Applied sciences
CATALYSTS
CHALCOGENIDES
CHEMICAL REACTION KINETICS
CHEMICAL REACTIONS
CHEMISTRY
CLAUS PROCESS
CONFIGURATION
DATA
Direct energy conversion and energy accumulation
DIRECT ENERGY CONVERTERS
Electrical engineering. Electrical power engineering
Electrical power engineering
ELECTROCATALYSTS
ELECTROCHEMICAL CELLS
Electrochemical conversion: primary and secondary batteries, fuel cells
ELECTROCHEMISTRY
ELECTRODES
ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION
Exact sciences and technology
EXPERIMENTAL DATA
FUEL CELLS
HYDROGEN COMPOUNDS
HYDROGEN SULFIDES
INFORMATION
INORGANIC, ORGANIC, PHYSICAL AND ANALYTICAL CHEMISTRY
KINETICS
MANGANESE COMPOUNDS
MANGANESE OXIDES
NUMERICAL DATA
OXIDATION
OXIDES
OXYGEN COMPOUNDS
PLATINUM COMPOUNDS
PLATINUM OXIDES
REACTION KINETICS
REFRACTORY METAL COMPOUNDS
STABILIZATION
SULFIDES
SULFUR COMPOUNDS
TRANSITION ELEMENT COMPOUNDS
TUNGSTEN COMPOUNDS
TUNGSTEN SULFIDES
USES
ZIRCONIUM COMPOUNDS
ZIRCONIUM OXIDES
Title An Electrochemical Claus Process for Sulfur Recovery
URI https://www.osti.gov/biblio/7227060
Volume 136
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