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      Electrochemical Production of Hydrogen Peroxide in Perchloric Acid Supporting Electrolytes for the Synthesis of Chlorine Dioxide

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          Abstract

          This work focuses on the electrochemical production of hydrogen peroxide in supporting electrolytes containing perchlorate ions for being used as a reagent in the reduction of chlorates to produce chlorine dioxide, as a first step in the manufacture of portable ClO 2 production devices. This study evaluates the effect of the current density, pressure, and temperature on the production of hydrogen peroxide, and concentrations over 400 mg L –1 are reached. The average rate for the formation of hydrogen peroxide is 9.85 mg h –1, and the effect of increasing electrolyte concentration (3.0 and 30.0 g L –1 perchloric acid), intensity, and pressure results in values of, respectively, −2.99, −4.49, and +7.73 mg h –1. During the manufacturing process, hydrogen peroxide is decomposed through two mechanisms. The average destruction rate is 1.93 mg h –1, and the effects of the three factors results in values of, respectively, +0.07, +0.11, and −0.12 mg h –1. Solutions of this hydrogen peroxide produced electrochemically in a perchloric acid aqueous electrolyte were used to reduce chlorates in strongly acidic media and produce chlorine dioxide. Conversions of around 100% were obtained, demonstrating that this electrochemical product can be used efficiently to reduce chlorates to chlorine dioxide.

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          Electrochemical synthesis of hydrogen peroxide from water and oxygen

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            Colorimetric Determination of Hydrogen Peroxide

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              General technoeconomic analysis for electrochemical coproduction coupling carbon dioxide reduction with organic oxidation

              Electrochemical processes coupling carbon dioxide reduction reactions with organic oxidation reactions are promising techniques for producing clean chemicals and utilizing renewable energy. However, assessments of the economics of the coupling technology remain questionable due to diverse product combinations and significant process design variability. Here, we report a technoeconomic analysis of electrochemical carbon dioxide reduction reaction–organic oxidation reaction coproduction via conceptual process design and thereby propose potential economic combinations. We first develop a fully automated process synthesis framework to guide process simulations, which are then employed to predict the levelized costs of chemicals. We then identify the global sensitivity of current density, Faraday efficiency, and overpotential across 295 electrochemical coproduction processes to both understand and predict the levelized costs of chemicals at various technology levels. The analysis highlights the promise that coupling the carbon dioxide reduction reaction with the value-added organic oxidation reaction can secure significant economic feasibility.
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                Author and article information

                Journal
                Ind Eng Chem Res
                Ind Eng Chem Res
                ie
                iecred
                Industrial & Engineering Chemistry Research
                American Chemical Society
                0888-5885
                1520-5045
                24 February 2022
                09 March 2022
                : 61
                : 9
                : 3263-3271
                Affiliations
                []Institute of Chemistry, Environmental and Applied Electrochemical Laboratory, Federal University of Rio Grande do Norte , Lagoa Nova, CEP, Natal 59078-970, Rio Grande do Norte, Brazil
                []Department of Chemical Engineering, Faculty of Chemical Sciences & Technologies, University of Castilla-La Mancha , Campus Universitario s/n, Ciudad Real 13005, Spain
                Author notes
                [* ]Email: manuel.rodrigo@ 123456uclm.es . Phone: +34-926-29-53-00 Ext. 3411.
                Author information
                https://orcid.org/0000-0001-6652-0496
                https://orcid.org/0000-0003-2518-8436
                Article
                10.1021/acs.iecr.1c04845
                8919508
                35300272
                215893bf-d78f-4dba-b3de-2aaeee7e3717
                © 2022 The Authors. Published by American Chemical Society

                Permits the broadest form of re-use including for commercial purposes, provided that author attribution and integrity are maintained ( https://creativecommons.org/licenses/by/4.0/).

                History
                : 10 December 2021
                : 16 February 2022
                : 15 February 2022
                Funding
                Funded by: Conselho Nacional de Desenvolvimento Científico e Tecnológico, doi 10.13039/501100003593;
                Award ID: 202069/2019-2
                Funded by: Agencia Estatal de Investigación, doi NA;
                Award ID: PID2019-110904RB-I00
                Funded by: Agencia Estatal de Investigación, doi NA;
                Award ID: PID2019-107271RB-I00
                Funded by: European Regional Development Fund, doi 10.13039/501100008530;
                Award ID: PID2019-110904RB-I00
                Funded by: European Regional Development Fund, doi 10.13039/501100008530;
                Award ID: PID2019-107271RB-I00
                Categories
                Article
                Custom metadata
                ie1c04845
                ie1c04845

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