Development of an Electrochemical Reactor for the Aqueous Phase Destruction of Chlorinated Hydrocarbons

A cylindrical electrochemical reactor with a 3 in diameter copper or nickel metal foam cathode and a concentric carbon cloth anode was used to destroy aqueous phase carbon tetrachloride (CT). The results show that a high CT conversion can be achieved in regions of the cathode near the anode, but a l...

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Main Author: Wang, Lei
Other Authors: Sáez, A. Eduardo
Language:EN
Published: The University of Arizona. 2008
Subjects:
Online Access:http://hdl.handle.net/10150/195095
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spelling ndltd-arizona.edu-oai-arizona.openrepository.com-10150-1950952015-10-23T04:42:07Z Development of an Electrochemical Reactor for the Aqueous Phase Destruction of Chlorinated Hydrocarbons Wang, Lei Sáez, A. Eduardo Arnold, Robert G. Sáez, A. Eduardo Sáez, A. Eduardo Arnold, Robert G. Betterton, Eric A. Blowers, Paul Aqueous Dechlorination Electrochemical Electrode Groundwater remediation PCE TCE CT A cylindrical electrochemical reactor with a 3 in diameter copper or nickel metal foam cathode and a concentric carbon cloth anode was used to destroy aqueous phase carbon tetrachloride (CT). The results show that a high CT conversion can be achieved in regions of the cathode near the anode, but a low CT conversion is obtained in the region around the center of the cathode. This CT conversion distribution in the radial current-conducting direction suggests that a portion of the cathode worked inefficiently even though the overall CT conversion is still adequate. Further research by changing the solution pH and conductivity suggests that the radial conversion distribution is due to radial variations in cathode surface availability. The inherent difficulties that these results imply with regards to reactor scale up suggested a new approach to the design. An annular reactor, consisting of a thin (3.2 mm) nickel foam cathode wrapped around an inert Plexiglas core and separated for an external concentric anode by a semi-permeable membrane was adopted. Under compatible operating conditions, the annular reactor showed a high overall effluent CT conversion. However, experiments at low pH (2.25) yielded higher conversions than under neutral pH conditions. This result suggests that CT conversion is favored by a relatively high proton concentration. This reactor can be simulated by a one dimensional model. The annular reactor was used to destroy PCE and TCE successfully, which suggests that this technique can be employed to treat groundwater contaminated with complex mixtures of chlorinated hydrocarbons.A multi-layer reactor based on the principle of the annular reactor was developed as an option for the scale up of the system. This reactor exhibited high and uniform radial CT conversion. 2008 text Electronic Dissertation http://hdl.handle.net/10150/195095 659750583 10095 EN Copyright © is held by the author. Digital access to this material is made possible by the University Libraries, University of Arizona. Further transmission, reproduction or presentation (such as public display or performance) of protected items is prohibited except with permission of the author. The University of Arizona.
collection NDLTD
language EN
sources NDLTD
topic Aqueous
Dechlorination
Electrochemical
Electrode
Groundwater remediation
PCE TCE CT
spellingShingle Aqueous
Dechlorination
Electrochemical
Electrode
Groundwater remediation
PCE TCE CT
Wang, Lei
Development of an Electrochemical Reactor for the Aqueous Phase Destruction of Chlorinated Hydrocarbons
description A cylindrical electrochemical reactor with a 3 in diameter copper or nickel metal foam cathode and a concentric carbon cloth anode was used to destroy aqueous phase carbon tetrachloride (CT). The results show that a high CT conversion can be achieved in regions of the cathode near the anode, but a low CT conversion is obtained in the region around the center of the cathode. This CT conversion distribution in the radial current-conducting direction suggests that a portion of the cathode worked inefficiently even though the overall CT conversion is still adequate. Further research by changing the solution pH and conductivity suggests that the radial conversion distribution is due to radial variations in cathode surface availability. The inherent difficulties that these results imply with regards to reactor scale up suggested a new approach to the design. An annular reactor, consisting of a thin (3.2 mm) nickel foam cathode wrapped around an inert Plexiglas core and separated for an external concentric anode by a semi-permeable membrane was adopted. Under compatible operating conditions, the annular reactor showed a high overall effluent CT conversion. However, experiments at low pH (2.25) yielded higher conversions than under neutral pH conditions. This result suggests that CT conversion is favored by a relatively high proton concentration. This reactor can be simulated by a one dimensional model. The annular reactor was used to destroy PCE and TCE successfully, which suggests that this technique can be employed to treat groundwater contaminated with complex mixtures of chlorinated hydrocarbons.A multi-layer reactor based on the principle of the annular reactor was developed as an option for the scale up of the system. This reactor exhibited high and uniform radial CT conversion.
author2 Sáez, A. Eduardo
author_facet Sáez, A. Eduardo
Wang, Lei
author Wang, Lei
author_sort Wang, Lei
title Development of an Electrochemical Reactor for the Aqueous Phase Destruction of Chlorinated Hydrocarbons
title_short Development of an Electrochemical Reactor for the Aqueous Phase Destruction of Chlorinated Hydrocarbons
title_full Development of an Electrochemical Reactor for the Aqueous Phase Destruction of Chlorinated Hydrocarbons
title_fullStr Development of an Electrochemical Reactor for the Aqueous Phase Destruction of Chlorinated Hydrocarbons
title_full_unstemmed Development of an Electrochemical Reactor for the Aqueous Phase Destruction of Chlorinated Hydrocarbons
title_sort development of an electrochemical reactor for the aqueous phase destruction of chlorinated hydrocarbons
publisher The University of Arizona.
publishDate 2008
url http://hdl.handle.net/10150/195095
work_keys_str_mv AT wanglei developmentofanelectrochemicalreactorfortheaqueousphasedestructionofchlorinatedhydrocarbons
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