influence of precipitate formation on the chemical oxidation of TCE DNAPL with potassium permanganate

A three-dimensional two-phase flow model is coupled to a non-linear reactive transport model to study the efficacy of potassium permanganate treatment on dense, non-aqueous phase liquid (DNAPL) source removal in porous media. A linear relationship between the soil permeability (k) and concentration...

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Veröffentlicht in:Advances in water resources 2008-02, Vol.31 (2), p.324-338
Hauptverfasser: West, M.R, Grant, G.P, Gerhard, J.I, Kueper, B.H
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Gerhard, J.I
Kueper, B.H
description A three-dimensional two-phase flow model is coupled to a non-linear reactive transport model to study the efficacy of potassium permanganate treatment on dense, non-aqueous phase liquid (DNAPL) source removal in porous media. A linear relationship between the soil permeability (k) and concentration of manganese dioxide precipitate ([MnO sub(2) sub(() sub(s) sub())]), k=k sub(o)+S sub(r) sub(i) sub(n) sub(d) [MnO sub(2) sub(() sub(s) sub())], is utilized to simulate nodal permeability reductions due to precipitate formation. Using published experimental column studies, an S sub(r) sub(i) sub(n) sub(d)=-5.5x10 super(-) super(1) super(6)m super(2)L /mg was determined for trichloroethylene (TCE) DNAPL. This S sub(r) sub(i) sub(n) sub(d) was then applied to treatment simulations on three-dimensional TCE DNAPL source zones comprising either DNAPL at residual saturations, or DNAPL at pooled saturations. DNAPL dissolution without oxidation treatment, simulated using equilibrium and the Nambi and Powers [Nambi I, Powers S. Mass transfer correlations for non-aqueous phase liquid dissolution from regions with high initial saturations. Water Resour Res 2003; 39(2):1-11, SBH 4] mass transfer expression, required 31 and 36 years, respectively, to eliminate the residual source zone. For equilibrium dissolution with continuous treatment and no precipitate influence (S sub(r) sub(i) sub(n) sub(d)=0m super(2)L/mg), the residual source zone was removed after 11 years. However, when considering the precipitate influence (i.e., S sub(r) sub(i) sub(n) sub(d)=-5.5x10 super(-) super(1) super(6)m super(2)L/mg), 21 years of treatment were necessary to remove the DNAPL. When considering pulse treatments of 1 and 2 years duration followed by only dissolution, approximately 36 and 38 years, respectively, were required before the source zone was depleted, suggesting that there is no benefit to pulse treatment. Similar trends were observed when allowing 10 years of dissolution prior to treatment initiation. The treatment behaviour of the pooled TCE source, while slightly more efficient than the residual saturation source, was similar. Based on simulation findings, the precipitate (rind) formation significantly influences DNAPL treatment with permanganate; the most significant reductions in efficacy were observed for single pulse treatments (of 1 and 2 years), which exhibited times to source depletion similar to the case of dissolution without treatment.
doi_str_mv 10.1016/j.advwatres.2007.08.011
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A linear relationship between the soil permeability (k) and concentration of manganese dioxide precipitate ([MnO sub(2) sub(() sub(s) sub())]), k=k sub(o)+S sub(r) sub(i) sub(n) sub(d) [MnO sub(2) sub(() sub(s) sub())], is utilized to simulate nodal permeability reductions due to precipitate formation. Using published experimental column studies, an S sub(r) sub(i) sub(n) sub(d)=-5.5x10 super(-) super(1) super(6)m super(2)L /mg was determined for trichloroethylene (TCE) DNAPL. This S sub(r) sub(i) sub(n) sub(d) was then applied to treatment simulations on three-dimensional TCE DNAPL source zones comprising either DNAPL at residual saturations, or DNAPL at pooled saturations. DNAPL dissolution without oxidation treatment, simulated using equilibrium and the Nambi and Powers [Nambi I, Powers S. Mass transfer correlations for non-aqueous phase liquid dissolution from regions with high initial saturations. Water Resour Res 2003; 39(2):1-11, SBH 4] mass transfer expression, required 31 and 36 years, respectively, to eliminate the residual source zone. For equilibrium dissolution with continuous treatment and no precipitate influence (S sub(r) sub(i) sub(n) sub(d)=0m super(2)L/mg), the residual source zone was removed after 11 years. However, when considering the precipitate influence (i.e., S sub(r) sub(i) sub(n) sub(d)=-5.5x10 super(-) super(1) super(6)m super(2)L/mg), 21 years of treatment were necessary to remove the DNAPL. When considering pulse treatments of 1 and 2 years duration followed by only dissolution, approximately 36 and 38 years, respectively, were required before the source zone was depleted, suggesting that there is no benefit to pulse treatment. Similar trends were observed when allowing 10 years of dissolution prior to treatment initiation. The treatment behaviour of the pooled TCE source, while slightly more efficient than the residual saturation source, was similar. 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A linear relationship between the soil permeability (k) and concentration of manganese dioxide precipitate ([MnO sub(2) sub(() sub(s) sub())]), k=k sub(o)+S sub(r) sub(i) sub(n) sub(d) [MnO sub(2) sub(() sub(s) sub())], is utilized to simulate nodal permeability reductions due to precipitate formation. Using published experimental column studies, an S sub(r) sub(i) sub(n) sub(d)=-5.5x10 super(-) super(1) super(6)m super(2)L /mg was determined for trichloroethylene (TCE) DNAPL. This S sub(r) sub(i) sub(n) sub(d) was then applied to treatment simulations on three-dimensional TCE DNAPL source zones comprising either DNAPL at residual saturations, or DNAPL at pooled saturations. DNAPL dissolution without oxidation treatment, simulated using equilibrium and the Nambi and Powers [Nambi I, Powers S. Mass transfer correlations for non-aqueous phase liquid dissolution from regions with high initial saturations. Water Resour Res 2003; 39(2):1-11, SBH 4] mass transfer expression, required 31 and 36 years, respectively, to eliminate the residual source zone. For equilibrium dissolution with continuous treatment and no precipitate influence (S sub(r) sub(i) sub(n) sub(d)=0m super(2)L/mg), the residual source zone was removed after 11 years. However, when considering the precipitate influence (i.e., S sub(r) sub(i) sub(n) sub(d)=-5.5x10 super(-) super(1) super(6)m super(2)L/mg), 21 years of treatment were necessary to remove the DNAPL. When considering pulse treatments of 1 and 2 years duration followed by only dissolution, approximately 36 and 38 years, respectively, were required before the source zone was depleted, suggesting that there is no benefit to pulse treatment. Similar trends were observed when allowing 10 years of dissolution prior to treatment initiation. The treatment behaviour of the pooled TCE source, while slightly more efficient than the residual saturation source, was similar. 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Hydrogeology</subject><subject>mathematical models</subject><subject>nonaqueous phase liquids</subject><subject>oxidation</subject><subject>Pollution, environment geology</subject><subject>porous media</subject><subject>potassium permanganate</subject><subject>remediation</subject><subject>simulation models</subject><subject>trichloroethylene</subject><issn>0309-1708</issn><issn>1872-9657</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2008</creationdate><recordtype>article</recordtype><recordid>eNpFkMFq3DAQhkVpoNs0zxBd2pudkey1pGPYJm1haQvZnIUkj7JabMuVvEn79lXYpYWBOcz3_wMfIdcMagasuznUpn9-MUvCXHMAUYOsgbE3ZMWk4JXq1uItWUEDqmIC5DvyPucDAMhW8BXBMPnhiJNDGj2dE7owh8UsSH1Mo1lCnGiZZY_U7XEMzgw0_g79-eLpbnNHP3-__bmlL2HZ0zkuJudwHOmMJT89mamUfSAX3gwZr877kuzu73abr9X2x5dvm9ttZZpuvVRr26IT0rKWg1S95c4xBU5w3njrsbedhR6ZFbwF1oJHIwVYBT10tlW8uSSfTrVzir-OmBc9huxwGMyE8Zg1h04BV00BxQl0Keac0Os5hdGkP5qBfrWqD_qfVf1qVYPUxWpJfjy_MLm48MlMLuT_caVUI0EV7vrEeRO1eUqFeXzgwJoivms5481fuGSF9w</recordid><startdate>20080201</startdate><enddate>20080201</enddate><creator>West, M.R</creator><creator>Grant, G.P</creator><creator>Gerhard, J.I</creator><creator>Kueper, B.H</creator><general>Elsevier Science</general><scope>FBQ</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7UA</scope><scope>C1K</scope><scope>F1W</scope><scope>H96</scope><scope>L.G</scope></search><sort><creationdate>20080201</creationdate><title>influence of precipitate formation on the chemical oxidation of TCE DNAPL with potassium permanganate</title><author>West, M.R ; Grant, G.P ; Gerhard, J.I ; Kueper, B.H</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a365t-5b4ec78b142089db2cc190c7223fbfedb6b0de1b7240140fea870b90d06b4923</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2008</creationdate><topic>aquifers</topic><topic>chemical precipitation</topic><topic>Earth sciences</topic><topic>Earth, ocean, space</topic><topic>Engineering and environment geology. Geothermics</topic><topic>Exact sciences and technology</topic><topic>groundwater contamination</topic><topic>Hydrogeology</topic><topic>hydrologic models</topic><topic>Hydrology. Hydrogeology</topic><topic>mathematical models</topic><topic>nonaqueous phase liquids</topic><topic>oxidation</topic><topic>Pollution, environment geology</topic><topic>porous media</topic><topic>potassium permanganate</topic><topic>remediation</topic><topic>simulation models</topic><topic>trichloroethylene</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>West, M.R</creatorcontrib><creatorcontrib>Grant, G.P</creatorcontrib><creatorcontrib>Gerhard, J.I</creatorcontrib><creatorcontrib>Kueper, B.H</creatorcontrib><collection>AGRIS</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><collection>Water Resources Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>Aquatic Science &amp; Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy &amp; Non-Living Resources</collection><collection>Aquatic Science &amp; Fisheries Abstracts (ASFA) Professional</collection><jtitle>Advances in water resources</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>West, M.R</au><au>Grant, G.P</au><au>Gerhard, J.I</au><au>Kueper, B.H</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>influence of precipitate formation on the chemical oxidation of TCE DNAPL with potassium permanganate</atitle><jtitle>Advances in water resources</jtitle><date>2008-02-01</date><risdate>2008</risdate><volume>31</volume><issue>2</issue><spage>324</spage><epage>338</epage><pages>324-338</pages><issn>0309-1708</issn><eissn>1872-9657</eissn><coden>AWREDI</coden><abstract>A three-dimensional two-phase flow model is coupled to a non-linear reactive transport model to study the efficacy of potassium permanganate treatment on dense, non-aqueous phase liquid (DNAPL) source removal in porous media. A linear relationship between the soil permeability (k) and concentration of manganese dioxide precipitate ([MnO sub(2) sub(() sub(s) sub())]), k=k sub(o)+S sub(r) sub(i) sub(n) sub(d) [MnO sub(2) sub(() sub(s) sub())], is utilized to simulate nodal permeability reductions due to precipitate formation. Using published experimental column studies, an S sub(r) sub(i) sub(n) sub(d)=-5.5x10 super(-) super(1) super(6)m super(2)L /mg was determined for trichloroethylene (TCE) DNAPL. This S sub(r) sub(i) sub(n) sub(d) was then applied to treatment simulations on three-dimensional TCE DNAPL source zones comprising either DNAPL at residual saturations, or DNAPL at pooled saturations. DNAPL dissolution without oxidation treatment, simulated using equilibrium and the Nambi and Powers [Nambi I, Powers S. Mass transfer correlations for non-aqueous phase liquid dissolution from regions with high initial saturations. Water Resour Res 2003; 39(2):1-11, SBH 4] mass transfer expression, required 31 and 36 years, respectively, to eliminate the residual source zone. For equilibrium dissolution with continuous treatment and no precipitate influence (S sub(r) sub(i) sub(n) sub(d)=0m super(2)L/mg), the residual source zone was removed after 11 years. However, when considering the precipitate influence (i.e., S sub(r) sub(i) sub(n) sub(d)=-5.5x10 super(-) super(1) super(6)m super(2)L/mg), 21 years of treatment were necessary to remove the DNAPL. When considering pulse treatments of 1 and 2 years duration followed by only dissolution, approximately 36 and 38 years, respectively, were required before the source zone was depleted, suggesting that there is no benefit to pulse treatment. Similar trends were observed when allowing 10 years of dissolution prior to treatment initiation. The treatment behaviour of the pooled TCE source, while slightly more efficient than the residual saturation source, was similar. Based on simulation findings, the precipitate (rind) formation significantly influences DNAPL treatment with permanganate; the most significant reductions in efficacy were observed for single pulse treatments (of 1 and 2 years), which exhibited times to source depletion similar to the case of dissolution without treatment.</abstract><cop>Oxford</cop><pub>Elsevier Science</pub><doi>10.1016/j.advwatres.2007.08.011</doi><tpages>15</tpages></addata></record>
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subjects aquifers
chemical precipitation
Earth sciences
Earth, ocean, space
Engineering and environment geology. Geothermics
Exact sciences and technology
groundwater contamination
Hydrogeology
hydrologic models
Hydrology. Hydrogeology
mathematical models
nonaqueous phase liquids
oxidation
Pollution, environment geology
porous media
potassium permanganate
remediation
simulation models
trichloroethylene
title influence of precipitate formation on the chemical oxidation of TCE DNAPL with potassium permanganate
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