Effects of pH on dechlorination of trichloroethylene by zero-valent iron
The surface normalized reaction rate constants ( k sa) of trichloroethylene (TCE) and zero-valent iron (ZVI) were quantified in batch reactors at pH values between 1.7 and 10. The k sa of TCE linearly decreased from 0.044 to 0.009 l/h m 2 between pH 3.8 and 8.0, whereas the k sa at pH 1.7 was more t...
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creator | Chen, Jiann-Long Al-Abed, Souhail R Ryan, James A Li, Zhenbin |
description | The surface normalized reaction rate constants (
k
sa) of trichloroethylene (TCE) and zero-valent iron (ZVI) were quantified in batch reactors at pH values between 1.7 and 10. The
k
sa of TCE linearly decreased from 0.044 to 0.009
l/h
m
2 between pH 3.8 and 8.0, whereas the
k
sa at pH 1.7 was more than an order higher than that at pH 3.8. The degradation of TCE was not observed at pH values of 9 and 10. The
k
sa of iron corrosion linearly decreased from 0.092 to 0.018
l/h
m
2 between pH 4.9 and 9.8, whereas it is significantly higher at pH 1.7 and 3.8. The
k
sa of TCE was 30–300 times higher than those reported in literature. The difference can be attributed to the pH effects and precipitation of iron hydroxide. The
k
sa of TCE degradation and iron corrosion at a head space of 6 and 10
ml were about twice of those at zero head space. The effect was attributed to the formation of hydrogen bubbles on ZVI, which hindered the transport the TCE between the solution and reaction sites on ZVI. The optimal TCE degradation rate was achieved at a pH of 4.9. This suggests that lowering solution pH might not expedite the degradation rate of TCE by ZVI as it also caused faster disappearance of ZVI, and hence decreased the ZVI surface concentration. |
doi_str_mv | 10.1016/S0304-3894(01)00193-5 |
format | Article |
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k
sa) of trichloroethylene (TCE) and zero-valent iron (ZVI) were quantified in batch reactors at pH values between 1.7 and 10. The
k
sa of TCE linearly decreased from 0.044 to 0.009
l/h
m
2 between pH 3.8 and 8.0, whereas the
k
sa at pH 1.7 was more than an order higher than that at pH 3.8. The degradation of TCE was not observed at pH values of 9 and 10. The
k
sa of iron corrosion linearly decreased from 0.092 to 0.018
l/h
m
2 between pH 4.9 and 9.8, whereas it is significantly higher at pH 1.7 and 3.8. The
k
sa of TCE was 30–300 times higher than those reported in literature. The difference can be attributed to the pH effects and precipitation of iron hydroxide. The
k
sa of TCE degradation and iron corrosion at a head space of 6 and 10
ml were about twice of those at zero head space. The effect was attributed to the formation of hydrogen bubbles on ZVI, which hindered the transport the TCE between the solution and reaction sites on ZVI. The optimal TCE degradation rate was achieved at a pH of 4.9. This suggests that lowering solution pH might not expedite the degradation rate of TCE by ZVI as it also caused faster disappearance of ZVI, and hence decreased the ZVI surface concentration.</description><identifier>ISSN: 0304-3894</identifier><identifier>EISSN: 1873-3336</identifier><identifier>DOI: 10.1016/S0304-3894(01)00193-5</identifier><identifier>PMID: 11348735</identifier><identifier>CODEN: JHMAD9</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Applied sciences ; Chlorinated organics ; Chlorine Compounds - chemistry ; Earth sciences ; Earth, ocean, space ; Engineering and environment geology. Geothermics ; Exact sciences and technology ; Groundwaters ; Hydrogen-Ion Concentration ; Iron - chemistry ; Iron corrosion ; Natural water pollution ; Organic Chemicals ; Pollution ; Pollution, environment geology ; trichloroethylene ; Trichloroethylene (TCE) ; Trichloroethylene - chemistry ; Water Pollution - prevention & control ; Water treatment and pollution ; Zero-valent iron (ZVI)</subject><ispartof>Journal of hazardous materials, 2001-05, Vol.83 (3), p.243-254</ispartof><rights>2001 Elsevier Science B.V.</rights><rights>2001 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c517t-a2d34e71a1e4f3cea1ca453488a42e6101dc473bdeb66da78172aa60cdab69df3</citedby><cites>FETCH-LOGICAL-c517t-a2d34e71a1e4f3cea1ca453488a42e6101dc473bdeb66da78172aa60cdab69df3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/S0304-3894(01)00193-5$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,778,782,3539,27911,27912,45982</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=993644$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/11348735$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Chen, Jiann-Long</creatorcontrib><creatorcontrib>Al-Abed, Souhail R</creatorcontrib><creatorcontrib>Ryan, James A</creatorcontrib><creatorcontrib>Li, Zhenbin</creatorcontrib><title>Effects of pH on dechlorination of trichloroethylene by zero-valent iron</title><title>Journal of hazardous materials</title><addtitle>J Hazard Mater</addtitle><description>The surface normalized reaction rate constants (
k
sa) of trichloroethylene (TCE) and zero-valent iron (ZVI) were quantified in batch reactors at pH values between 1.7 and 10. The
k
sa of TCE linearly decreased from 0.044 to 0.009
l/h
m
2 between pH 3.8 and 8.0, whereas the
k
sa at pH 1.7 was more than an order higher than that at pH 3.8. The degradation of TCE was not observed at pH values of 9 and 10. The
k
sa of iron corrosion linearly decreased from 0.092 to 0.018
l/h
m
2 between pH 4.9 and 9.8, whereas it is significantly higher at pH 1.7 and 3.8. The
k
sa of TCE was 30–300 times higher than those reported in literature. The difference can be attributed to the pH effects and precipitation of iron hydroxide. The
k
sa of TCE degradation and iron corrosion at a head space of 6 and 10
ml were about twice of those at zero head space. The effect was attributed to the formation of hydrogen bubbles on ZVI, which hindered the transport the TCE between the solution and reaction sites on ZVI. The optimal TCE degradation rate was achieved at a pH of 4.9. This suggests that lowering solution pH might not expedite the degradation rate of TCE by ZVI as it also caused faster disappearance of ZVI, and hence decreased the ZVI surface concentration.</description><subject>Applied sciences</subject><subject>Chlorinated organics</subject><subject>Chlorine Compounds - chemistry</subject><subject>Earth sciences</subject><subject>Earth, ocean, space</subject><subject>Engineering and environment geology. Geothermics</subject><subject>Exact sciences and technology</subject><subject>Groundwaters</subject><subject>Hydrogen-Ion Concentration</subject><subject>Iron - chemistry</subject><subject>Iron corrosion</subject><subject>Natural water pollution</subject><subject>Organic Chemicals</subject><subject>Pollution</subject><subject>Pollution, environment geology</subject><subject>trichloroethylene</subject><subject>Trichloroethylene (TCE)</subject><subject>Trichloroethylene - chemistry</subject><subject>Water Pollution - prevention & control</subject><subject>Water treatment and pollution</subject><subject>Zero-valent iron (ZVI)</subject><issn>0304-3894</issn><issn>1873-3336</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2001</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqFkUtLAzEQgIMotlZ_grIgiB5Wkya72T2JlGqFggf1HGaTWRrZbmqyLdRfb_pAjz0NM3zzyBdCLhm9Z5TlD--UU5HyohS3lN1RykqeZkekzwrJU855fkz6f0iPnIXwRSMlM3FKeoxxEbmsTybjukbdhcTVyWKSuDYxqGeN87aFzsY01jtvtyWH3WzdYItJtU5-0Lt0BTHtEutde05OamgCXuzjgHw-jz9Gk3T69vI6epqmOmOyS2FouEDJgKGouUZgGkQWrylADDGPTzNaSF4ZrPLcgCyYHALkVBuo8tLUfEBudnMX3n0vMXRqboPGpoEW3TIoVlCZySE_DIqI0bh7QLIdqL0LwWOtFt7Owa8Vo2rjWm1dq41IRZnaulabvqv9gmU1R_PftZcbges9AEFDU3totQ1_XFnyXIhIPe4ojNZWFr0K2mKr0Vgff0YZZw8c8gtDCZro</recordid><startdate>20010530</startdate><enddate>20010530</enddate><creator>Chen, Jiann-Long</creator><creator>Al-Abed, Souhail R</creator><creator>Ryan, James A</creator><creator>Li, Zhenbin</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>C1K</scope><scope>SOI</scope><scope>7TV</scope></search><sort><creationdate>20010530</creationdate><title>Effects of pH on dechlorination of trichloroethylene by zero-valent iron</title><author>Chen, Jiann-Long ; Al-Abed, Souhail R ; Ryan, James A ; Li, Zhenbin</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c517t-a2d34e71a1e4f3cea1ca453488a42e6101dc473bdeb66da78172aa60cdab69df3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2001</creationdate><topic>Applied sciences</topic><topic>Chlorinated organics</topic><topic>Chlorine Compounds - chemistry</topic><topic>Earth sciences</topic><topic>Earth, ocean, space</topic><topic>Engineering and environment geology. Geothermics</topic><topic>Exact sciences and technology</topic><topic>Groundwaters</topic><topic>Hydrogen-Ion Concentration</topic><topic>Iron - chemistry</topic><topic>Iron corrosion</topic><topic>Natural water pollution</topic><topic>Organic Chemicals</topic><topic>Pollution</topic><topic>Pollution, environment geology</topic><topic>trichloroethylene</topic><topic>Trichloroethylene (TCE)</topic><topic>Trichloroethylene - chemistry</topic><topic>Water Pollution - prevention & control</topic><topic>Water treatment and pollution</topic><topic>Zero-valent iron (ZVI)</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Chen, Jiann-Long</creatorcontrib><creatorcontrib>Al-Abed, Souhail R</creatorcontrib><creatorcontrib>Ryan, James A</creatorcontrib><creatorcontrib>Li, Zhenbin</creatorcontrib><collection>Pascal-Francis</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Environment Abstracts</collection><collection>Pollution Abstracts</collection><jtitle>Journal of hazardous materials</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Chen, Jiann-Long</au><au>Al-Abed, Souhail R</au><au>Ryan, James A</au><au>Li, Zhenbin</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Effects of pH on dechlorination of trichloroethylene by zero-valent iron</atitle><jtitle>Journal of hazardous materials</jtitle><addtitle>J Hazard Mater</addtitle><date>2001-05-30</date><risdate>2001</risdate><volume>83</volume><issue>3</issue><spage>243</spage><epage>254</epage><pages>243-254</pages><issn>0304-3894</issn><eissn>1873-3336</eissn><coden>JHMAD9</coden><abstract>The surface normalized reaction rate constants (
k
sa) of trichloroethylene (TCE) and zero-valent iron (ZVI) were quantified in batch reactors at pH values between 1.7 and 10. The
k
sa of TCE linearly decreased from 0.044 to 0.009
l/h
m
2 between pH 3.8 and 8.0, whereas the
k
sa at pH 1.7 was more than an order higher than that at pH 3.8. The degradation of TCE was not observed at pH values of 9 and 10. The
k
sa of iron corrosion linearly decreased from 0.092 to 0.018
l/h
m
2 between pH 4.9 and 9.8, whereas it is significantly higher at pH 1.7 and 3.8. The
k
sa of TCE was 30–300 times higher than those reported in literature. The difference can be attributed to the pH effects and precipitation of iron hydroxide. The
k
sa of TCE degradation and iron corrosion at a head space of 6 and 10
ml were about twice of those at zero head space. The effect was attributed to the formation of hydrogen bubbles on ZVI, which hindered the transport the TCE between the solution and reaction sites on ZVI. The optimal TCE degradation rate was achieved at a pH of 4.9. This suggests that lowering solution pH might not expedite the degradation rate of TCE by ZVI as it also caused faster disappearance of ZVI, and hence decreased the ZVI surface concentration.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><pmid>11348735</pmid><doi>10.1016/S0304-3894(01)00193-5</doi><tpages>12</tpages></addata></record> |
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subjects | Applied sciences Chlorinated organics Chlorine Compounds - chemistry Earth sciences Earth, ocean, space Engineering and environment geology. Geothermics Exact sciences and technology Groundwaters Hydrogen-Ion Concentration Iron - chemistry Iron corrosion Natural water pollution Organic Chemicals Pollution Pollution, environment geology trichloroethylene Trichloroethylene (TCE) Trichloroethylene - chemistry Water Pollution - prevention & control Water treatment and pollution Zero-valent iron (ZVI) |
title | Effects of pH on dechlorination of trichloroethylene by zero-valent iron |
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