Serial ozone/peroxide/low pressure UV treatment for synergistic and effective organic micropollutant conversion
Serial ozone/peroxide/low pressure UV was tested for an advanced oxidation process (AOP) application on pre-treated surface water in a pilot plant. The pilot plant consisted of an ozone loop reactor followed by a low pressure UV (LP-UV) reactor. Fourteen model compounds and 6 or 10ppm hydrogen perox...
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description | Serial ozone/peroxide/low pressure UV was tested for an advanced oxidation process (AOP) application on pre-treated surface water in a pilot plant. The pilot plant consisted of an ozone loop reactor followed by a low pressure UV (LP-UV) reactor. Fourteen model compounds and 6 or 10ppm hydrogen peroxide were dosed to the water. Ozone doses varied from 0.5 to 2.0g/m3 and UV doses varied, depending on the UV transmission (73–83%) of the water, between 700 and 950mJ/cm2. The treatment process was evaluated on bromate formation, compound conversion and energy demand. The bromate formation during the O3/H2O2 process was kept lower than 0.5μg/L by using a peroxide dose of 6ppm and an ozone dose of 1.5mg/L. With a 1.5mg/L ozone dose and 6ppm of peroxide, 8 out of 14 compounds were converted by more than 90% with an energy consumption of 0.027kWh/m3. During the subsequent UV/H2O2, the EEO for atrazine was 0.52kWh/m3; together with the O3/H2O2, the EEO for serial AOP was 0.55kWh/m3, which was 0.73kWh/m3 for UV/H2O2 only. During O3/H2O2 treatment, the DOC decreased with 0.2mg/L and the UV-T254 increased with almost 5%, illustrating the synergistic effect of serial AOP. When 3 UV reactors in series were used, with each reactor dosing 1/3 of the total dose, the total conversion increased 5–15%. |
doi_str_mv | 10.1016/j.seppur.2012.08.030 |
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The pilot plant consisted of an ozone loop reactor followed by a low pressure UV (LP-UV) reactor. Fourteen model compounds and 6 or 10ppm hydrogen peroxide were dosed to the water. Ozone doses varied from 0.5 to 2.0g/m3 and UV doses varied, depending on the UV transmission (73–83%) of the water, between 700 and 950mJ/cm2. The treatment process was evaluated on bromate formation, compound conversion and energy demand. The bromate formation during the O3/H2O2 process was kept lower than 0.5μg/L by using a peroxide dose of 6ppm and an ozone dose of 1.5mg/L. With a 1.5mg/L ozone dose and 6ppm of peroxide, 8 out of 14 compounds were converted by more than 90% with an energy consumption of 0.027kWh/m3. During the subsequent UV/H2O2, the EEO for atrazine was 0.52kWh/m3; together with the O3/H2O2, the EEO for serial AOP was 0.55kWh/m3, which was 0.73kWh/m3 for UV/H2O2 only. During O3/H2O2 treatment, the DOC decreased with 0.2mg/L and the UV-T254 increased with almost 5%, illustrating the synergistic effect of serial AOP. When 3 UV reactors in series were used, with each reactor dosing 1/3 of the total dose, the total conversion increased 5–15%.</description><identifier>ISSN: 1383-5866</identifier><identifier>EISSN: 1873-3794</identifier><identifier>DOI: 10.1016/j.seppur.2012.08.030</identifier><language>eng</language><publisher>Kidlington: Elsevier B.V</publisher><subject>Advanced oxidation process ; Applied sciences ; atrazine ; Bromate ; Bromates ; Chemical engineering ; Continental surface waters ; Conversion ; energy conversion ; Exact sciences and technology ; hydrogen peroxide ; Low pressure ; Low pressure UV ; Natural water pollution ; oxidation ; Ozone ; Peroxide ; Peroxides ; Pilot plants ; Pollution ; Reactors ; Serials ; surface water ; synergism ; Water treatment and pollution</subject><ispartof>Separation and purification technology, 2012-10, Vol.100, p.22-29</ispartof><rights>2012 Elsevier B.V.</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c393t-94da5f7e0f3d187b440c16233abb323894c354df094c989c42d7df5f2ce4fc693</citedby><cites>FETCH-LOGICAL-c393t-94da5f7e0f3d187b440c16233abb323894c354df094c989c42d7df5f2ce4fc693</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S1383586612004625$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=26569238$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Lekkerkerker-Teunissen, K.</creatorcontrib><creatorcontrib>Knol, A.H.</creatorcontrib><creatorcontrib>van Altena, L.P.</creatorcontrib><creatorcontrib>Houtman, C.J.</creatorcontrib><creatorcontrib>Verberk, J.Q.J.C.</creatorcontrib><creatorcontrib>van Dijk, J.C.</creatorcontrib><title>Serial ozone/peroxide/low pressure UV treatment for synergistic and effective organic micropollutant conversion</title><title>Separation and purification technology</title><description>Serial ozone/peroxide/low pressure UV was tested for an advanced oxidation process (AOP) application on pre-treated surface water in a pilot plant. The pilot plant consisted of an ozone loop reactor followed by a low pressure UV (LP-UV) reactor. Fourteen model compounds and 6 or 10ppm hydrogen peroxide were dosed to the water. Ozone doses varied from 0.5 to 2.0g/m3 and UV doses varied, depending on the UV transmission (73–83%) of the water, between 700 and 950mJ/cm2. The treatment process was evaluated on bromate formation, compound conversion and energy demand. The bromate formation during the O3/H2O2 process was kept lower than 0.5μg/L by using a peroxide dose of 6ppm and an ozone dose of 1.5mg/L. With a 1.5mg/L ozone dose and 6ppm of peroxide, 8 out of 14 compounds were converted by more than 90% with an energy consumption of 0.027kWh/m3. During the subsequent UV/H2O2, the EEO for atrazine was 0.52kWh/m3; together with the O3/H2O2, the EEO for serial AOP was 0.55kWh/m3, which was 0.73kWh/m3 for UV/H2O2 only. During O3/H2O2 treatment, the DOC decreased with 0.2mg/L and the UV-T254 increased with almost 5%, illustrating the synergistic effect of serial AOP. When 3 UV reactors in series were used, with each reactor dosing 1/3 of the total dose, the total conversion increased 5–15%.</description><subject>Advanced oxidation process</subject><subject>Applied sciences</subject><subject>atrazine</subject><subject>Bromate</subject><subject>Bromates</subject><subject>Chemical engineering</subject><subject>Continental surface waters</subject><subject>Conversion</subject><subject>energy conversion</subject><subject>Exact sciences and technology</subject><subject>hydrogen peroxide</subject><subject>Low pressure</subject><subject>Low pressure UV</subject><subject>Natural water pollution</subject><subject>oxidation</subject><subject>Ozone</subject><subject>Peroxide</subject><subject>Peroxides</subject><subject>Pilot plants</subject><subject>Pollution</subject><subject>Reactors</subject><subject>Serials</subject><subject>surface water</subject><subject>synergism</subject><subject>Water treatment and pollution</subject><issn>1383-5866</issn><issn>1873-3794</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><recordid>eNp9kU2LFDEQhhtRcF39B4K5CF66J5_d6Ysgi1-w4GEdryGTVIYMPUlb6R5df71ZevHoKUV4qvLWk6Z5zWjHKOt3p67APK_Yccp4R3VHBX3SXDE9iFYMo3xaa6FFq3TfP29elHKilA1M86sm3wFGO5H8JyfYzYD5d_Swm_IvMiOUsiKQ_Q-yINjlDGkhISMp9wnwGMsSHbHJEwgB3BIvQDIebaq35-gwz3ma1sXWJpfTBbDEnF42z4KdCrx6PK-b_aeP32--tLffPn-9-XDbOjGKpR2ltyoMQIPwdY2DlNSxngthDwfBhR6lE0r6QGsx6tFJ7gcfVOAOZHD9KK6bd9vcGfPPFcpizrE4mCabIK_FMM6Z1mqgqqJyQ2vkUhCCmTGeLd4bRs2DX3Mym1_z4NdQbarf2vb28QVbnJ0C2uRi-dfLe9WPNWnl3mxcsNnYI1Zmf1cHqfoHnCvKK_F-I6AKuURAU1yE5MBHrF6Nz_H_Uf4Cb5ye_Q</recordid><startdate>20121024</startdate><enddate>20121024</enddate><creator>Lekkerkerker-Teunissen, K.</creator><creator>Knol, A.H.</creator><creator>van Altena, L.P.</creator><creator>Houtman, C.J.</creator><creator>Verberk, J.Q.J.C.</creator><creator>van Dijk, J.C.</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>FBQ</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SU</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>JG9</scope></search><sort><creationdate>20121024</creationdate><title>Serial ozone/peroxide/low pressure UV treatment for synergistic and effective organic micropollutant conversion</title><author>Lekkerkerker-Teunissen, K. ; 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The pilot plant consisted of an ozone loop reactor followed by a low pressure UV (LP-UV) reactor. Fourteen model compounds and 6 or 10ppm hydrogen peroxide were dosed to the water. Ozone doses varied from 0.5 to 2.0g/m3 and UV doses varied, depending on the UV transmission (73–83%) of the water, between 700 and 950mJ/cm2. The treatment process was evaluated on bromate formation, compound conversion and energy demand. The bromate formation during the O3/H2O2 process was kept lower than 0.5μg/L by using a peroxide dose of 6ppm and an ozone dose of 1.5mg/L. With a 1.5mg/L ozone dose and 6ppm of peroxide, 8 out of 14 compounds were converted by more than 90% with an energy consumption of 0.027kWh/m3. During the subsequent UV/H2O2, the EEO for atrazine was 0.52kWh/m3; together with the O3/H2O2, the EEO for serial AOP was 0.55kWh/m3, which was 0.73kWh/m3 for UV/H2O2 only. During O3/H2O2 treatment, the DOC decreased with 0.2mg/L and the UV-T254 increased with almost 5%, illustrating the synergistic effect of serial AOP. When 3 UV reactors in series were used, with each reactor dosing 1/3 of the total dose, the total conversion increased 5–15%.</abstract><cop>Kidlington</cop><pub>Elsevier B.V</pub><doi>10.1016/j.seppur.2012.08.030</doi><tpages>8</tpages></addata></record> |
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subjects | Advanced oxidation process Applied sciences atrazine Bromate Bromates Chemical engineering Continental surface waters Conversion energy conversion Exact sciences and technology hydrogen peroxide Low pressure Low pressure UV Natural water pollution oxidation Ozone Peroxide Peroxides Pilot plants Pollution Reactors Serials surface water synergism Water treatment and pollution |
title | Serial ozone/peroxide/low pressure UV treatment for synergistic and effective organic micropollutant conversion |
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