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Copper-Doped Silica Materials Silanized With Bis-(Triethoxy Silyl Propyl)-Tetra Sulfide for Mercury Vapor Capture
The use of Cu−S sites for Hg capture from the gas phase has been successfully applied to a silica-based platform using an S4 organic polysulfane and copper sulfate. The maximum fixed-bed equilibrium capacity achieved using these materials was 19 789 μg Hg·g−1 sorbent for a material with 2.5 wt % Cu...
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Published in: | Energy & fuels 2008-07, Vol.22 (4), p.2290-2298 |
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creator | Meyer, D. E Meeks, N Sikdar, S Hutson, N. D Hua, D Bhattacharyya, D |
description | The use of Cu−S sites for Hg capture from the gas phase has been successfully applied to a silica-based platform using an S4 organic polysulfane and copper sulfate. The maximum fixed-bed equilibrium capacity achieved using these materials was 19 789 μg Hg·g−1 sorbent for a material with 2.5 wt % Cu and 6 wt % S. An optimal S level was determined to be around 3 wt % because enhancement of capacity was only 18% when increasing from this 3 to 6 wt %. The rate of adsorption in pure beds ranged from 0.6 to 1.6 μg Hg·min−1 depending on the inlet concentration. Differences in breakthrough times suggest that material deposition is not uniform. When compared to two other platforms, commercially available Darco HG-LH and previously tested Fe−Cu−S4 nanoaggregates, the Si-1 material performed the best in fixed-bed testing. During entrained-flow testing, a steady-state Hg removal of 82% was achieved using Si-1 at injection rates of both 6 × 10−5 and 1.2 × 10−4 g·L−1·h−1. The lack of increase in Hg removal when the injection rate is doubled suggests that pore accessibility is the rate-controlling step during dynamic Hg capture. A calculation of the approximate pore usage based on injection testing helped confirm this observation. During injection testing, the performance of Si-1 was only diminished 10% when exposed to 20 ppm SO3. This is an encouraging result for flue-gas applications where SO3 levels range from 1 to 40 ppm. Testing demonstrated that Si-1 is stable when exposed to leaching conditions after concrete blending and cement impregnation. This is an important aspect to consider for injection because the sale of fly ash for concrete is a key cost-recovery tool for power plants. |
doi_str_mv | 10.1021/ef8001873 |
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E ; Meeks, N ; Sikdar, S ; Hutson, N. D ; Hua, D ; Bhattacharyya, D</creator><creatorcontrib>Meyer, D. E ; Meeks, N ; Sikdar, S ; Hutson, N. D ; Hua, D ; Bhattacharyya, D</creatorcontrib><description>The use of Cu−S sites for Hg capture from the gas phase has been successfully applied to a silica-based platform using an S4 organic polysulfane and copper sulfate. The maximum fixed-bed equilibrium capacity achieved using these materials was 19 789 μg Hg·g−1 sorbent for a material with 2.5 wt % Cu and 6 wt % S. An optimal S level was determined to be around 3 wt % because enhancement of capacity was only 18% when increasing from this 3 to 6 wt %. The rate of adsorption in pure beds ranged from 0.6 to 1.6 μg Hg·min−1 depending on the inlet concentration. Differences in breakthrough times suggest that material deposition is not uniform. When compared to two other platforms, commercially available Darco HG-LH and previously tested Fe−Cu−S4 nanoaggregates, the Si-1 material performed the best in fixed-bed testing. During entrained-flow testing, a steady-state Hg removal of 82% was achieved using Si-1 at injection rates of both 6 × 10−5 and 1.2 × 10−4 g·L−1·h−1. The lack of increase in Hg removal when the injection rate is doubled suggests that pore accessibility is the rate-controlling step during dynamic Hg capture. A calculation of the approximate pore usage based on injection testing helped confirm this observation. During injection testing, the performance of Si-1 was only diminished 10% when exposed to 20 ppm SO3. This is an encouraging result for flue-gas applications where SO3 levels range from 1 to 40 ppm. Testing demonstrated that Si-1 is stable when exposed to leaching conditions after concrete blending and cement impregnation. This is an important aspect to consider for injection because the sale of fly ash for concrete is a key cost-recovery tool for power plants.</description><identifier>ISSN: 0887-0624</identifier><identifier>EISSN: 1520-5029</identifier><identifier>DOI: 10.1021/ef8001873</identifier><identifier>CODEN: ENFUEM</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>01 COAL, LIGNITE, AND PEAT ; ADSORBENTS ; ADSORPTION ; Air pollution caused by fuel industries ; AIR POLLUTION CONTROL ; Applied sciences ; CAPTURE ; COPPER ; Energy ; Energy. 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E</creatorcontrib><creatorcontrib>Meeks, N</creatorcontrib><creatorcontrib>Sikdar, S</creatorcontrib><creatorcontrib>Hutson, N. D</creatorcontrib><creatorcontrib>Hua, D</creatorcontrib><creatorcontrib>Bhattacharyya, D</creatorcontrib><title>Copper-Doped Silica Materials Silanized With Bis-(Triethoxy Silyl Propyl)-Tetra Sulfide for Mercury Vapor Capture</title><title>Energy & fuels</title><addtitle>Energy Fuels</addtitle><description>The use of Cu−S sites for Hg capture from the gas phase has been successfully applied to a silica-based platform using an S4 organic polysulfane and copper sulfate. The maximum fixed-bed equilibrium capacity achieved using these materials was 19 789 μg Hg·g−1 sorbent for a material with 2.5 wt % Cu and 6 wt % S. An optimal S level was determined to be around 3 wt % because enhancement of capacity was only 18% when increasing from this 3 to 6 wt %. The rate of adsorption in pure beds ranged from 0.6 to 1.6 μg Hg·min−1 depending on the inlet concentration. Differences in breakthrough times suggest that material deposition is not uniform. When compared to two other platforms, commercially available Darco HG-LH and previously tested Fe−Cu−S4 nanoaggregates, the Si-1 material performed the best in fixed-bed testing. During entrained-flow testing, a steady-state Hg removal of 82% was achieved using Si-1 at injection rates of both 6 × 10−5 and 1.2 × 10−4 g·L−1·h−1. The lack of increase in Hg removal when the injection rate is doubled suggests that pore accessibility is the rate-controlling step during dynamic Hg capture. A calculation of the approximate pore usage based on injection testing helped confirm this observation. During injection testing, the performance of Si-1 was only diminished 10% when exposed to 20 ppm SO3. This is an encouraging result for flue-gas applications where SO3 levels range from 1 to 40 ppm. Testing demonstrated that Si-1 is stable when exposed to leaching conditions after concrete blending and cement impregnation. This is an important aspect to consider for injection because the sale of fly ash for concrete is a key cost-recovery tool for power plants.</description><subject>01 COAL, LIGNITE, AND PEAT</subject><subject>ADSORBENTS</subject><subject>ADSORPTION</subject><subject>Air pollution caused by fuel industries</subject><subject>AIR POLLUTION CONTROL</subject><subject>Applied sciences</subject><subject>CAPTURE</subject><subject>COPPER</subject><subject>Energy</subject><subject>Energy. Thermal use of fuels</subject><subject>Environmental</subject><subject>Exact sciences and technology</subject><subject>FLUE GAS</subject><subject>MERCURY</subject><subject>Pollution reduction</subject><subject>SILANES</subject><subject>SILICA</subject><subject>SORBENT INJECTION PROCESSES</subject><issn>0887-0624</issn><issn>1520-5029</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2008</creationdate><recordtype>article</recordtype><recordid>eNptkEFv1DAQhSMEEkvhwD-IhED0ELAd24mPsNCC1IWiXcrRGuyx1iWNU9uRuv31eLXVcuE0mnnfvNG8qnpJyTtKGH2PrieE9l37qFpQwUgjCFOPqwXp-64hkvGn1bOUrgkhsu3ForpdhmnC2HwKE9p67QdvoF5BxuhhSPsBjP6-SL983tYffWrebqLHvA13u726G-rLGKbdcNpsMEeo1_PgvMXahVivMJo57uormEq3hCnPEZ9XT1yxxhcP9aT6efZ5s_zSXHw__7r8cNFA28vc9CAVU045IVVLFf0NRnXGgmglt8Ky3oJizhoiOBPWthIodtRyYTsLzmJ7Ur06-IaUvU7GZzRbE8YRTdaMkp4rTgv15kBNMdzOmLK-8cngUN7GMCfNSnBcCVnA0wNoYkgpotNT9DcQd5oSvY9eH6Mv7OsHU0gGBhdhND4dFxgRVLWcF645cD5lvDvqEP9o2bWd0JvLtearbiXPv13pH_98wSR9HeY4lgD_c_8vS5-eEQ</recordid><startdate>20080701</startdate><enddate>20080701</enddate><creator>Meyer, D. 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E</creatorcontrib><creatorcontrib>Meeks, N</creatorcontrib><creatorcontrib>Sikdar, S</creatorcontrib><creatorcontrib>Hutson, N. D</creatorcontrib><creatorcontrib>Hua, D</creatorcontrib><creatorcontrib>Bhattacharyya, D</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Pollution Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>OSTI.GOV</collection><jtitle>Energy & fuels</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Meyer, D. E</au><au>Meeks, N</au><au>Sikdar, S</au><au>Hutson, N. D</au><au>Hua, D</au><au>Bhattacharyya, D</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Copper-Doped Silica Materials Silanized With Bis-(Triethoxy Silyl Propyl)-Tetra Sulfide for Mercury Vapor Capture</atitle><jtitle>Energy & fuels</jtitle><addtitle>Energy Fuels</addtitle><date>2008-07-01</date><risdate>2008</risdate><volume>22</volume><issue>4</issue><spage>2290</spage><epage>2298</epage><pages>2290-2298</pages><issn>0887-0624</issn><eissn>1520-5029</eissn><coden>ENFUEM</coden><abstract>The use of Cu−S sites for Hg capture from the gas phase has been successfully applied to a silica-based platform using an S4 organic polysulfane and copper sulfate. The maximum fixed-bed equilibrium capacity achieved using these materials was 19 789 μg Hg·g−1 sorbent for a material with 2.5 wt % Cu and 6 wt % S. An optimal S level was determined to be around 3 wt % because enhancement of capacity was only 18% when increasing from this 3 to 6 wt %. The rate of adsorption in pure beds ranged from 0.6 to 1.6 μg Hg·min−1 depending on the inlet concentration. Differences in breakthrough times suggest that material deposition is not uniform. When compared to two other platforms, commercially available Darco HG-LH and previously tested Fe−Cu−S4 nanoaggregates, the Si-1 material performed the best in fixed-bed testing. During entrained-flow testing, a steady-state Hg removal of 82% was achieved using Si-1 at injection rates of both 6 × 10−5 and 1.2 × 10−4 g·L−1·h−1. The lack of increase in Hg removal when the injection rate is doubled suggests that pore accessibility is the rate-controlling step during dynamic Hg capture. A calculation of the approximate pore usage based on injection testing helped confirm this observation. During injection testing, the performance of Si-1 was only diminished 10% when exposed to 20 ppm SO3. This is an encouraging result for flue-gas applications where SO3 levels range from 1 to 40 ppm. Testing demonstrated that Si-1 is stable when exposed to leaching conditions after concrete blending and cement impregnation. This is an important aspect to consider for injection because the sale of fly ash for concrete is a key cost-recovery tool for power plants.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ef8001873</doi><tpages>9</tpages></addata></record> |
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subjects | 01 COAL, LIGNITE, AND PEAT ADSORBENTS ADSORPTION Air pollution caused by fuel industries AIR POLLUTION CONTROL Applied sciences CAPTURE COPPER Energy Energy. Thermal use of fuels Environmental Exact sciences and technology FLUE GAS MERCURY Pollution reduction SILANES SILICA SORBENT INJECTION PROCESSES |
title | Copper-Doped Silica Materials Silanized With Bis-(Triethoxy Silyl Propyl)-Tetra Sulfide for Mercury Vapor Capture |
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