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        <identifier>oai:www.ideals.illinois.edu:2142/83208</identifier>
        <datestamp>2023-07-11</datestamp>
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        <thesis xmlns="http://www.ndltd.org/standards/metadata/etdms/1.1/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:dc="http://purl.org/dc/elements/1.1/" xsi:schemaLocation="http://www.ndltd.org/standards/metadata/etdms/1.1/ http://www.ndltd.org/standards/metadata/etdms/1.1/etdms11.xsd http://purl.org/dc/elements/1.1/ http://www.ndltd.org/standards/metadata/etdms/1.1/etdmsdc.xsd">
          <dc:contributor>Rood, Mark J.</dc:contributor>
          <dc:creator>Sullivan, Patrick D.</dc:creator>
          <dc:date>2015-09-25T21:03:34Z</dc:date>
          <dc:date>2015-09-25T21:03:34Z</dc:date>
          <dc:date>10000-01-01</dc:date>
          <dc:date>2003</dc:date>
          <dc:date>2003</dc:date>
          <dc:description>This research developed a new air quality control technology that captures and recovers solvents for reuse in the process that generated the pollutants. This adsorption-based technology integrates the unique properties of Activated Carbon Fiber Cloth (ACFC), a high-performance micro-engineered adsorbent, with rapid in-situ Electrothermal Desorption (ED). ED regenerates the adsorbent by efficient electrical resistance heating. A unique aspect of this technology is that adsorbate readily condenses inside the adsorption vessel and is recovered as a pure liquid with only passive cooling during the regeneration of the ACFC. Such feature eliminates the need for auxiliary unit operations to treat the effluent that is generated during regeneration. A new adsorber configuration was also developed, with the ACFC arranged in multiple annular-shaped cartridges. Equilibrium adsorption isotherm data were also generated while alternating current was passing through the ACFC and at temperatures above the boiling point of the adsorbate. Solid-gas equilibria were shown to be accurately represented by the Dubinin-Radushkevich (DR) equation. A one-dimensional, homogenous, non-adiabatic model for the ED process was developed, which predicts the energy consumption and adsorbate mass recovery to within 7% of the experimental results. This new capture-and-recovery technology is cost-competitive, and can be used in situations where no current technology is practical.</dc:description>
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  Previous issue date: 2003</dc:description>
          <dc:description>Embargo set by: Seth Robbins for item 84489
Lift date: Forever
Reason: Restricted to the U of I community idenfinitely during batch ingest of legacy ETDs</dc:description>
          <dc:description>Restricted to the U of I community idenfinitely during batch ingest of legacy ETDs</dc:description>
          <dc:description>U of I Only</dc:description>
          <dc:description>118 p.</dc:description>
          <dc:description>Thesis (Ph.D.)--University of Illinois at Urbana-Champaign, 2003.</dc:description>
          <dc:identifier>http://hdl.handle.net/2142/83208</dc:identifier>
          <dc:identifier>(MiAaPQ)AAI3086194</dc:identifier>
          <dc:language>eng</dc:language>
          <dc:subject>Engineering, Chemical</dc:subject>
          <dc:title>Organic Vapor Recovery Using Activated Carbon Fiber Cloth and Electrothermal Desorption</dc:title>
          <dc:type>text</dc:type>
          <degree>
            <department>Civil and Environmental Engineering</department>
            <discipline>Civil and Environmental Engineering</discipline>
            <grantor>University of Illinois at Urbana-Champaign</grantor>
            <level>Dissertation</level>
            <name>Ph.D.</name>
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