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  <titleInfo>
    <title>Syngas production via bi-reforming of methane using transition metal based catalysts</title>
  </titleInfo>
  <name type="personal">
    <namePart>Heng, Yee Phang</namePart>
    <role>
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    <dateIssued encoding="marc">2024</dateIssued>
    <copyrightDate encoding="marc">2024</copyrightDate>
    <issuance>monographic</issuance>
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  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
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  <physicalDescription>
    <extent>xv, 41 pages : illustrations ;</extent>
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  <abstract>Amidst global concerns over greenhouse gas emissions and fossil fuel depletion, the exploration of clean and sustainable energy became paramount. This research explored the field of methane bi-reforming, an innovative process that simultaneously produced syngas and reduced emissions of both methane and carbon dioxide. Catalyst deactivation in bi-reforming posed challenges, necessitating optimization for enhanced efficiency. This research priortized Ni and Co catalysts because of their balance between effectiveness and affordability. Hence, mono-metallic (Ni and Co) and bi-metallic (Ni-Co) were evaluated via bi-reforming of methane in this study. Three catalysts, 15%Ni/CeO2-CaO, 15%Co/CeO2-CaO and 7.5%Ni-7.5%Co/CeO2-CaO were synthesized using an ultrasonic impregnation-assisted technique and employed in bi-reforming of methane reaction for 8 hours. XRD, BET, SEM and TPO analysis were used to characterize the catalyst. Performance studies were conducted with different catalyst and temperature settings. In accordance with BET analysis, 7.5%Ni-7.5%Co/CeO2-CaO catalyst, possessing the largest surface area, demonstrated the greatest catalytic activity. The results from bi-reforming of methane reaction indicated 7.5%Ni-7.5%Co/CeO2-CaO catalyst displayed superior performance. This was evident in its high conversions, reaching 84% and 92% for CH4 and CO2 respectively, at a temperature of 800°C. Temperature variation experiments on the bi-metallic catalyst identified 900°C as optimal, achieving 91% CH4 conversion and 75% CO2 conversion. Unexpectedly, the high temperature resulting high ratio of H2/CO. This can be explained by the basic support provided by CeO2-CaO, facilitating the adsorption of CO2 while preventing reverse water gas shift reaction from producing CO. Post-reaction XRD on the spent catalyst at 800°C revealed crystalline graphite structures associated with carbon deposition while a lower degree of graphitization at lower temperatures. TPO analysis demonstrated that the bi-metallic catalyst had a high catalytic activity by showing significant amount of graphitic carbon had been deposited on its surface.</abstract>
  <targetAudience authority="marctarget">specialized</targetAudience>
  <note type="statement of responsibility">Heng Yee Phang</note>
  <note>Faculty of Chemical and Process Engineering Technology</note>
  <note>Final Year Report (Bachelor of Chemical Engineering ) -- Universiti Malaysia Pahang Al-Sultan Abdullah - 2024</note>
  <note>Include bibliographical reference</note>
  <subject authority="lcsh">
    <name type="corporate">
      <namePart>Faculty of Chemical and Process Engineering Technology</namePart>
    </name>
    <topic>Dissertations</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Universities and colleges</topic>
    <topic>Dissertations</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Theses</topic>
    <topic>Dissertations</topic>
  </subject>
  <identifier type="isbn">THE0010600 (Local)</identifier>
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    <recordCreationDate encoding="marc">260612</recordCreationDate>
    <recordChangeDate encoding="iso8601">20260612122245.0</recordChangeDate>
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      <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
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