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  <titleInfo>
    <title>Concentration of biopetrol synthesized from oleic acid through catalytic cracking using zeolite as catalyst</title>
  </titleInfo>
  <titleInfo type="alternative">
    <title>Concentration of biopetrol synthesized from oleic acid through catalytic cracking using zeolite as catalyst</title>
  </titleInfo>
  <name type="personal">
    <namePart>Nurul Liana Abd Rahman</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <typeOfResource>text</typeOfResource>
  <genre authority="marc">theses</genre>
  <originInfo>
    <place>
      <placeTerm type="code" authority="marccountry">my</placeTerm>
    </place>
    <place>
      <placeTerm type="text">Kuantan</placeTerm>
    </place>
    <publisher>UMP</publisher>
    <dateIssued>2009</dateIssued>
    <issuance>monographic</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
    <form authority="marcform">print</form>
    <form authority="gmd">electronic resource</form>
    <extent>95 p. : ill. (some col.) ; 30 cm. + 1 computer disc</extent>
  </physicalDescription>
  <abstract>Oleic acid is one of the major fatty acid in vegetable oil. In this research, zeolite catalysts  are  used  over  the  conversion  of  oleic  acid  into  isooctane  as  the  future biopetrol in a heating mantle at atmospheric pressure. The main purposed of studies is to improve the concentration of isooctane using catalytic cracking method. The effect of various amount of Zeolite catalyst at 1g, 5g, 10g and 20g and various dilution factor of isooctane to hexane at 1%, 5%, 10% and 20% are studied over the yield of biopetrol at 98o C. Gas chromatography is used for the qualitative and quantitative analysis of the  samples.  Backward  calculation  is  applied  to  calculate  the  actual  concentration  of isooctane in the distilled oleic acid. The maximum yield of desired isooctane obtained at  20g  of  catalyst  and  dilution  of  20%  isooctane  to  hexane  is  recorded  at  7.89%. Experimental  works  has  successful  show  that  catalytic  cracking  is  greater  in conversion than thermal cracking.</abstract>
  <targetAudience authority="marctarget">specialized</targetAudience>
  <note type="statement of responsibility">Nurul Liana Bte Abd Rahman</note>
  <note>Project paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang – 2009</note>
  <subject authority="lcsh">
    <topic>Oleic acid</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Ethylhexanol</topic>
  </subject>
  <identifier type="isbn">THE0002123(Local)</identifier>
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    <recordContentSource authority="marcorg">UMP</recordContentSource>
    <recordCreationDate encoding="marc">100219</recordCreationDate>
    <recordChangeDate encoding="iso8601">20251114204452.0</recordChangeDate>
    <recordIdentifier source="KUKTEM">vtls000045146</recordIdentifier>
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