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  <titleInfo>
    <title>Esterification of octanoic acid and ethanol using sulfated zirconia in the presence of triglycerides</title>
    <subTitle>kinetic and modelling study</subTitle>
  </titleInfo>
  <titleInfo type="alternative">
    <title>Esterification of octanoic acid and ethanol using sulfated zirconia in the presence of triglycerides</title>
    <subTitle>kinetic and modelling study</subTitle>
  </titleInfo>
  <name type="personal">
    <namePart>Bryan Lester Binar</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, Pahang</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">computer file</form>
    <extent>57 p. : ill. (some col.) ; 30 cm. + 1 computer disc</extent>
  </physicalDescription>
  <abstract>The  esterification  of  octanoic  acid  and  ethanol  using  sulfated  zirconia  in  the presence of  triglycerides  is one of  the methods  to produce biodiesel. As  the  fuel used today, petroleum is estimated depleted around 30-45 years in the future, Biodiesel is an alternative biofuel that can be produced using esterification method. The esterification of octanoic acid is done to determine the best operation condition to yield better conversion of  octanoic  acid.  The  operation  conditions  for  the  esterification  of  octanoic  acid  are temperature  of  reaction,  amount  of  sulfated  zirconia  used,  amount  of  triglycerides presence and molar ratio of octanoic acid to ethanol. The temperature of reaction ranged from 30ºC to 50ºC. The amount of sulfated zirconia used ranged from 0.5g to 1.5g. The amount of triglycerides presence ranged from 30ml to 70ml. The molar ratio of octanoic acid  to  ethanol  ranged  to  1:1  to  1:5.  The  best  operating  condition  achieved  for  the esterification of octanoic acid and ethanol were 30ºC reaction temperature, 1.5g sulfated zirconia  used,  1:1  molar  ratio  of  octanoic  acid  to  ethanol  and  50ml  of  triglycerides presence  in  the  esterification.  The  kinetic  model  been  used  is  pseudo-homogeneous kinectic model based on the experimental data gained. The pseudo-homogeneous kinetic model gives a good agreement between the experimental data and the model used.</abstract>
  <targetAudience authority="marctarget">specialized</targetAudience>
  <note type="statement of responsibility">Bryan Lester Binar</note>
  <note>Project paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang - 2009</note>
  <note>Bibiliography : p. 45-47</note>
  <subject authority="lcsh">
    <topic>Biodiesel fuels</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Triglyceride</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Esterification</topic>
  </subject>
  <identifier type="isbn">THE0004599(Local)</identifier>
  <recordInfo>
    <recordContentSource authority="marcorg">UMP</recordContentSource>
    <recordCreationDate encoding="marc">100218</recordCreationDate>
    <recordChangeDate encoding="iso8601">20251114204458.0</recordChangeDate>
    <recordIdentifier source="KUKTEM">vtls000045125</recordIdentifier>
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