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  <titleInfo>
    <title>Production of mixed-matrix membrane (psf/zeolite) for co2 / n2 separation</title>
    <subTitle>screening study of polymer concentration</subTitle>
  </titleInfo>
  <name type="personal">
    <namePart>Chen, Chee Lek</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <typeOfResource manuscript="yes">text</typeOfResource>
  <genre authority="marc">theses</genre>
  <originInfo>
    <place>
      <placeTerm type="code" authority="marccountry">my</placeTerm>
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    <place>
      <placeTerm type="text">Kuantan, Pahang</placeTerm>
    </place>
    <publisher>UMP</publisher>
    <dateIssued>2014</dateIssued>
    <issuance>monographic</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
    <form authority="marcform">print</form>
    <extent>xvii, 84 p. : ill. ; 30 cm. + 1 CD-ROM</extent>
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  <abstract>This research investigated the permeability of CO2 and N2 as well as selectivity of CO2  over N2 of polysulfone (PSF) mixed matrix membranes filled with zeolite 4Å particles.  The mixed matrix membrane was prepared by immersion precipitation method with  zeolite and PSf were ranged from 10 to 30 W/V% dissolved in the NMP varied from 75  to 100 cm3. The mixture was then mixed homogenously and utilized to determine the  permeation rates of N2 and CO2. It is characterized by FTIR and the gas separation  performance is analysed by Design of Expert (DOE) method. In accordance to our  expectation, FTIR results revealed that the intensity at 3596.17 cm−1 described the  existence of an interaction between polymer and zeolite. The permeability of CO2  through the membrane was in higher range from 9.873 to 11.641 GPU. At lower  operating pressure, the greater solubility of gas encourages a higher permeation rate.  The single concentration variable has low effect, however the interaction between PSf  and NMP (BC) has considerable effect on the permeability of CO2 with the highest F  value of 0.46. NMP exhibited a high degree of polarity and hydrogen bonding which led  to effect of selective skin and permeation rate. The more solvent evaporated, the thicker  the concentrated polymer region which then leads to a thicker selective skin and a  reduction in permeation rate. The interaction of zeolite and PSf had the least significant  effect on the selectivity of CO2 over N2 due to the lower F value with 0.023, however  the interaction had higher permeability of CO2 with the F value of 0.45. The cause of  low permeability of CO2 was poor association between the zeolite and the polymer  leading to an increased in free volume within the membrane. Although it enhanced the  permeability of CO2, but it limited the sieving mechanism which resulted low selectivity  of CO2 over N2. The model regression equations were evaluated by F-test ANOVA  which revealed that these regressions are statistically significant at 95% confidence level  to screening the permeability of CO2 and N2 as well as selectivity of CO2/N2. In future  research, optimisation is proposed based on the screening study of PSf and zeolite  concentration ranged from 22.30 to 27.45 W/V% to stress on the high permeability and  selectivity CO2/N2 separation membranes</abstract>
  <targetAudience authority="marctarget">specialized</targetAudience>
  <note type="statement of responsibility">Chen Chee Lek</note>
  <note>Faculty of Chemical &amp; Natural Resources Engineering</note>
  <note>Project paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang – 2014</note>
  <note>Bibliography : p. 65-84</note>
  <subject authority="lcsh">
    <topic>Carbon dioxide</topic>
  </subject>
  <identifier type="isbn">THE0004567(Local)</identifier>
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    <recordCreationDate encoding="marc">150115</recordCreationDate>
    <recordChangeDate encoding="iso8601">20251117113236.0</recordChangeDate>
    <recordIdentifier source="KUKTEM">vtls000084888</recordIdentifier>
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