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  <titleInfo>
    <title>Performance of crossflow microfiltration</title>
    <subTitle>models and experiments</subTitle>
  </titleInfo>
  <name type="personal">
    <namePart>Pandey, Janardan Raj</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
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  <name type="personal">
    <namePart>Vigneswaran, Saravanamuthu</namePart>
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  <name type="personal">
    <namePart> Hanaki, K.</namePart>
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      <roleTerm type="text">Examination Committee</roleTerm>
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  <name type="personal">
    <namePart>Shin, H. S.</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>Danish International Development Agency  (DANIDA)</namePart>
    <role>
      <roleTerm type="text">Scholarhship Donor</roleTerm>
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  <originInfo>
    <place>
      <placeTerm type="text">Bangkok</placeTerm>
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    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1987</dateIssued>
    <issuance>monographic</issuance>
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  <language>
    <languageTerm authority="iso639-2b" type="code">En</languageTerm>
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  <abstract>Crossflow microfiltration is a pressure driven membrane process  in which the fluid to be filtered flows parallel to the membrane  surface, which reduces the formation of filter cake allowing better  permeate flow.  Laboratory-scale microfiltration experiments with kaolin clay  and latex suspension were carried out to study the membrane filter  performance with respect to operating parameters. The operating  parameters choosen were membrane pore size , particle size , particle  concentration, crossflow velocity and applied pressure. It was found  that clogging in the membrane occurs fast in case of bigger membrane  pore size and finer particles. Also the existence of a optimum crossflow  velocity (for which the filtration rate is maximum) was noticed . This  filtration rate could be increased by increasing the module entrance  pressure . The filtrate quality continued improving as the filtration  proceeds.  In this study, a mathematical model was formulated to predict  the filtrate efficiency of the membrane filter. The developed model , was  verified with the laboratory-scale experiments. The filtrate efficiency  predicted by t his model differed from that of experimental value as t he  assumptions made in t he development of model were suitable only for  ideal cases.  Also an empirical model to correlate the membrane fouling of  different pore sizes was found. A standard curve was developed between  percentage of pores blocked and total solids deposited on the membrane,  to predict the fouling of t he membrane of different pore sizes which may  be useful in extrapolation of data.</abstract>
  <note>A thesis submitted in partial fulfillment of the requirements for the degree of Master of Engineering, School of Environment, Resources and Development</note>
  <note>Thesis (M. Eng.) - Asian Institute of Technology, 1987</note>
  <subject authority="lcsh">
    <topic>Filters and filtration</topic>
  </subject>
  <relatedItem type="series">
    <titleInfo>
      <title>Asian Institute of Technology. Thesis ; no. EV-87-8</title>
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  <identifier type="uri">http://203.159.5.9/ait-thesis/detail.php?q=B19214</identifier>
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