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  <titleInfo>
    <title>Modelling the HYPHI digester process for methanization of pig manure</title>
  </titleInfo>
  <name type="personal">
    <namePart>Ngo Van Thanh</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Tentscher, Wolfgang</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Surapong Chiraratananon</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Edelman, David J.</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>The Government of French</namePart>
    <role>
      <roleTerm type="text">Scholarship Donor</roleTerm>
    </role>
  </name>
  <typeOfResource>text</typeOfResource>
  <originInfo>
    <place>
      <placeTerm type="code" authority="marccountry">th</placeTerm>
    </place>
    <place>
      <placeTerm type="text">Bangkok</placeTerm>
    </place>
    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1991</dateIssued>
    <issuance>monographic</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
    <extent>116 p.</extent>
  </physicalDescription>
  <abstract>A kinetic model for digestion of pig manure with high concentration of suspended  matter was developed based on HASHIMOTO's model. At first, this model was verified with  32 actual data points. Furthermore, a term for the death rate of microbial organisms was  introduced. It was applied for computing the optimum conditions for volumetric loading rate  rv,CH4 (m3 CHJm3 r.d) at a given temperature. The hydraulic retention time eH was varied from  2 to 25 days with increments of 1 day and the influent VS concentration Cvso (kgVSjm3 r) was  varied from 1 to 100 with increments of 0.1. It was shown that, under tropical climate with  average temperatures of 30°C, maximum values of rv,CH4 occur at eH ""' 10 days and Cvso ""'  70 (kgVSjm3 }, therefore, the volume of the digester may be reduced and total investment  costs can be decreased.  The average ultimate methane yield B0 is about 0.5 (m3 CHJkgVS0 ). Computation on  the effects of Cvso on the kinetic parameter K was determined by eq. 5.2.1. Fig. 5.2.1 showed  that threshold concentration of influent VS concentration can be up to over 80 (kgVSjm3 r)  without causing inhibition. Thereby, confirming experimental results of HILL D.T. and co workers (1986).  The exact solution of the first order differential equation was used for kinetic  description of the low solids reactor. In this case, the kinetic parameter K1 (day)"1 does not  only depend on temperature, but also on type of the material and configuration of the packed  bed.  The HYPHI computer package was written for biogas plant systems with four  modifications (Plug-Flow Reactor Only, Plug-Flow with Settler, HYPHI system with a PF  Reactor and AF Reactor and HYPHI system with PF Reactor and UASB Reactor) to design  and model all biogas systems. The program environment of Turbo-Pascal Version 6.0 was  used for the HYPHI package.</abstract>
  <note>A Thesis submitted in Partial Fulfillment of the Requirements for the Degree  of Master of Science, School of Environmental, Resources and Development</note>
  <note>Thesis (M.Sc.) - Asian Institute of Technology, 1991</note>
  <subject authority="lcsh">
    <topic>HYPHI (Computer program)</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Farm manure</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Biogas</topic>
  </subject>
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    <titleInfo>
      <title>Thesis ; no. ET-91-22</title>
    </titleInfo>
    <name type="corporate">
      <namePart>Asian Institute of Technology.</namePart>
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    </name>
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  <identifier type="uri">http://203.159.5.9/ait-thesis/detail.php?q=B17519</identifier>
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    <recordCreationDate encoding="marc">290998</recordCreationDate>
    <recordChangeDate encoding="iso8601">20260818155605.0</recordChangeDate>
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