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  <titleInfo>
    <title>Energy management in corn alcohol distilleries in China</title>
  </titleInfo>
  <name type="personal">
    <namePart>Fu Xiaofeng</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>Mora, J. A.</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Yongping, Zhai</namePart>
    <role>
      <roleTerm type="text">Examination Committee </roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>EEC</namePart>
    <role>
      <roleTerm type="text">Scholarship Donor  </roleTerm>
    </role>
  </name>
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  <originInfo>
    <place>
      <placeTerm type="code" authority="marccountry">th</placeTerm>
    </place>
    <place>
      <placeTerm type="text">Bangkok</placeTerm>
    </place>
    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1992</dateIssued>
    <issuance>continuing</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
    <extent>103 leaves : ill.</extent>
  </physicalDescription>
  <abstract>The energy consumption pattern in two corn alcohol  distilleries in China, Liaoning Province, were investigated and  analyzed. The electri city consumption was about 1 MJ e and steam  consumption about 18.5 MJth per liter pure alcohol (1 p.a.) in  bot h distilleries. Cooking and distillation consumed about 34 %  and 56% of the total thermal energy , respectively.  This study focused on analyzing the energy conservation  potential of a) the vapor recompression cyc l e (VRC) system in  distillation processes and b) biogas generated by anaerobic  digestion of wastewaters (slops).  As already mentioned, the largest energy consumer is  distillation wit h a share of 56% (Longguan) and 57% (Shenyang) of  the total energy consumption, respectively. A vapor recompression  cycle system (heat pump), may reduce the total energy consumption  (electricity+ steam) by 44% and 46%. Ass uming an initial  investment of 18315$ (Longguan) and 27472$ (Shenyang), payback  periods of about 3 and 4 years, respectively could be achieved.  By applying the Contois kinetic model, the operating  conditions of the existing HYBRID biogas plant were opt imi zed in  regard to maximum volumetric me thane production rate (2 . 85 CH4 N  m3/m3). The following conditions were proposed: HRT: 1.4 days,  temperature: 40°C, substrate con centration: 23.4 CODo/l. If all  the s lop (135 m3/d) would be treated, in Longgaun about 1,080 Nm3  CH4/d (about 8 Nm3 CH4/m3 slop) could be generated . This  corresponds to 288 MJ/m3 slop at a slop : ethano l ratio of 14.71,  to 4.23 MJ/l p.a.. The specific e n ergy consumption may replace  88% of the electricity consumpt ion. Actually, 38% of the slop is  treated. Thus, the specific energy production from slop is 1.6  MJ/l p . a .. This could cover , at an energy conversion efficiency  of 0.23 from methane to electricity. Only 36% of the electricity  consumption could be replaced. And the energy bill will be  reduced from 0 . 056 $/1 . p . a to 0.047 $/1 . p.a. (Longquan) and from  0.044 $/1.p.a . to 0 . 038 $/1.p.a. (Shenyang), respectively,  calcu l ated with a e l ectricity cost 0.033 $/kWh.</abstract>
  <note>A thesis submitted in partial fulfillment of the requirement for the degree of Master of Engineering</note>
  <note>Thesis (M.Eng.) - Asian Institute of Technology</note>
  <subject authority="lcsh">
    <topic>Distilleries</topic>
    <topic>Energy concumption</topic>
  </subject>
  <relatedItem type="series">
    <titleInfo>
      <title>Thesis ; no. ET-92-8</title>
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      <namePart>Asian Institute of Technology.</namePart>
      <namePart/>
    </name>
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  <identifier type="uri">http://203.159.5.9/ait-thesis/detail.php?q=B16250</identifier>
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  <recordInfo>
    <recordCreationDate encoding="marc">290998</recordCreationDate>
    <recordChangeDate encoding="iso8601">20260818095848.0</recordChangeDate>
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