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  <controlfield tag="008">260224s2012    xxu                 ing  </controlfield>
  <datafield tag="041" ind1=" " ind2=" ">
    <subfield code="a">Ingl&#xE9;s</subfield>
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  <datafield tag="245" ind1="0" ind2="0">
    <subfield code="a">Technical Assessment of Isothermal and Non-Isothermal Modelings of Natural Gas Pipeline Operational Conditions</subfield>
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  <datafield tag="260" ind1=" " ind2=" ">
    <subfield code="a"></subfield>
    <subfield code="b"></subfield>
    <subfield code="c">mayo/jun. 2012</subfield>
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  <datafield tag="270" ind1=" " ind2=" ">
    <subfield code="a">15/05/2013 ; 15/05/2013</subfield>
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  <datafield tag="300" ind1=" " ind2=" ">
    <subfield code="a">14 p. ; 435-449</subfield>
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  <datafield tag="520" ind1=" " ind2=" ">
    <subfield code="a">Traducci&#xF3;n del res&#xFA;men del autor: Modeling of equipment in a gas pipeline was performed here by deriving a new form of conservation equation set for compressible flow. Then a section of the third Iranian gas transmission pipeline (Nourabad-Pataveh-Dorahan, N-P-D) was investigated by isothermal (IT) and non-isothermal (NIT) modeling approaches taking into account the effects of ground temperature. In the first part, the steady state operation of the N-P-D pipeline including a compressor station at Pataveh was studied. For the known values of natural gas mass flow rate, and inlet/outlet gas pressures at Nourabad/Dorahan points, the IT and NIT modelings showed about 33.7%, 16.6% and 23% maximum difference percent points for the compressors head, compressors rotational speed and fuel consumption rates respectively. In the second part, the unsteady operation of the N-P-D pipeline due to the shutdown of a compressor at Pataveh Compressor Station (PCS) was studied. The results confirmed that at lower ground temperatures (0 and 20&#xB0;C), the remaining compressors could compensate the loss of one compressor. However, at higher ground temperatures (40 and 50&#xB0;C), the compressors had to run faster than the highest permissible speed to be able to deliver a certain mass flow rate without reducing the required pipeline pressure. In all above studied cases, the computing time for the non-isothermal modeling was about three times longer than that for the isothermal one.</subfield>
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    <subfield code="a">3</subfield>
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    <subfield code="t">Oil and Gas Science and Technology</subfield>
    <subfield code="g">67</subfield>
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    <subfield code="c">ARTICULO</subfield>
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    <subfield code="a">Sanaye, S.</subfield>
    <subfield code="9">53190</subfield>
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  <datafield tag="100" ind1="1" ind2=" ">
    <subfield code="a">Mahmoudimehr, J.</subfield>
    <subfield code="9">53191</subfield>
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  <datafield tag="999" ind1=" " ind2=" ">
    <subfield code="c">187695</subfield>
    <subfield code="d">187695</subfield>
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    <subfield code="0">0</subfield>
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    <subfield code="7">0</subfield>
    <subfield code="9">255514</subfield>
    <subfield code="a">BAAB</subfield>
    <subfield code="b">BAAB</subfield>
    <subfield code="d">2026-03-06</subfield>
    <subfield code="j">200059837</subfield>
    <subfield code="l">0</subfield>
    <subfield code="p">200059837</subfield>
    <subfield code="r">2026-03-06 00:17:41</subfield>
    <subfield code="w">2026-03-06</subfield>
    <subfield code="y">ARTICULO</subfield>
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