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  <controlfield tag="008">260224s2010    xxu                      </controlfield>
  <datafield tag="245" ind1="0" ind2="0">
    <subfield code="a">Directly producing clean and low softening point diesel using integrated hydrotreating and hydroisomerizing catalysts</subfield>
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    <subfield code="c">jul./ago. 2010</subfield>
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    <subfield code="a">18/11/2010 ; 18/11/2010</subfield>
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  <datafield tag="300" ind1=" " ind2=" ">
    <subfield code="a">6 p. ; 3772-3777</subfield>
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  <datafield tag="520" ind1=" " ind2=" ">
    <subfield code="a">Transcripci&#xF3;n del resumen del autor. A novel hydrotreating (HT) catalyst of Mo-W-Ni-P supported on -Al2O3 modified by a Group IVA element and a hydroisomerizing (HI) catalyst of W-Ni supported on modified zeolite &#xDF; with mesopores were prepared by the impregnation method. An integrated process using HT and HI catalysts was designed, and its advantages were well-investigated for directly producing clean diesel from various feedstocks. An industrial application shows that the integrated catalysts have flexible operating modes and are suitable for a wide range of feedstocks. For the HT operating mode, the integrated catalysts showed better hydrodesulfurization (HDS) performance for upgrading the poor quality diesel with a sulfur content of 1000 ppmw and a nitrogen content of 1131 ppmw. The sulfur content of diesel product is less than 40 ppmw, coupled with a hydrodenitrogenation (HDN) rate of 85.76% and an HDS rate of 96.3%. The cetane index increases by 7 units, and the diesel yield is more than 98.0 wt %. For the hydro-dewaxing operating mode, the integrated catalysts showed excellent catalytic performance for upgrading the feeds, with a sulfur content of 990 ppmw and a nitrogen content of 805 ppmw. The HDN rate of 99.42% and HDS rate of 99.99% were also achieved. More importantly, while retaining the cetane index, the diesel yield was as high as 88.72 wt % and the sulfur content and solidifying point of diesel were less than 10 ppmw and -29.3 &#xB0;C, respectively. The higher HDS and HDN activities of the integrated catalysts are associated primarily with enhanced hydrogenation activity and increased acidity of the HI catalyst.</subfield>
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    <subfield code="t">Energy &amp; fuels</subfield>
    <subfield code="g">24</subfield>
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    <subfield code="c">ARTICULO</subfield>
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  <datafield tag="100" ind1="1" ind2=" ">
    <subfield code="a">Zhang, Xuejun</subfield>
    <subfield code="9">19594</subfield>
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    <subfield code="a">Guo, Aijun</subfield>
    <subfield code="9">43688</subfield>
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    <subfield code="a">Wang, Fucun</subfield>
    <subfield code="9">40824</subfield>
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    <subfield code="c">171988</subfield>
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    <subfield code="7">0</subfield>
    <subfield code="9">239807</subfield>
    <subfield code="a">BAAB</subfield>
    <subfield code="b">BAAB</subfield>
    <subfield code="d">2026-03-05</subfield>
    <subfield code="j">200049956</subfield>
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    <subfield code="p">200049956</subfield>
    <subfield code="r">2026-03-05 16:07:43</subfield>
    <subfield code="w">2026-03-05</subfield>
    <subfield code="y">ARTICULO</subfield>
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