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The hydroliquefaction of Göynük oil shale with/without catalyst was carried out in the presence of supercritical toluene. The maximum conversion and the yield of extract was reached at 400°C for non-catalysis hydroliquefaction experiments. The conversion and the yield of extract reached a maximum value at 400°C for catalytic hydroliquefaction with pyrite. The pyrite catalyst showed no noticable effect...
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