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    • 7. 发明授权
    • Process for deashing primary coal liquids
    • 降低初级煤液的工艺
    • US4476012A
    • 1984-10-09
    • US433176
    • 1982-10-06
    • John G. Gatsis
    • John G. Gatsis
    • C10G21/00C10G1/04
    • C10G21/003
    • A process for deashing primary coal liquids with a selective hydrocarbon solvent separation wherein the coal liquids and selective hydrocarbon solvent are contacted initially at a temperature greater than the temperature at which the deashing separation occurs. More particularly, a process for the production of deashed coal liquid which comprises the sequential steps of: (a) admixing a primary coal liquid containing ash and a hydrocarbon deashing solvent having no hydrogen-transferring ability at a selected admixing temperature from about 250.degree. F. to about 575.degree. F.; (b) reducing the temperature of the entire resulting admixture of the primary coal liquid and hydrocarbon deashing solvent to a deashing temperature about 50.degree. F. to about 125.degree. F. less than the admixing temperature of step (a); and deashing the primary coal liquid with the deashing solvent at the deashing temperature of step (b).
    • 一种采用选择性烃溶剂分离除渣的初级煤液的方法,其中煤液体和选择性烃溶剂最初在大于发生脱气分离的温度的温度下接触。 更具体地说,一种生产除泥煤液的方法,其包括以下步骤:(a)在选定的约250°F的混合温度下混合含有灰分的初级煤液和不具有氢转移能力的烃类除溶剂 至约575°F。 (b)将初级煤液和烃类脱溶剂溶剂的整个混合物的温度降低至步骤(a)的混合温度低约50°F至约125°F的脱气温度; 并且在步骤(b)的脱泡温度下用所述脱溶剂溶解所述初级煤液体。