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    • 87. 发明授权
    • Iron catalyzed coal liquefaction process
    • 铁催化煤液化过程
    • US4411766A
    • 1983-10-25
    • US352282
    • 1982-02-25
    • Diwakar GargEdwin N. Givens
    • Diwakar GargEdwin N. Givens
    • C10G1/06C07C1/00C10G1/08
    • C10G1/086C07C1/00C07C2523/745C07C2527/043
    • A process is described for the solvent refining of coal into a gas product, a liquid product and a normally solid dissolved product. Particulate coal and a unique co-catalyst system are suspended in a coal solvent and processed in a coal liquefaction reactor, preferably an ebullated bed reactor. The co-catalyst system comprises a combination of a stoichiometric excess of iron oxide and pyrite which reduce predominantly to active iron sulfide catalysts in the reaction zone. This catalyst system results in increased catalytic activity with attendant improved coal conversion and enhanced oil product distribution as well as reduced sulfide effluent. Iron oxide is used in a stoichiometric excess of that required to react with sulfur indigenous to the feed coal and that produced during reduction of the pyrite catalyst to iron sulfide.
    • 描述了将煤的溶剂精炼成气体产物,液体产物和通常为固体的溶解产物的方法。 颗粒煤和独特的助催化剂体系悬浮在煤溶剂中,并在煤液化反应器,优选沸腾床反应器中加工。 助催化剂体系包括化学计量过量的氧化铁和黄铁矿的组合,其主要在反应区域中还原成活性硫化铁催化剂。 该催化剂体系导致催化活性增加,伴随改善的煤转化率和提高的油产物分布以及减少的硫化物流出物。 氧化铁以化学计量过量的量使用,与原料煤中的硫反应所需的量以及在将黄铁矿催化剂还原成硫化铁时产生的氧化铁。