会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 15. 发明授权
    • Coal refining
    • 炼煤
    • US4269692A
    • 1981-05-26
    • US75279
    • 1979-09-13
    • Suresh P. BabuRichard A. Knight
    • Suresh P. BabuRichard A. Knight
    • C10G1/04C10G1/00
    • C10G1/04
    • A process for fossil fuel refining by contacting ground solid fossil fuel for about 1/2 to about 3 hours with phenol at a temperature of about 600.degree. to 690.degree. F. and a corresponding saturation pressure of about 250 to 430 psig, the phenol being present in greater amounts by weight than the fossil fuel and dissolving refined product from the fossil fuel leaving a solid fuel residue. The phenol containing the refined product is removed from the fuel residue while heated, followed by cooling and separation of the refined product from the phenol which is recycled to the solvent extraction process. The process provides refined products low in mineral matter and sulfur following a low pressure solvent refining process which does not require a proton donor, acid catalyst or an external source of hydrogen.
    • 在大约600至690°F的温度和约250至430psig的相应的饱和压力下将接地固体化石燃料与苯酚接触约1/2至约3小时的化石燃料精炼方法,苯酚为 以比化石燃料重量更大的量存在,并且从化石燃料中溶解精制产物留下固体燃料残余物。 含有精制产物的苯酚在加热的同时从燃料残渣中除去,然后将精制产物与再循环至溶剂萃取过程的苯酚进行冷却和分离。 该方法在不需要质子供体,酸催化剂或外部氢源的低压溶剂精制方法之后提供矿物质和硫的低精炼产物。