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公开(公告)号:US4326946A
公开(公告)日:1982-04-27
申请号:US157837
申请日:1980-06-09
CPC分类号: C10G1/042
摘要: A process of producing a solvent useful in coal liquefaction which includes separating the heavy liquid produced from the liquefaction of coal into a fraction boiling at 200.degree. to 210.degree. C., a fraction boiling at 211.degree. to 230.degree. C., and a fraction boiling at not less than 231.degree. subjecting the fraction boiling at 211.degree. to 230.degree. C. to a hydrogenation treatment to produce a hydrogenated fraction, mixing the hydrogenated fraction with the fraction boiling at 200.degree. to 210.degree. C. to form a resultant mixture, and mixing a portion of the resultant mixture with a portion of the fraction boiling at not less than 231.degree. C. Alternately, the solvent is produced from the heavy liquid by separating it into a fraction boiling at 200.degree. C. to 210.degree. C., a fraction boiling at 211.degree. C. to 230.degree. C., a fraction boiling at 231.degree. C. to 250.degree. C., a fraction boiling at 251.degree. C. to 350.degree. C. and a fraction boiling at not less than 351.degree. C., subjecting each of the middle three fractions to a hydrogenation treatment to form three hydrogenated fractions, mixing the three hydrogenated fractions with the fraction boiling at 200.degree. C. to 210.degree. C. to form a resultant mixture, and mixing the resultant mixture with a portion of the fraction boiling at not less than 351.degree. C.
摘要翻译: 一种生产可用于煤液化的溶剂的方法,其包括将从液化产生的重液体分离成沸腾温度为200至210℃的馏分,沸点为211至230℃的馏分,以及馏分 沸腾不低于231℃,使沸点为211〜230℃的馏分进行氢化处理,生成氢化馏分,将氢化馏分与沸点为200〜210℃的馏分混合,形成混合物 并将所得混合物的一部分与沸点不低于231℃的部分混合。或者,通过将溶液分离成在200℃至210℃沸腾的馏分,将该溶剂从重质液体中制备 ,在211℃至230℃沸腾的馏分,沸点在231℃至250℃的馏分,沸点在251℃至350℃的馏分和沸点不低于的馏分 比351℃高,每个中间三分 进行氢化处理以形成三个氢化馏分,将三个氢化馏分与200℃至210℃的馏分混合以形成所得混合物,并将所得混合物与一部分沸点不同的馏分混合 小于351℃