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
    • 4. 发明专利
    • LIQUEFACTION OF COAL BY USING COAL IMPREGNATED WITH CATALYST
    • JPH0598265A
    • 1993-04-20
    • JP26404391
    • 1991-10-11
    • ASAHI CHEMICAL IND
    • HAYASHI SHIGEYOSHITAMURA NOBUHIRO
    • B01J27/053C10G1/06C10G1/08
    • PURPOSE:To make it possible to reduce the amount of a catalyst used and to increase the yield of low-boiling fractions by using coal impregnated with a catalyst containing a metal sulfate in liquefying coal by reacting coal slurried in a hydrocarbon oil at high temperature and high pressure with hydrogen. CONSTITUTION:20-50wt.% coal powder (e.g. Pacific coal which can pass a 100-mesh screen) is thrown into a 0.001-0.06mol aqueous solution of a sulfate containing metallic ions (e.g. ferrous sulfate), and the resulting mixture is agitated and thoroughly deaerated. After the coal powder is impregnated for at least one hour, it is dried with a spray dryer. The amount of the catalyst used in coal liquefaction is 0.01-10wt.% (in terms of Fe, dry ash-free base). Although it is not always necessary to add an oil (e.g. crystal-free anthracene oil) as a medium, the catalyst is added in an amount of generally 100-400wt.% based on the coal. The temperature of coal during the liquefaction is 300-900 deg.C. Although hydrogen need not be added in the liquefaction if a fully hydrogenated oil is used as a medium, it is generally suitable to use highly pure hydrogen. The pressure of hydrogen in the reaction is 10kg/cm or above.
    • 9. 发明专利
    • PREVENTION OF BLOCKAGE OF SLURRY PREHEATER
    • JPH0598269A
    • 1993-04-20
    • JP25921391
    • 1991-10-07
    • ASAHI CHEMICAL IND
    • HAYASHI SHIGEYOSHITAMURA NOBUHIRO
    • C10G1/06C10G1/08
    • PURPOSE:To prevent the blockage of a slurry preheater by using a pre-sulfided metal oxide as a catalyst for a coal liquefaction reaction. CONSTITUTION:A metal oxide (e.g. iron ore) as a catalyst, an oil (e.g. crystal- free anthracene oil) as a medium and a promoter (e.g. powdered sulfur) are fed to a preparation tank and subjected to pre-sulfidation. The promoter sulfur is used in an amount to give an atomic ratio to the iron atoms of the catalyst of 0.2-1. The presulfidation is performed for at least 15min at 50-500 deg.C in a hydrogen stream. After the presulfidation, powdered coal and powdered sulfur are mixed into the mixture to form a slurry. The coal (Pacific coal which can pass a 100-mesh screen) is used in a concentration of 30-50% and the catalyst is used in an amount to give an Fe/DAF coal weight ratio of 0.02-0.03 in the presulfidation. The promoter sulfur in the liquefaction is used in an amount to give an S/Fe atomic ratio of 0.02-3. The liquefaction is performed for 30-90min at 420-460 deg.C under a reaction pressure of 170-200kg/cm in a hydrogen stream. According to this process, the liquefier can be operated continuously for a long time without blocking the slurry preheater.