发明名称 MADEN KOEMUERUENUEN SUREKLI HIDROKARBONIZASYONUNA MAHSUS USUL
摘要 1529850 Coal hydrocarbonization UNION CARBIDE CORP 23 Dec 1975 [27 Dec 1974] 52600/75 Heading C5E A process for the hydrocarbonization of coal particles employing a fluid bed reaction zone comprises the steps: (a) pressurizing said particles with a hydrogen-rich gas; (b) fluidizing said particles with a non-oxidizing gas to form a dense phase; (c) optionally preheating said coal particles in said dense phase in a substantially oxygen-free environment to a temperature below a temperature at which said coal particles undergo plastic transformation; (d) providing a fluid-bed within said zone for hydrocarbonization at a reaction temperature of from 480‹ C. to 600‹ C., said fluidbed comprising a matrix of non-agglomerating particles at said reaction temperature fluidized by a hydrogen-rich (defined), oxygen-free gas; (e) continuously introducing said coal particles and a hydrogen-rich, oxygen-free conveying gas into the lower portion of said zone in substantially vertically upwards direction, said coal particles having a velocity sufficient to disperse rapidly and uniformly within said matrix at said predetermined temperature; (f) continuously reacting said coal particles in said zone with hydrogen in said zone at said reaction temperature to produce a product comprising a condensable vapour and solid char; (g) maintaining the solids in said zone for an average residence time of 5 to 60 minutes and said vapour for 10 to 250 seconds; (h) maintaining the average hydrogen partial pressure in said zone at 100 p.s.i. to 1200 p.s.i.; and (i) continuously withdrawing from said zone said product vapour and solids. Oil recovered from the condensable vapour product may be recycled by upward injection into the reaction zone.
申请公布号 TR19481(A) 申请公布日期 1979.01.22
申请号 TR19750019481 申请日期 1975.12.26
申请人 UNION CARBIDE CORP 发明人
分类号 C07C27/00;C07C37/00;C07C37/52;C07C39/00;C07C67/00;C10B57/08;C10G1/06;C10G1/08;C10J3/54 主分类号 C07C27/00
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