between 1 and 5 mpa the post treatment of the tgr reactor products allows the process to meet higher product specifications the post treatment process is a very mild operation since the typical precursors to catalytic poisoning coke and metals are processed upstream in the tgr reactor referring to fig3 provides for the operation of a combined process of distillation hydrotreating hydrocracking and gasification distillation trays 101 are provided for fractionation a reflux stream 87 is provided to condense reactor vapors and control the upper section temperature gradient side stream products lines 88 and 92 remove the fractions with endpoint temperatures of 320 c and 270 c respectively a circulating stream of catalyst stream 100 is dispersed in feed stream 12 the mixture of feed and catalyst stream 13 enters reactor 15 through distributor 14 into contact trays 102 the feed is cracked and stabilized in the presence of hydrogen generated in catalytic bed 16 the catalyst is continuously removed through line 97 and regenerated in regenerator 99 the regenerated catalyst is recirculated through line 100 and dispersed in feed stream 12 referring to fig4 provides for a variation in a combined process of distillation hydrotreating hydrocracking and gasification in this method two distinct catalysts are used catalyst bed 16 is specific to promote the generation of hydrogen whereas catalyst bed 102 is specific to promote the hydrogenation of cracked products the upper part of the reactor employs fractionation trays 101 to produce three distinct streams 88 92 and 18 referring to fig5.