Patent GB-548134-A (GB)
Title: An improved process for the catalytic treatment of hydrocarbon oils
IPC: C10G11/18
Filed: 1940-03-12
Abstract: 548,134. Catalytic conversion of hydrocarbon oils. KELLOGG CO., M. W. March 12, 1940, No. 4629. Convention date, May 20, 1939. [Classes 1 (i) and 32] In processes for the catalytic conversion of hydrocarbon oils of the kind in which the catalyst is passed in suspension in the hydrocarbon vapours through the reaction zone, and after separation therefrom regenerated by passage in suspension in an oxygen-containing gas through a regenerating zone and returned to the reaction zone, the catalyst and hydrocarbons are fed through the reaction zone in such proportions that at least half the heat generated in the regeneration zone is absorbed by the catalyst, the ratio by weight of catalyst to hydrocarbons passed through the reaction zone being maintained in conformity with the formula where C represents the fraction of charged hydrocarbon converted to form carbonaceous deposit on the catalysts; H, the heat of combustion of the carbonaceous material in B.T.U.s per lb.; S, the specific heat of the catalyst; T 1 , the deactivation temperature of the catalyst; T 2 , the temperature of the catalyst entering the regeneration zone; and K is the proportion (not less than one half) of the heat generated in the regeneration which is to be absorbed by the catalyst. The regeneration is preferably controlled to leave a predetermined quantity of carbonaceous material deposited on the catalyst and the crude oils are vaporized by contact with the hot regenerated catalyst returned to the reaction cycle. The Specification as open to inspection under Sect. 91 describes apparatus in which a gas oil fraction obtained by the topping distillation of crude oil in a still 3 and tower 4 is fed through a line 12, preferably in admixture with recycle stock from line 14, and is injected through line 15 to mix with hot regenerated catalyst in a pipe 16 constituting an extension of the conversion reactor 17 and provided with a conveyer 19. The oil is vaporized by the hot catalyst and the suspension of vapours and catalyst with the aid of steam injected through line 20 flows upwardly through the tubular conversion zone 17. The reaction products pass to a settling tank 21 where most of the catalyst is separated and flows by gravity through pipe 22 and steam stripper tower 23 into a surge chamber 30. The vapours pass from the settler 21 through line 24 to separator 25 where they are mixed with gases and vapours evolved in the tower 23, the mixture being fed into a fractionating tower 32 where the vapours are fractionated into a fraction of gasoline boiling range recovered overhead through line 33, a light gas oil removed through line 34, a heavy gas oil removed through line 38 and heavy oil recycled through line 39. Any residual catalyst remaining in .the vapours is removed by spraying the vapours with heavy oil removed through line 37 and returned by pump 35. Catalyst collected in surge drum 30 is fed by conveyer 41 through line 42 into the tubular regenerator zone 44 up which it passes in suspension in oxidizing gases injected through line 43. The catalyst is separated and purged from gases and vapours in a cyclone separator 46 and fed to surge chamber 18 from which it is returned to the cycle of operations. This subject-matter does not appear in the Specification as accepted.