Patent GB-195055-A (GB)
Title: Improvements in or relating to treating oils, waxes and the like to remove or recover substances therefrom
IPC: C10G73/42
Filed: 1923-03-01
Abstract: 195,055. Silica Gel Corporation, (Assignees of Patrick, W. A., and uliller, E. B.). March 16, 1922, [Convention date]. Purifying fatty, mineral, and tar oils, mineral and other maxes.-The process of adsorbing a solute from a non-aqueous solution by porous material having very fine pores, described in Specification 175,987, [Class 2 (iii), Dyes &c.], is applied to purifying oils and waxes, benzine, toluene, carbontetrachloride and aniline. The adsorbing-material preferred is the silica gel described in Specification 136,543, [Class 1 (i), Chemical processes &c.]; other substances having sufficiently fine pores, such as activated charcoal, or gels of the oxides of iron, tin, aluminium, tungsten, zirconium and titanium, preferably made by the process described in Specification 212,065, [Class 1 (i), Chemical processes &c.], may be used. The substances adsorbed may be fractionally liberated by immersing the adsorbing-material first in cold water to remove the high-boiling hydrocarbons, and then in hot water to remove the heavier fractions, or by distilling, preferably in the absence of air, or by treating with steam or hot non-oxidizing gases. The adsorption may be carried out by passing the crude liquid through, or mixing it with, adsorptive material. In the plant shown, the crude petroleum &c. is pumped through a series of agitators 13, 13<2>, 13<3> and separators 20, 20<2>, 20<3>. Fresh adsorptive material supplied from a hopper 27 to the final agitator 13<3>, passes to the separator 20<3>, and thence by a pipe 30 to the agitator 13<2> and separator 20<2>. The adsorptive material then passes in a similar manner through the agitator 13 and the separator 20, and is afterwards led by a pipe 33 to a series of agitators 35 41, and separator 37, 44, where it is washed with cold and hot water to displace the adsorbed substances. The washed adsorptive material is pumped to the filter-press 50, and possed thence by a duct 51 to an activator 52, where residual adsorbed material is distilled off in the absence of air. The activator comprises a chamber heated by horizontal transverse tubes through which hot gases circulate. Steam or other gas may also be supplied to the interior by inlet 110. The dried adsorbing-material is driven by a fan 54 to a cyclone separator 55, from which it passes by a feed device to prevent passage of vapours into hopper 56, and thence bv worm 60 to the cooled hopper 27. The feed device comprises a plate oscillating horizontally just below the lower outlet of the separator 55. The steam &c. may be conveyed back to the fan circuit by a pipe 112. An auxiliary activator fed by a pipe 123 and discharging by a pipe 126 is provided. A refined petroleum product is obtained which contains at least 10 per cent of unsaturated hydrocarbons and less than 0.02 per cent of sulphur, and a petroleum product is recovered from the pores of the adsorbing-material, which contains at least 25 per cent of unsaturated hydrocarbons and having a S.G. of at least 40 BÚ. Reference has been directed by the Comptroller to Specifications 24667/10, 163,505, 175,987, and 186,955.