Method for removal of last traces of soluble ash and elements fr

Fuel and related compositions – Liquid fuels – Aluminum or heavy metal – other than lead – containing

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C10L 910

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active

040959546

ABSTRACT:
Solvent refined coal is treated with liquid water at a temperature of about 500.degree.-550.degree. F in a closed cylindrical vessel under the saturation pressure 665-1030 psig of water at that temperature and under gentle agitation to insure low shear liquid-solid contact for about 1/2 to 2 hours.
Surprisingly, the soluble ash, generally sodium or potassium salts, is leached out to bring the sodium content down from 50-60 parts per million to a value of less than 1 part per million which makes the product very suitable as a feed for direct firing in a gas turbine.
In addition the total ash content is reduced from a value of approximately 0.1% to a value less than 0.05% which means that in addition to reducing the quantity of sodium and potassium, there are other constituents of the ash which also have been removed.

REFERENCES:
patent: 1420164 (1922-06-01), Trent
patent: 2761824 (1956-09-01), Eastman et al.
patent: 4021328 (1977-05-01), Wolk

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