Process of treating the gasification residue formed by the gasification of solid fuels in a fluidized bed
AssigneeMetallgesellschaft Aktiengesellschaft
InventorsPeter Herbert, Rainer Reimert, Michael Stroder
Life of this patent
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Abstract
In addition to ash and coke, the gasification residue contains alkaline earth metal sulfide and alkaline earth metal oxide because desulfuring agents have been supplied to the gasifier. At temperatures from 5.degree. to 80.degree. C. the gasification residue is mixed with an acid-containing aqueous solution so that a gas which is rich in H.sub.2 S is produced. Ash, coke, and alkaline earth metal salt are supplied to a flotation zone, in which coke is separated. A solid residue which contains ash and alkaline earth metal salt is withdrawn from the flotation zone. Carbonic acid or dilute sulfuric acid is preferably used as an acid.
Claims3
A process for treating a gasification residue that is formed by the gasification of sulfur-containing granular fuel selected from the group consisting of coal, lignite and peat, said granular fuel being gasified in a fluidized bed reactor at a temperature from 700.degree. to 1100.degree. C. by feeding an oxygen-containing fluidizing gas into said reactor, and feeding into said reactor at least one alkaline earth metal carbonate or alkaline earth metal oxide for effecting at least a partial desulfurization of a product gas, by the gasification said product gas and said gasification residue being formed, said process comprising the steps of:
- a) withdrawing at least a portion of said gasification residue from the lower part of said reactor, said withdrawn residue containing ash, 8 to 80 percent by weight coke, 2 to 45 percent by weight alkaline earth metal sulfide, and 1 to 25 percent by weight alkaline earth metal oxide, and cooling said withdrawn residue to a temperature in the range of 5.degree. to 80.degree. C.;
- b) feeding the cooled residue from step (a) into a mixing zone and mixing it with an aqueous solution of sulfuric acid, reacting said residue with said acid and producing alkaline earth metal salt and a gas which is rich in H.sub.2 S, withdrawing said gas from said mixing zone;
- c) from the mixing zone of step (b) withdrawing a remaining gasification residue, said remaining residue containing ash, coke and alkaline each metal salt, supplying said remaining residue into a flotation zone, feeding a gas and a vegetable oil or mineral oil into said flotation zone and forming a coke-containing froth in said flotation zone, withdrawing said coke-containing froth from said flotation zone and supplying at least a portion of said withdrawn coke into said fluidized bed reactor;
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- d) withdrawing from said flotation zone a suspension containing ash and alkaline earth metal, and dewatering said suspension.
Dependencies are inferred from the claim text.