US 4,049,570 AGranted

Method and apparatus for removing vapors and aerosols from gases produced in a gasification plant

AssigneeDr. C. Otto & Comp. G.m.b.H.

InventorsPaul Gernhardt, Wolfgang Grams, Siegfried Pohl, Wilhelm Danguillier

Life of this patent

Estimating the term…

Loading patent…

Abstract

The high temperature gasification of solid fuel or mixtures of solid and liquid fuels is carried out by a method and apparatus wherein the gasified product from a high temperature gasification chamber having a slag bath therein is fed into a first dust collector. Gases, including vapors or aerosols, are fed from the dust collector into a waste heat boiler to reduce the temperature of the gases down to about 250.degree. C. The solids which essentially include flue coke are discharged from the dust collector into a separate heat exchanger wherein the temperature of the solids is reduced down to about 200.degree. C. The cooled solids and the cooled gases are fed into an absorption chamber wherein for a period of 1 to 10 seconds, the aerosols are absorbed into the flue coke. The absorption chamber is connected to a second dust collector that separates the gases from the flue coke having the absorbed aerosols. The purified gases are then discharged from the second dust collector and the flue coke with the absorbed aerosols is returned to the slag bath in the gasification chamber.

Claims6

Dependent claims

In a process for removing vapors or aerosols from the product of high temperature gasification of solid fuel or a mixture of solid and liquid fuels wherein the fuel is fed into a gasification chamber of the type including a melting chamber therein having a slag bath at the bottom thereof, and wherein a mixture of gases and solids is discharged from the top of the gasification chamber at a temperature within the range of 800.degree. C. to 1000.degree. C. and slag is normally discharged from the bottom of the gasification chamber, the improvement comprising the steps of:

separating said mixture after discharge from the gasification chamber into a gas phase including aerosols and into a solid phase which essentially includes flue coke,
separately cooling at least down to a temperature within the range of 300.degree. C. to 100.degree. C. both the gases and the solids after separation thereof,
combining the cooled gases and the cooled solids for a period of 1 to 10 seconds within a chamber for the absorption of aerosols by the flue coke from the gases,
separating flue coke including the absorbed aerosols from the remaining gases consisting cheifly of carbon monoxide and hydrogen,
discharging said remaining gases,
returning the flue coke including the absorbed aerosols to said melting chamber for gasification of the flue coke, and
discharging aerosols together with slag from the bottom of said gasification chamber.

4 more elements

Dependencies are inferred from the claim text.