Patent ID: 7842108

Claim:
A device for generating crude gas having a particle size of fine dust of <20 μm in an entrained flow reactor by gasification of ash containing solid fuels such as bituminous or lignite coals and petroleum coke, with a water content of <10 wt % and a grain size of <200 μm, in the flue stream with an oxidizing medium containing free oxygen, by partial oxidation at pressures between atmospheric pressure and 80 bar, and at temperatures between 1,200 and 1900 degrees Celsius, the device comprising: a pneumatic metering system adapted for pulverized fuel having a water content of less than 10 wt % and a grain size of <200 μm, comprising lines to a bunker whose outlet opens into at least one pressurized sluice, into which sluice open a line for inert gas and a line for depressurized gas, with discharge from the pressurized sluice leading to a metering tank, in the bottom of which tank there is a line for inert gas; a reactor connected to the metering tank via a transport line, the reactor being adapted for gasifying supplied pulverized fuel with an oxidizing medium containing free oxygen at a temperature between 1200 and 1900° C. and at a pressure between atmospheric pressure and 80 bar, said reactor having a transport pipe for fluidized fuel and a line for an oxidizing medium that are fed by means of burners into a reaction chamber having a cooling shield consisting of water-cooled pipes welded gas-tight, and a discharge device; a quenching cooler connected to the discharge device, said quenching cooler having no internals, so as to prevent deposition of slag or dust entrained by the crude gas, and in which nozzles are arranged in one or more nozzle rings, through which quenching water is sprayed in, with the nozzles ending flush with a wear shell made of metal that is placed to protect a pressurized jacket, said quenching cooler further comprising a water bath, an outflow, and an outlet; a dust separator or crude gas scrubber located at the outlet of the quenching cooler; and a condensation stage connected to the dust separator or crude gas scrubber and following the dust separator or crude gas scrubber, said condensation stage being adapted for removing fine dust <20 μm and salt mists by indirectly cooling down the crude gas by 5 to 10° C.