Process for purifying the off-gases from industrial furnaces, especially from waste incineration plants
AssigneeCiba-Geigy Corporation
InventorsVolker Fattinger, Jurg Schneider
Life of this patent
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AssigneeCiba-Geigy Corporation
InventorsVolker Fattinger, Jurg Schneider
Estimating the term…
A process for purifying the off-gases from industrial furnaces and especially from waste incineration plants is described in which process the off-gases which contain acid, neutral and/or basic pollutants in the gaseous or solid form or in the form of a mist, are treated in an evaporative cooler and then in a dry purifier, in which they are freed from at least a substantial portion of the solid pollutants, and finally in a scrubber by means of a wash liquid. The temperature of the off-gases in the evaporative cooler is kept above the dew point, and the wash liquid in the scrubber is cycled through a slurry separator, from which suspension or solution of pollutants is withdrawn from the sludge separator and fed into the evaporative cooler and mixed in a mixing space in the latter with the hot off-gases. Those walls of the evaporative cooler which come into contact with the mixture of off-gases and recycled suspension or solution of pollutants and which consist of a material that can be corroded by the said mixture at room temperature are heated from the outside to a temperature above the dew point. As a rule the pH value of the liquid phase in the sludge separator and in each of the gas wash stages of the scrubber directly upstream of the said separator is kept below 4.
A process for purifying the off-gases from industrial furnaces, especially from waste incineration plants, in which process the off-gases, which contain harmful substances selected from acid, neutral and basic pollutants in the gaseous or solid form or in the form of a mist, are treated in an evaporative cooler and then in a dry purifier, in which they are freed from at least a substantial portion of the solid pollutants, and then in a scrubber by means of a wash liquid, the temperature of the off-gases in the evaporative cooler being kept above the dew point, and the wash liquid in the scrubber being cycled through a sludge separator, from which suspension or solution of pollutants is withdrawn, said withdrawn suspension of pollutants being fed from the sludge separator to the evaporative cooler and mixed in a mixing space in the latter with the hot off-gases, with the gases and the suspension being separately removed from the bottom of the evaporative cooler;
A process as described in claim 9, wherein the pH value of the wash liquid in the final wash stage of the scrubber and the sludge separator which is directly downstream of said final wash stage is kept above 1.
A process as described in claim 10, wherein the proportion which can be evaporated of the liquid phase of the pollutants suspension to be fed into the evaporative cooler is at least 90 percent by weight, and the pH value of the wash liquid in the final wash stage of the scrubber and in the sludge separator which is directly downstream of said final wash stage is kept in the range of 2 to 3.5.
A process as described in claim 15, wherein the gas resistance of the aerosol separator is from 10 to 30 mbars.
Dependencies are inferred from the claim text.