Abstract A wet process for stack gas treatment wherein the stack gas is scrubbed with a suspension containing calcium hydroxide and/or calcium carbonate to remove sulfur oxides from the gas, characterized in that (1) air or oxygen-containing gas is supplied to the gas scrubber so as to oxidize at least 18% of the sulfur oxides absorbed by the scrub liquid to gypsum, and then part of the gypsum from the gypsum-containing scrub liquid partly taken out is recycled to the scrubber, or (2) part or whole of the scrub liquid is taken out from the scrubber into an oxidizer, where it is oxidized with the supply of air or oxygen-containing gas, and, after the oxidation, part of the scrub liquid from the oxidizer is recycled to the scrubber, whereby at least 18% of the sulfur oxides absorbed from the gas by the scrub liquid is oxidized to gypsum.
A wet process for stack gas treatment wherein the stack gas is scrubbed in a scrubber with a scrubbing suspension containing calcium hydroxide, calcium carbonate, or mixtures thereof to remove sulfur oxides from the gas, characterized in that at least a part of the scrubbing suspension is taken out from the scrubber into the oxidizer, where it is oxidized with a supply of air or oxygen containing gas and, after the oxidation, all of the scrubbing suspension from said oxidizer is recycled to said scrubber whereby at least 18% of the sulfur oxides absorbed from the gas by said scrubbing suspension is oxidized to gypsum, the concentration of calcium sulfate in said scrubbing suspension being from 2 to 15% by weight of the total weight of the liquid in said scrubbing suspension.
Claim 2
Dependent Claim
132 words
A wet process for stack gas treatment wherein the stack gas is scrubbed in a scrubber with a scrubbing suspension containing calcium hydroxide, calcium carbonate, or mixtures thereof to remove sulfur oxides from the gas, characterized in that at least a part of the scrubbing suspension is taken out from the scrubber into the oxidizer, where it is oxidized with a supply of air or oxygen containing gas and, after the oxidation, all of the scrubbing suspension from said oxidizer is recycled to said scrubber whereby at least 18% of the sulfur oxides absorbed from the gas by said scrubbing suspension is oxidized to gypsum, the concentration of calcium sulfate in said scrubbing suspension being from 2 to 15% by weight of the total weight of the liquid in said scrubbing suspension.