Abstract PCT No. PCT/SE83/00280 Sec. 371 Date Mar. 8, 1984 Sec. 102(e) Date Mar. 8, 1984 PCT Filed Jul. 11, 1983 PCT Pub. No. WO84/00390 PCT Pub. Date Feb. 2, 1984.A method for keeping the heating surfaces in the final thickener (VI), which is divided into several sections (A,B,C), clean in evaporating waste liquors in pulping processes for recovering the cooking chemicals. Chemical solutions e.g. residual products from other processes as tall oil separation and chlorine dioxide production are added to cover the chemical losses. According to the invention the chemical solutions are supplied to those sections of the final thickener which are at the time not being washed with thick waste liquor from the preceding evaporator (II).
In the process of evaporation of a waste liquor from a pulping process to recover useful chemicals wherein the dilute waste liquor is evaporated in a plurality of evaporation stages to obtain thick waste liquor, and concentrated in a thickener, the thickener comprising at least two zones, a solution of a residual product from other processes is added to the waste liquor, said residual product being a member selected from the group consisting of (1) spent acid from a chlorine dioxide production plant and (2) spent acid from a tall oil plant, wherein during operation, at least one zone of said thickener is washed with thick waste liquor from a preceding evaporation stage, the improvement which comprises introducing said residual product to a zone of said thickener which is not being washed with thick waste liquor from a preceding evaporation stage.
Claim 2
Dependent Claim
141 words
In the process of evaporation of a waste liquor from a pulping process to recover useful chemicals wherein the dilute waste liquor is evaporated in a plurality of evaporation stages to obtain thick waste liquor, and concentrated in a thickener, the thickener comprising at least two zones, a solution of a residual product from other processes is added to the waste liquor, said residual product being a member selected from the group consisting of (1) spent acid from a chlorine dioxide production plant and (2) spent acid from a tall oil plant, wherein during operation, at least one zone of said thickener is washed with thick waste liquor from a preceding evaporation stage, the improvement which comprises introducing said residual product to a zone of said thickener which is not being washed with thick waste liquor from a preceding evaporation stage.
Claim 3
Dependent Claim
18 words
The process according to claim 1, wherein said waste liquor from a pulping process is the sulfate liquor.
Claim 4
Dependent Claim
13 words
The process according to claim 1, wherein the thickener is a heat exchanger.