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US4138231A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of wet-cleaning gases containing sulfur dioxide, halogens and arsenic from pyrometallurgical treatment of sulphidic materials

Assignee: Boliden AB
•
Filing: 1977-03-30
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Granted: 1979-02-06
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Expires: 1997-03-30
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Abstract

Abstract The invention comprises a method of wet-cleaning gases containing sulfur dioxide, halogens together with arsenic and/or arsenic compounds obtained in a pyrometallurgical treatment of sulfidic materials. The gases are washed in a diluted sulfuric acid circulating in a closed circuit, from which arsenic is recovered. The gases are then cooled to water condensation whereby the halogens are substantially completely taken up in said condensate and separated. The separated condensate is then discharged to a recipient after precipitation of residual arsenic and neutralization.

Inventors

  • 👤 Bo G. V. Hedenas
  • 👤 Johan E. Wiklund
  • 👤 Thore R. H. Johansson
  • 👤 Karl-Axel Melkersson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 22:41
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/68; B01D53/48; B01D53/50; B01D53/507

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 192 words
A method of wet-cleaning gases containing sulfur dioxide, halogens, and at least one volatilized substance selected from the group consisting of arsenic and arsenic compounds emanating from pyrometallurgical treatment of sulfidic materials, comprising washing the gases with diluted sulfuric acid circulating in a closed circuit, substantially the whole amount of the volatilized substance or substances present being taken up and solidified in said diluted acid; selectively separating said solidified substance or substances from a part-stream of said diluted sulfuric acid in said closed circuit; recycling the part-stream to the washing step and the pyrometallurgical treatment; removing from the washed gases any entrained liquid sulfuric acid; controlling the water content of the gases so as to permit a substantial water condensation to be obtained during the subsequent cooling, cooling the washed gases having controlled water content whereby halogen ions are substantially completely taken up in the formed condensate; separating the condensate from the gases; treating at least a part of the condensate with a precipitating agent so as to precipitate any residual amounts of arsenic compounds; separating the precipitate from the remaining condensate and neutralizing and discharging said remaining condensate to a recipient.
Claim 2
Independent Claim 192 words
A method of wet-cleaning gases containing sulfur dioxide, halogens, and at least one volatilized substance selected from the group consisting of arsenic and arsenic compounds emanating from pyrometallurgical treatment of sulfidic materials, comprising washing the gases with diluted sulfuric acid circulating in a closed circuit, substantially the whole amount of the volatilized substance or substances present being taken up and solidified in said diluted acid; selectively separating said solidified substance or substances from a part-stream of said diluted sulfuric acid in said closed circuit; recycling the part-stream to the washing step and the pyrometallurgical treatment; removing from the washed gases any entrained liquid sulfuric acid; controlling the water content of the gases so as to permit a substantial water condensation to be obtained during the subsequent cooling, cooling the washed gases having controlled water content whereby halogen ions are substantially completely taken up in the formed condensate; separating the condensate from the gases; treating at least a part of the condensate with a precipitating agent so as to precipitate any residual amounts of arsenic compounds; separating the precipitate from the remaining condensate and neutralizing and discharging said remaining condensate to a recipient.
Claim 3
Dependent Claim 34 words
A method according to claim 1, wherein any mercury present in the gases is substantially taken up in the washing stage by ensuring that said diluted sulfuric acid contains at least 0.5 g/l mercury(II)-ions.
Claim 4
Dependent Claim 21 words
A method according to claim 1, wherein said diluted sulfuric acid contains more than 50 g/l arsenic trioxide in solid form.
Claim 5
Dependent Claim 53 words
A method according to claim 1, wherein said solidified substances are partly separated from said diluted sulfuric acid, and withdrawn from the process and wherein any solid compounds other than said solidified substances which also are separated from said diluted sulfuric acid are returned to the pyrometallurgical treatment stage for decomposition or incineration.
Claim 6
Dependent Claim 30 words
A method according to claim 1, wherein the gases subsequent to washing, are moistened in a separate stage to a water vapor content of at least 25 g/m 3 .
Claim 7
Dependent Claim 37 words
A method according to claim 1, wherein said condensate is removed after cooling the gas and partly recycled to the washing stage, and partly transferred to treatment with a precipitating agent and precipitation of residual arsenic compounds.
Claim 8
Dependent Claim 62 words
A method according to claim 1, wherein the gases are cooled subsequent to being moistened, and wherein at least part of the condensed water is freed, by precipitation and separation, from residual arsenic compounds, whereafter the water is discharged to recipient and wherein residual quantities of non-purified water are returned as make up water to the washing stage and the moistening stage.
Claim 9
Dependent Claim 31 words
A method according to claim 7, wherein the condensed water is purified by adding a sulfide of a metal selected from the group consisting of alkali metals and alkaline earth metals.
Claim 10
Dependent Claim 20 words
A method according to claim 7, wherein the condensed water is purified in an alkaline environment with an iron salt.
Claim 11
Dependent Claim 42 words
A method according to claim 1, wherein the sulfuric acid concentration of said diluted sulfuric acid is permitted to vary from the selected content at most 3%-units, and wherein the said content is preferably held within the range of 40-70% by weight.
Claim 12
Dependent Claim 36 words
A method according to claim 10, wherein said sulfuric acid content is controlled by supplying diluted sulfuric acid, from a washing stage of an external plant in which sulfuric acid is used, in a non-purified form.

References Cited (Backward Citations)

US2028318A Cited
US2416011A Cited
GB742052A Cited
GB780984A Cited
US3677696A Cited
US3899308A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-02-05 1982-08-07 1983-02-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-02-05 1986-08-07 1987-02-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-02-05 1990-08-07 1991-02-06 $7700.00 Window Closed / Lapsed

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