CS240878B1 - The method of reducing gaseous arsenic exhales in the condensation melting of copper concentrators - Google Patents
The method of reducing gaseous arsenic exhales in the condensation melting of copper concentrators Download PDFInfo
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- CS240878B1 CS240878B1 CS843664A CS366484A CS240878B1 CS 240878 B1 CS240878 B1 CS 240878B1 CS 843664 A CS843664 A CS 843664A CS 366484 A CS366484 A CS 366484A CS 240878 B1 CS240878 B1 CS 240878B1
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Abstract
Zníženie plynných arzénových exhalátov pri koncentračnom tavení měděných sulfidických koncentrátov sa dosiahne použitím trosiek s prídavkom oxidu vápenatého so zníženým obsahom oxidu křemičitého, pričom celkový obsah troskotvorných přísad a množstvo trosky ostává nezměněné.The reduction of gaseous arsenic exhalates during the concentration smelting of copper sulphide concentrates is achieved by using slags with the addition of calcium oxide and a reduced content of silicon dioxide, while the total content of slag-forming additives and the amount of slag remain unchanged.
Description
Vynález sa týká koncentračného tavenia sulfidických měděných koncentrátov, u ktorého sa rieši zniženie plynných arzénových exhalátov·The invention relates to the concentration melting of sulphide copper concentrates in which the reduction of gaseous arsenic pollutants is solved.
Pri pyrometalurgicksj výrobě médi sa arzén rozděluje medzi kondenzované a plynné produkty koncentračného tavenia a konverto rovania. S odpadnými produktami sa móže arzén dostat do okolia a ohrozit životné prostredie· Pri koncentračnom taveni sa arzén obsiahnutý vo veádzke rozdělí medzi kamienok, odvalovú trosku, úlet a odplyny. Arzén je v odvalovej troske viazaný vo formě stabilných chemických zlúčenín, neohrozujúcich životné prostredie· Arzén v kamienku postupuje do technologickej operácie konvertorovania, kde sa zneškodňuje. Úlet z koncentračného tavenia sa repetuje. Množstvo arzénu, ktoré prechádza pri koncentračnom tavení do odplynov koliše v intervale 50 až 60 % z celkového množstva arzénu, obsiahnutého vo vsádzke. Pri konvertorovaní, vzhladom na vysokú koncentráciu oxidu siřičitého, sa odplyny obvykle využívajú na výrobu kyseliny sírovej a přitom sa zachytí a zneškodni aj unikajúci arzén. Hlavným kanálom úniku arzénu do okolia v procese výroby médi sú teda odplyny z koncentračnáho tavenia. Pri koncentračnom tavení v neintenzifikovaných zariadeniach zatial neexistuje ekonomicky efektivny spósob zachytávania arzénu.In pyrometallurgical media production, arsenic is partitioned between condensed and gaseous concentration melting and converging products. With waste products, arsenic can get into the environment and endanger the environment. · During concentration smelting, arsenic contained in the plant is divided between stone, waste slag, drift and off-gases. Arsenic is bound in the waste slag in the form of stable, environmentally-friendly chemical compounds · Arsenic in the stone is progressing into a technological conversion operation where it is disposed of. The flux from the concentration melting is repeated. The amount of arsenic that passes into the flue gas at concentration range 50 to 60% of the total amount of arsenic contained in the batch at concentration melting. In the conversion process, due to the high concentration of sulfur dioxide, the off-gases are typically used to produce sulfuric acid, while also escaping arsenic is trapped and destroyed. Thus, the main channel of arsenic leakage into the environment in the process of producing media is the off-gases from the concentration melting process. At concentration melting in non-intensified plants, there is no economically effective method of arsenic capture yet.
Vyššie uvedené nedostatky sú odstránené spósobom podlá vynálezu, ktorého podstatou je, že pri koncentračnom taveni sa použijú trosky s obsahom oxidu vápenatého 10 až 20 hmotnostných % a s obsahom oxidu křemičitého 25 až 35 hmotnostných Tým sa dosiahne zvýšenie přechodu arzénu do trosky vo formě stabilného arzsnlčnanu vápenatého, čim sa zniži přechod arzénu do odplynov na 13 až 26 % z arzénu obsiahnutého vo vsádzke.The above-mentioned drawbacks are overcome by the method according to the invention, which consists in using slags with a calcium content of 10 to 20% by weight and a silica content of 25 to 35% by weight in concentrating melting. thereby reducing arsenic transfer to off-gases to 13 to 26% of the arsenic contained in the feed.
- 3Priklad- 3Example
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Na tavenia sa použila sulfidická surovina s priemerným obsahom 31,6 hmotnostných % Cu a 1,82 hmotnostných % Ae. Ďalej sa použil oxid vápenatý v množstve 0,23 kg/kg sulfidickej suroviny a oxid křemičitý v množstve 0,30 kg sulfidickej suroviny· Tavením zmiešanej vsádzky sa ziekal kamienok 9 obsahom 0,86 hmotnostných % As a troska s obsahom 0,45 hmotnostných % As, 12,72 hmotnostných % CaO, 32,85 hmotnostných % SiOg. Do úlatov přešlo 26 % As z celkového obsahu arzénu v sulfidickej surovině.A sulfide feedstock having an average content of 31.6 wt% Cu and 1.82 wt% Ae was used for melting. Furthermore, 0.23 kg / kg of sulphide feedstock and 0.20 kg of sulphide feedstock were used. · Melt 9 mixed with 0.86 wt% As and slag containing 0.45 wt% As, 12.72 wt% CaO, 32.85 wt% SiOg. 26% of As from the total arsenic content of the sulphide feedstock went into the bricks.
PřikladExample
Na tavenie sa použila sulfidická surovina s priemerným obsa hom 31,6 hmotnostných % Cu a 1,82 hmotnostných % As. Ďalej sa použil oxid vápenatý v množstve 0,26 kg/kg sulfidickej suroviny a oxid křemičitý v množstve 0,26 kg/kg sulfidickej suroviny. Tavením zmiešanej vsádzky sa získal kamienok a obsahom 0,98 hmotnostných % As a troska s obsahom 0,58 hmotnostných % As, 19,52 hmotnostných % CaO, 26,15 hmotnostných % SiOg. Do úletov přešlo 13 % As z celkového obsahu arzénu v sulfidickej surovině .A sulfide feedstock with an average content of 31.6 wt% Cu and 1.82 wt% As was used for melting. Further, calcium oxide was used in an amount of 0.26 kg / kg sulfide feedstock and silica in an amount of 0.26 kg / kg sulfide feedstock. Melting of the mixed batch yielded a pebble containing 0.98 wt% As and a slag containing 0.58 wt% As, 19.52 wt% CaO, 26.15 wt% SiOg. Do dusts passed 13% and the total content of arsenic in sulfidic raw material.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS843664A CS240878B1 (en) | 1984-05-17 | 1984-05-17 | The method of reducing gaseous arsenic exhales in the condensation melting of copper concentrators |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS843664A CS240878B1 (en) | 1984-05-17 | 1984-05-17 | The method of reducing gaseous arsenic exhales in the condensation melting of copper concentrators |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CS366484A1 CS366484A1 (en) | 1985-07-16 |
| CS240878B1 true CS240878B1 (en) | 1986-03-13 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS843664A CS240878B1 (en) | 1984-05-17 | 1984-05-17 | The method of reducing gaseous arsenic exhales in the condensation melting of copper concentrators |
Country Status (1)
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| CS (1) | CS240878B1 (en) |
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1984
- 1984-05-17 CS CS843664A patent/CS240878B1/en unknown
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| Publication number | Publication date |
|---|---|
| CS366484A1 (en) | 1985-07-16 |
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