CN1167833A - Integrated recovery of Pb and Sn as valuable metal from chloride slag - Google Patents
Integrated recovery of Pb and Sn as valuable metal from chloride slag Download PDFInfo
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- CN1167833A CN1167833A CN97103222A CN97103222A CN1167833A CN 1167833 A CN1167833 A CN 1167833A CN 97103222 A CN97103222 A CN 97103222A CN 97103222 A CN97103222 A CN 97103222A CN 1167833 A CN1167833 A CN 1167833A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
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Abstract
A method for comprehensive recovering of valuable metals from chloridized slags which are generated by wet extraction of Au and Ag includes cyanidation to extract Au, ammonium carbonate conversion to remove Pb, retailoring, etc. and features reasonable combination of said techniques and proper selection of technological parameters. Its advantages are use of cheap reagent and conventional apparatus, direct extraction of Pb, Sn, alloy, Ag, Au, etc. less environmental pollution, and high utilization rate of chloridized slags.
Description
The present invention relates to the refinement of non-ferrous metals such as gold and silver and slicker solder.
Smeltery's wet method is extracted gold and silver and is obtained a kind of golden 150g/t that contains later on, and the leached mud of argentiferous below 0.25% is called chloride slag traditionally.This slag is difficult to carry out the further processing of former technology, often causes the pollution of environment and occupies the factory building useful space.Except wherein gold and silver still can extract the recovery, also have valuable metals such as a large amount of lead, antimony, tin to utilize.The factory that has is added to the plumbous smelting procedure of blister copper with this chloride slag as copper-lead smeltery batching, and the valuable metal internal circulating load increases as a result, and loss increases.
The objective of the invention is to overcome the deficiencies in the prior art part, propose a kind of comprehensive recycling process, with comprehensive recovery of gold silver and Pb and Sn as valuable metal effectively from chloride slag.Utilize the inventive method, both can obtain significant direct economic benefit, environmental pollution is less again.
Technical scheme of the present invention is reasonably to make up to utilize prior art, comprises that extraction of gold by cyanidation, volatile salt transform deleading, retailoring etc., and suitably select for use processing parameter to handle chloride slag.
Feature of the present invention is that following operation is arranged:
A. chloride slag adds lime control pH 9～11 after residual acid is gone in washing, pulp density 20～30%, and NaCN concentration 0.1～0.2% leached 24～26 hours, and with zinc dust precipitation, gold and silver reclaims in the displacement gold mud after the cyanating solution deoxidation;
B. cyanidation tailings is after remaining prussiate is removed in washing, Gu at liquid/than (liquid/solid ratio, mg/mL of unit or kg/L) 2～6: 1,1.1～3 times of volatile salts of theoretical amount, agitation leach is 1～8 hour under 15～40 ℃ of conditions of temperature, leach liquor discards or the reclaim(ed) sulfuric acid ammonium, admittedly leached mud is at liquid/than 2～6: 1,1.1～2 times of rare nitric acid of theoretical amount, agitation leach is 1～8 hour under 80～90 ℃ of conditions of temperature, and lead is transformed into lead nitrate and enters leach liquor, the latter adds the sulfuric acid of calculated amount, precipitated sulfur lead plumbate and rare nitric acid of regenerating return use, and the The product sulfur lead plumbate also can convert the Chemicals or the lead bullion of corresponding lead again to; The also available following method of this cyanidation tailings is handled, admittedly promptly at liquid/than 8～10: 1, under 80～90 ℃ of conditions of temperature, agitation leach is 2～3 hours in the 20%NaOH solution, reclaims lead bullion from leach liquor, i.e. 3V at room temperature, 100～120A/cm
2The direct current electrodeposition is 12～14 hours under the condition, the output lead bullion;
Admittedly C. take off lead skim at liquid/than 2～8: 1,4.0～5.5M HCl concentration, agitation leach is 1～8 hour under 80～90 ℃ of conditions of temperature, and antimony, bismuth, copper enter leach liquor, reclaim it with traditional method, and when antimony in the raw material does not account for when leading, this operation can be cancelled;
D. taking off antimony slag (or taking off lead skim) allocates material into and weighs 5～15% coal dusts, 5～15% lime powders, 5～10% boraxs, in reduction or weak oxide atmosphere electric furnace or coke stove or reverberatory furnace, melting is 15～60 minutes under 1100～1300 ℃ of conditions, obtains the Sn-Pb-Sb alloy, this alloy also enrichment the gold and silver in the raw material, obtain the stanniferous slag simultaneously, alloy can further be processed into product, and the tin slag send tin-smelting plant to reclaim.
In the D operation, also can add 0～5% glass powder.
Compare with prior art, the present invention has following advantage:
1. directly obtain lead with quite cheap reagent and conventional equipment from chloride slag, useful Chemicals such as tin and alloy, and gold and silver, direct economic benefit is remarkable.
2. process exhaust gas discharged, waste water are few, and waste residue is utilized effectively, and environmental benefit is better.
Embodiment 1
The chloride slag of certain factory's following ingredients (wt.%): Au 0.01367, Ag 0.25, and Cu 0.17, and Pb 22.78, Sb 6.30, Sn 17.37, after residual acid is gone in washing, add lime control pH to 9, pulp density 20%, with concentration is that 0.1% NaCN leached 24 hours, and with zinc dust precipitation, gold and silver reclaims in the displacement gold mud after the cyanating solution deoxidation; After extracting gold and silver, obtain the cyanidation tailings (wt.%) of following ingredients: Au26 g/t, Ag 0.16, and Cu 0.66, and Pb 22.29, and Sb 4.21, Sn 17.59.
Admittedly above-mentioned cyanidation tailings is at liquid/than 2.5: 1,2 times of volatile salts of theoretical amount, agitation leach is 2 hours under 30 ℃ of conditions of temperature, filters, soak slag with hot water wash to the no SO of check
4 =Admittedly filter residue is at liquid/than 2.5: 1,2 times of rare nitric acid of theoretical amount, agitation leach is 2 hours under 80 ℃ of conditions of temperature, filters, hot water wash is to neutral, obtain the leach liquor of leaded 62g/L, plumbous leaching yield 80%, the filter residue composition is (wt.%): Ag 0.274, Pb 6.89, Sb 7.95, and Sn 27.03, and Cu 0.37. sulfuric acid precipitation with calculated amount from leach liquor goes out lead sulfate and reclaims rare nitric acid.
Take off lead skim with 8% coal dust, 8% lime powder, 8% borax and 4% glass powder, 1200 ℃ of following meltings are 15 minutes in electric furnace, the Sn-Pb-Sb alloy (wt.%) of output following ingredients: Au 100 (g/t), and Ag 1.01, Sn 62.0, Pb 15.1, and Sb 16.0, and Cu 2.84. is the silicate slag of output stanniferous 7.26% simultaneously.The rate of recovery 75.78% of tin in alloy, the rate of recovery 13.41% in slag, total yield 89.19%.
Embodiment 2
With the chloride slag of embodiment 1, after the washing, pulp density 25% adds lime and regulates pH to 11, and NaCN concentration 0.2% stirs fills air leaching 26 hours, reclaims gold and silver with zinc dust precipitation after the filtrate deoxidation.Filter residue is cleaned back composition (wt.%): Au 38 (g/t), and Ag 0.14, and Cu 0.11, and Pb 25.20, and Sb 4.86, and Sn 18.03, Al
2O
315.76, SiO
213.4. this cyanidation tailings in that liquid/admittedly than 10: 1, under 90 ℃ of conditions of temperature, agitation leach was 2 hours in the 20%NaOH solution, plumbous leaching yield 88.2% reclaims lead bullion, promptly at room temperature 3V, 100A/cm from leach liquor
2The direct current electrodeposition is 12 hours under the condition, leaded 70% lead bullion of output, and lead slag-removed composition (wt.%): Au 39.5 (g/t), Ag 0.16, and Pb 4.48, and Sb 7.26, Sn 29.85.
The 1300 ℃ of meltings 10 minutes in intermediate frequency furnace of lead slag-removed 10% coal dust that is equipped with, 16% lime powder, 10% borax, the output crude tin alloy, its composition (wt.%) is; Sn 56.1, and Sb 13.5, Pb 8.4.
Embodiment 3
With the chloride slag of embodiment 1, by the described same procedure of embodiment 1 handle obtain cyanidation tailings after, admittedly at liquid/than 5: 1,2 times of volatile salts of theoretical amount, agitation leach is 2 hours under 15 ℃ of conditions of temperature, press embodiment 1 described same procedure processing.Plumbous leaching yield 74.5%, lead slag-removed composition (wt.%) is: Ag 0.366, Pb 8.95, Sb7.56, and Sn 30.67, Cu 0.43. takes off lead skim again by embodiment 1 described same procedure melting, obtain Sn-Pb-Sb alloying constituent (wt.%): Ag 1.22, and Pb 20.8, and Sb 15.4, Sn 55.8, Cu 2.77. tin slag stanniferous 6.93%.
Claims (2)
1, a kind of from chloride slag the method for integrated recovery of Pb and Sn as valuable metal, comprise that extraction of gold by cyanidation, volatile salt transform deleading, retailoring etc., feature of the present invention is that following concrete operation is arranged:
A. chloride slag adds lime control pH9～11 after residual acid is gone in washing, pulp density 20～30%, and NaCN concentration 0.1～0.2% leached 24～26 hours, and with zinc dust precipitation, gold and silver reclaims in the displacement gold mud after the cyanating solution deoxidation;
B. cyanidation tailings is after remaining prussiate is removed in washing, Gu at liquid/than (liquid/solid ratio, mg/mL of unit or kg/L) 2～6: 1,1.1～3 times of volatile salts of theoretical amount, agitation leach is 1～8 hour under 15～40 ℃ of conditions of temperature, leach liquor discards or the reclaim(ed) sulfuric acid ammonium, admittedly leached mud is at liquid/than 2～6: 1,1.1～2 times of rare nitric acid of theoretical amount, agitation leach is 1～8 hour under 80～90 ℃ of conditions of temperature, and lead is transformed into lead nitrate and enters leach liquor, the latter adds the sulfuric acid of calculated amount, precipitated sulfur lead plumbate and rare nitric acid of regenerating return use, and the The product sulfur lead plumbate also can convert the Chemicals or the lead bullion of corresponding lead again to; Perhaps, the also available following method of this cyanidation tailings is handled, admittedly promptly at liquid/than 8～10: 1, under 80～90 ℃ of conditions of temperature, agitation leach is 2～3 hours in the 20%NaOH solution, reclaims lead bullion from leach liquor, i.e. 3V at room temperature, 100～120A/cm
2The direct current electrodeposition is 12～14 hours under the condition, the output lead bullion;
Admittedly C. take off lead skim at liquid/than 2～8: 1,4.0～5.5 M HCl concentration, agitation leach is 1～8 hour under 80～90 ℃ of conditions of temperature, and antimony, bismuth, copper enter leach liquor, reclaim it with traditional method, and when antimony in the raw material does not account for when leading, this operation can be cancelled;
D. taking off antimony slag (or taking off lead skim) allocates material into and weighs 5～15% coal dusts, 5～15% lime powders, 5～10% boraxs, in reduction or weak oxide atmosphere electric furnace or coke stove or reverberatory furnace, melting is 15～60 minutes under 1100～1300 ℃ of conditions, obtains the Sn-Pb-Sb alloy, this alloy also enrichment the gold and silver in the raw material, obtain the stanniferous slag simultaneously, alloy can further be processed into product, and the tin slag send tin-smelting plant to reclaim.
2,, it is characterized in that also can allocating in the antimony slag (or taking off lead skim) glass powder of material heavy 0～5% taking off of step D according to the method for claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97103222A CN1048289C (en) | 1997-03-26 | 1997-03-26 | Integrated recovery of Pb and Sn as valuable metal from chloride slag |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97103222A CN1048289C (en) | 1997-03-26 | 1997-03-26 | Integrated recovery of Pb and Sn as valuable metal from chloride slag |
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| Publication Number | Publication Date |
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| CN1167833A true CN1167833A (en) | 1997-12-17 |
| CN1048289C CN1048289C (en) | 2000-01-12 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN97103222A Expired - Fee Related CN1048289C (en) | 1997-03-26 | 1997-03-26 | Integrated recovery of Pb and Sn as valuable metal from chloride slag |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102002596A (en) * | 2010-11-17 | 2011-04-06 | 江西稀有金属钨业控股集团有限公司 | Process for reclaiming bismuth and silver from bismuth refining slag |
| CN104178629A (en) * | 2013-05-23 | 2014-12-03 | 汨罗市绿岩金属有限公司 | Method of recovering valuable metals from waste electronic circuit board multi-metal powder |
| CN104388680A (en) * | 2014-10-16 | 2015-03-04 | 中国科学院合肥物质科学研究院 | Method for recovering thallium from lead and lithium alloy |
| CN104419836A (en) * | 2013-09-02 | 2015-03-18 | 侯连东 | Novel gold reducing agent and use method thereof |
| CN109022812A (en) * | 2018-10-24 | 2018-12-18 | 郴州市金贵银业股份有限公司 | A method of refined bismuth and refined copper are recycled from high-copper bismuth slag |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1045796C (en) * | 1996-09-16 | 1999-10-20 | 昆明贵金属研究所 | Extraction of gold, silver and valued metals from arsenic-and copper-bearing anode sludge |
-
1997
- 1997-03-26 CN CN97103222A patent/CN1048289C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102002596A (en) * | 2010-11-17 | 2011-04-06 | 江西稀有金属钨业控股集团有限公司 | Process for reclaiming bismuth and silver from bismuth refining slag |
| CN102002596B (en) * | 2010-11-17 | 2012-11-07 | 江西稀有金属钨业控股集团有限公司 | Process for reclaiming bismuth and silver from bismuth refining slag |
| CN104178629A (en) * | 2013-05-23 | 2014-12-03 | 汨罗市绿岩金属有限公司 | Method of recovering valuable metals from waste electronic circuit board multi-metal powder |
| CN104178629B (en) * | 2013-05-23 | 2017-05-31 | 汨罗市绿岩金属有限公司 | The method that valuable metal is reclaimed from many metal dusts of waste electronic wiring board |
| CN104419836A (en) * | 2013-09-02 | 2015-03-18 | 侯连东 | Novel gold reducing agent and use method thereof |
| CN104419836B (en) * | 2013-09-02 | 2018-02-09 | 侯连东 | A kind of new golden reducing agent and its application method |
| CN104388680A (en) * | 2014-10-16 | 2015-03-04 | 中国科学院合肥物质科学研究院 | Method for recovering thallium from lead and lithium alloy |
| CN104388680B (en) * | 2014-10-16 | 2016-09-07 | 中国科学院合肥物质科学研究院 | The recovery method of thallium in a kind of lead lithium alloy |
| CN109022812A (en) * | 2018-10-24 | 2018-12-18 | 郴州市金贵银业股份有限公司 | A method of refined bismuth and refined copper are recycled from high-copper bismuth slag |
| CN109022812B (en) * | 2018-10-24 | 2020-02-11 | 郴州市金贵银业股份有限公司 | Method for recovering refined bismuth and refined copper from high-copper bismuth slag |
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|---|---|
| CN1048289C (en) | 2000-01-12 |
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Free format text: CORRECT: PATENTEE; FROM: KUNMING INSTITUTE OF PRECIOUS METALS TO: GUIYAN PLATIUM CO., LTD. |
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Address after: Walnut, two ring road, Yunnan, Kunming Patentee after: Guiyan Platinum Industry Co., Ltd. Patentee before: Kunming Institute of Precious Metals |
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Owner name: YUNNAN KAIYUAN GOLD LAKE RARE METAL LIMITED LIABI Free format text: FORMER OWNER: GUIYAN PLATIUM CO., LTD. Effective date: 20020401 |
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Effective date of registration: 20020401 Address after: 661600 Yunnan Province, Kaiyuan city, Honghe Prefecture small Longtan Lu Yuehua Patentee after: Yunnan Kaiyuan Jintan Rare Metal Co. Ltd. Address before: 650221, Yunnan Kunming Second Ring Road walnut head: Bullock Patentee before: Guiyan Platinum Industry Co., Ltd. |
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