CN102618730A - Process for separating materials containing indium, lead, silver, copper and bismuth - Google Patents

Process for separating materials containing indium, lead, silver, copper and bismuth Download PDF

Info

Publication number
CN102618730A
CN102618730A CN2012100424118A CN201210042411A CN102618730A CN 102618730 A CN102618730 A CN 102618730A CN 2012100424118 A CN2012100424118 A CN 2012100424118A CN 201210042411 A CN201210042411 A CN 201210042411A CN 102618730 A CN102618730 A CN 102618730A
Authority
CN
China
Prior art keywords
copper
bismuth
silver
indium
lead
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN2012100424118A
Other languages
Chinese (zh)
Other versions
CN102618730B (en
Inventor
章震云
陈世民
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yongxing County Huaxin Slicher Solder Co Ltd
Original Assignee
Yongxing County Huaxin Slicher Solder Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yongxing County Huaxin Slicher Solder Co Ltd filed Critical Yongxing County Huaxin Slicher Solder Co Ltd
Priority to CN 201210042411 priority Critical patent/CN102618730B/en
Publication of CN102618730A publication Critical patent/CN102618730A/en
Application granted granted Critical
Publication of CN102618730B publication Critical patent/CN102618730B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Abstract

The invention discloses a process for separating materials containing indium, lead, silver, copper and bismuth. The process includes adding vulcanizer with the weight equal to copper content, from 1 to 10% of adhesive and from 5 to 10% of lime into the processed materials and mixing the vulcanizer, the adhesive and the lime with the processed materials to obtain mixed materials; realizing briquetting forming of the mixed materials under the pressure ranging from 5000KN to 8000KN, placing the mixed materials at the normal temperature for 5 to 10 days after briquetting and forming, and leading block masses to be cured after oxidation reaction of the materials under the high pressure; and feeding the block masses and coke into a shaft furnace to smelt the block masses and the coke at the temperature ranging from 1250 DEG C to 1350 DEG C, and realizing lead, bismuth and silver smelting for produced slag including from 20 to 30% of FeO, from 25 to 35% of SiO2 and from 15 to 25% of CaO to obtain alloy. In the process, the copper is separated and enriched due to the fact that the copper and the iron sulfide are reacted to generate sulfur, and the indium is volatilized and enriched into smoke. The process is simple, and is fine in enrichment effect and high in recycling rate of various metals.

Description

The separating technology that contains the plumbous silver-bearing copper bismuth of indium material
Technical field
The invention belongs to the separation and the beneficiation technologies field of the multiple valuable metal of non-ferrous metal, relate to a kind of employing and make the separating technology that contains the plumbous silver-bearing copper bismuth of indium material that sulfonium divides the plumbous bismuth silver alloy of copper volatilizing and enriching indium melting simultaneously.
Background technology
Have when producing to plant and contain the plumbous silver-colored bismuth copper intermediate material of indium, value height, composition complicacy in the copper-lead smeltery; To its comprehensive recovery is a very complicated technological problems, and tradition is to leach with concentrated hydrochloric acid to reclaim indium copper, replaces copper then and carries extraction recovery indium; But because elements such as containing metal attitude lead bronze bismuths, the leaching yield of indium is low, and the spent acid water yield is also big simultaneously; Environmental protection is had very big pressure, and plumbous and silver remains a kind of intermediate material, does not well reclaim.
Summary of the invention
The object of the present invention is to provide a kind of technology simple, concentration effect is good, the separating technology that contains the plumbous silver-bearing copper bismuth of indium material that various metal recovery rates are high.
Present method comprises the steps:
1, mixing of materials: material adds the vulcanizing agent that copper content is equal to, the 1-10% sticker, and 5-10% lime mixes;
2, normal temperature is pressed group: at normal temperatures; Press down a moulding with fully automatic hydroform machine said mixture material at pressure 5000-8000KN, placed at normal temperatures 5-10 days, wait material under high pressure to carry out oxidizing reaction; Make the agglomerate slaking, intensity does not get final product not pulverize at 1 meter eminence freely falling body;
3, matte stove melting: agglomerate and coke are dropped in the shaft furnace in 1250-1350 ℃ of following melting, and the output slag type is: FeO20-30%, SiO 225-35%, CaO 15-25%.Plumbous bismuth silver melting obtains alloy, and the sulphur in copper and the iron sulphide generates sulfonium makes copper obtain separation and concentration, and the indium volatilizing and enriching is in flue dust.
Wherein: vulcanizing agent is an iron sulphide, the metallic sulfide of lead sulfide;
Material is the lead bullion scum silica frost, the mixture of blister copper blowing slag;
Sticker is a lime, cement, clay, the mixture of iron powder.
The invention has the beneficial effects as follows:
1, multiple one step of valuable metal separation and concentration.Dividing copper to refine plumbous enrichment indium can accomplish in a step, and all metals have all obtained effective recovery.
2, indium enrichment 5-10 times, copper enrichment 2-4 times, plumbous silver-colored bismuth directly obtains alloy, the process energy-conserving and environment-protective.
3, whole process valuable metal direct yield is high, the recovery 90-98% of silver, and plumbous recovery 90-98%, the recovery of copper reaches 95-98%, and the recovery of bismuth reaches 95-98%, indium 85-95%.
Description of drawings:
Fig. 1 is a concrete process flow sheet of the present invention.
Specific embodiment according to technical process shown in the drawings;
1, mixing of materials: material adds the vulcanizing agent that copper content is equal to, the 1-10% sticker, and 5-10% lime mixes;
2, normal temperature is pressed group: at normal temperatures; Press down a moulding with fully automatic hydroform machine said mixture material at pressure 5000-8000KN, placed at normal temperatures 5-10 days, wait material under high pressure to carry out oxidizing reaction; Make the agglomerate slaking, intensity does not get final product not pulverize at 1 meter eminence freely falling body;
3, matte stove melting: agglomerate and coke are dropped in the shaft furnace in 1250-1350 ℃ of following melting, and the output slag type is: FeO 20-30%, SiO 225-35%, CaO 15-25%, plumbous bismuth silver melting obtains alloy, and the sulphur in copper and the iron sulphide generates sulfonium makes copper obtain separation and concentration, and the indium volatilizing and enriching is in flue dust.
Wherein: vulcanizing agent is an iron sulphide, the metallic sulfide of lead sulfide;
Material is the lead bullion scum silica frost, the mixture of blister copper blowing slag;
Sticker is a lime, cement, clay, the mixture of iron powder.
The main chemical reactions formula is:
Me n++O 2→MeO
Me represents Fe, Cu, Pb, Bi etc., and wherein n has different variations according to the valency difference.
The melting of matte stove is under 1250-1350 ℃, in weak oxide atmosphere, and iron and the slag making of calcium silicon; Plumbous bismuth silver then is reduced into metal and becomes to merge gold altogether and emit from the bottom, and then reaction obtains cupric sulfide to copper with iron sulphide, on alloy; Form sulfonium, indium then gets into flue dust as suboxide.
The main chemical reactions formula is:
C+O→CO2
C+O→CO
CO+O2→CO2
Me n++CO→CO2+Me
Cu2O+FeS→CuS+Fe?O
Wherein m, n have different variations according to the valency difference.
This operation is the direct melting of plumbous bismuth silver an alloy then, and electrolysis gets final product the anode sludge of separation of lead and rich bismuth silver, and copper then generates sulfide and send copper metallurgy as the copper raw materials for metallurgy separately; Indium then is enriched in the flue dust with the form of oxide compound, when reclaiming indium, can leach at the low sulfuric acid of acidity; Not only acid consumption is little; The leaching yield of indium is also high, and wastewater flow rate is 1/5th of a traditional process, extracts indium slag afterwards and returns the group's of pressure recovery lead etc.
Obtaining product has: plumbous silver-colored bismuth alloy contains, sulfonium, flue dust, slag, and its composition sees the following form.
The Chemical Composition of various materials (%)
Figure BDA0000137814620000041
Visible by last table: after the present invention's processing, contain the material one step initial gross separation enrichment of the plumbous silver-bearing copper bismuth of indium, plumbous silver-colored bismuth obtains alloy simultaneously; So that subsequent handling reclaims, 5 times of indium enrichments simultaneously, the wastewater flow rate that reclaims indium also reduces 5 times; Reach the purpose of energy-conserving and environment-protective, good economic environmental benefit is arranged.
Fume amount is the 10-20% of add-on in the production.Know that by table 1 indium enrichment 5-10 times, copper enrichment 2-4 times, plumbous silver-colored bismuth directly obtains alloy, the process energy-conserving and environment-protective.Whole process valuable metal direct yield is high, the recovery to 95% of silver, and the plumbous recovery to 90%, the recovery of copper reaches 98%, and the recovery of bismuth reaches 98%, and indium reaches 88%.

Claims (1)

1. separating technology that contains the plumbous silver-bearing copper bismuth of indium material is characterized in that may further comprise the steps:
1), mixing of materials: material adds the vulcanizing agent that copper content is equal to, 1-10% sticker, the mixing of 5-10% lime;
2), normal temperature is pressed group: at normal temperatures; Press down a moulding with fully automatic hydroform machine said mixture material at pressure 5000-8000KN, placed at normal temperatures 5-10 days, wait material under high pressure to carry out oxidizing reaction; Make the agglomerate slaking, intensity does not get final product not pulverize at 1 meter eminence freely falling body;
3), matte stove melting: agglomerate and coke are dropped in the shaft furnace in 1250-1350 ℃ of following melting, and the output slag type is: FeO 20-30%, SiO 225-35%, CaO 15-25%.Plumbous bismuth silver melting obtains alloy, and the sulphur in copper and the iron sulphide generates sulfonium makes copper obtain separation and concentration, and the indium volatilizing and enriching is in flue dust.
Wherein: vulcanizing agent is an iron sulphide, the metallic sulfide of lead sulfide;
Material is the lead bullion scum silica frost, the mixture of blister copper blowing slag;
Sticker is a lime, cement, clay, the mixture of iron powder.
CN 201210042411 2012-02-23 2012-02-23 Process for separating materials containing indium, lead, silver, copper and bismuth Expired - Fee Related CN102618730B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201210042411 CN102618730B (en) 2012-02-23 2012-02-23 Process for separating materials containing indium, lead, silver, copper and bismuth

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201210042411 CN102618730B (en) 2012-02-23 2012-02-23 Process for separating materials containing indium, lead, silver, copper and bismuth

Publications (2)

Publication Number Publication Date
CN102618730A true CN102618730A (en) 2012-08-01
CN102618730B CN102618730B (en) 2013-11-06

Family

ID=46558930

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201210042411 Expired - Fee Related CN102618730B (en) 2012-02-23 2012-02-23 Process for separating materials containing indium, lead, silver, copper and bismuth

Country Status (1)

Country Link
CN (1) CN102618730B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102628103A (en) * 2012-02-23 2012-08-08 永兴县华鑫铅锡有限责任公司 Method for enriching valuable metal from mine tailing and smelting slag by fire method
CN103937988A (en) * 2014-05-04 2014-07-23 云南锡业股份有限公司 Process for producing unpurified silver by pyro-refining precious lead

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55158126A (en) * 1979-05-23 1980-12-09 Nippon Mining Co Ltd Separation of indium from substance leached from indium-containing substance with sulfuric acid
CN1621544A (en) * 2004-12-31 2005-06-01 沈奕林 Comprehensive treating process for indium lead and stibium -containing smelting water quenching residue
CN101078053A (en) * 2007-06-23 2007-11-28 王树楷 Method for extracting metal indium, zinc and bismuth from blast furnace gas ash
CN101255502A (en) * 2008-04-02 2008-09-03 河南豫光金铅股份有限公司 Process for comprehensive recovery of indium, cadmium, thallium and zinc from lead system smoke
CN101525693A (en) * 2009-04-17 2009-09-09 深圳市中金岭南有色金属股份有限公司韶关冶炼厂 Method for vulcanization, reducing oxidation and enrichment of low-grade material containing arsenic, indium and germanium
CN102628103A (en) * 2012-02-23 2012-08-08 永兴县华鑫铅锡有限责任公司 Method for enriching valuable metal from mine tailing and smelting slag by fire method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55158126A (en) * 1979-05-23 1980-12-09 Nippon Mining Co Ltd Separation of indium from substance leached from indium-containing substance with sulfuric acid
CN1621544A (en) * 2004-12-31 2005-06-01 沈奕林 Comprehensive treating process for indium lead and stibium -containing smelting water quenching residue
CN101078053A (en) * 2007-06-23 2007-11-28 王树楷 Method for extracting metal indium, zinc and bismuth from blast furnace gas ash
CN101255502A (en) * 2008-04-02 2008-09-03 河南豫光金铅股份有限公司 Process for comprehensive recovery of indium, cadmium, thallium and zinc from lead system smoke
CN101525693A (en) * 2009-04-17 2009-09-09 深圳市中金岭南有色金属股份有限公司韶关冶炼厂 Method for vulcanization, reducing oxidation and enrichment of low-grade material containing arsenic, indium and germanium
CN102628103A (en) * 2012-02-23 2012-08-08 永兴县华鑫铅锡有限责任公司 Method for enriching valuable metal from mine tailing and smelting slag by fire method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102628103A (en) * 2012-02-23 2012-08-08 永兴县华鑫铅锡有限责任公司 Method for enriching valuable metal from mine tailing and smelting slag by fire method
CN103937988A (en) * 2014-05-04 2014-07-23 云南锡业股份有限公司 Process for producing unpurified silver by pyro-refining precious lead

Also Published As

Publication number Publication date
CN102618730B (en) 2013-11-06

Similar Documents

Publication Publication Date Title
CN102776376B (en) Method for recovering valuable metal from waste residue containing lead and zinc through wet-fire combination process
CN104263965B (en) The method that gold and lead are reclaimed in difficult-treating gold mine collocation lead containing sludge raw material oxygen enriched molten bath melting
CN104278162B (en) A kind of antimonial lead complex materials selectivity fused bath smelting method
CN103667712B (en) A kind of method of the leaded and synchronous bath smelting of copper-bearing waste material
CN102433439B (en) Method for recovering rhenium from arsenic filter cake
US11293076B2 (en) Method for preparing iron ore concentrates by recycling copper slag tailings
CN102051478B (en) Wet process for treating lead copper matte
US20180282837A1 (en) Method for extracting metals from concentrated sulphurated minerals containing metals by direct reduction with regeneration and recycling of the reducing agent, iron, and of the flux, sodium carbonate
CN103320614B (en) A kind of lead matte pyrogenic attack technique
CN106086413B (en) A kind of technique of zinc hydrometallurgy lead smelting gas recycling
CN103266225A (en) Side-blown furnace reduction smelting technology for lead anode mud
CN108823425A (en) A kind of difficult-treating gold mine fused-extracting enrichment Method for extracting gold
CN106834720B (en) A kind of method that arsenic-containing smoke dust integrated treatment and regulation growth method synthesize solid arsenic mineral
CN110777264A (en) Method suitable for independent smelting of various complex gold concentrates
CN105132694B (en) Comprehensive recovery method of tailings containing precious metals
CN1323177C (en) High Iron zinc calcine process method
CN104046782A (en) Method for recycling industrial waste material containing tungsten and iron and low-grade refractory ferberite
CN106834709B (en) The method that a kind of comprehensive utilization of arsenic-containing smoke dust and precipitation transformation method synthesize solid arsenic mineral
CN104004907A (en) Method for separating copper from lead matte and comprehensively utilizing lead matte
CN109207726A (en) From low-grade containing the method for recycling antimony gold in golden antimony sulfide ore
CN102618730B (en) Process for separating materials containing indium, lead, silver, copper and bismuth
US4135912A (en) Electric smelting of lead sulphate residues
CN109735703B (en) Method for extracting lead, zinc and silver from lead-zinc-silver composite sulfide ore
CN104388980A (en) Method for extracting gold from difficultly treated gold ore
CN108048651B (en) A kind of method of the complicated high silver ore of synthetical recovery

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20131106

Termination date: 20170223

CF01 Termination of patent right due to non-payment of annual fee