CN101845642A - Process for refining and purifying silver - Google Patents
Process for refining and purifying silver Download PDFInfo
- Publication number
- CN101845642A CN101845642A CN201010176583A CN201010176583A CN101845642A CN 101845642 A CN101845642 A CN 101845642A CN 201010176583 A CN201010176583 A CN 201010176583A CN 201010176583 A CN201010176583 A CN 201010176583A CN 101845642 A CN101845642 A CN 101845642A
- Authority
- CN
- China
- Prior art keywords
- silver
- mother liquor
- refining
- mother solution
- electrolyzer
- 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.)
- Pending
Links
Images
Landscapes
- Manufacture And Refinement Of Metals (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
The invention discloses a process for refining and purifying silver, which comprises the following steps of: sampling and detecting a raw material, determining the distribution conditions of metal elements in the raw material, preparing mother solution in an electrolysis bath, adding a fixed quantity of silver into the mother solution while preparing the mother solution, and keeping the silver content between 50 and 70 percent per liter; adding a fixed quantity of acid into the mother solution, and keeping the acidity at 5 grams per liter; circulating the mother solution in the bath; smelting coarse silver into water flower silver of small and uniform granules, and regulating and controlling the output current according to the detection result of a fed material during electrolytic refining; when other valuable metal elements are increased and a single metal element exceeds the standard, purifying the mother solution; pumping the mother solution into a purification device to perform stirring, adding KOH agent into the purification device to perform reaction, putting back the upper clarified solution into the electrolysis bath, and adding a fixed quantity of acid into the electrolysis bath to use the clarified solution normally; refining a resolved electrolytic silver finished product, collecting silver powder, putting the silver powder into a centrifuge to perform cleaning, and adding diluted acid into the centrifuge according to the condition of the silver powder; and after the silver powder is cleaned by using clean water, drying the silver powder to obtain 99.995 percent electrolytic silver finished product.
Description
Technical field
The invention belongs to the silver refining and purify, specifically be meant the processing method that a kind of elementary silver-colored refining is purified.
Background technology
The various valuable metal elements that contain in the thick silver of regenerating are more, and content is comparatively inhomogeneous.Wherein the more valuable metal of content includes: Fe, Ca, Pd, Ni, Zn etc., the content of this class low level metal in thick silver is higher, relatively good management and control when refining is purified.Another kind of is the low rare precious metal of content, includes: Pd, Sb, Se, Te, Bi etc., and the content of this metalloid element is very rare, but because of its characteristic of elements, the influence to the refined product quality in electrorefining is purified production is very big, also difficult to govern control.
Summary of the invention
The object of the present invention is to provide a kind of different potentials attribute by metallic element, in media liquid, the differing appearance behavior of Haas electric current is carried out that thick silver-colored primary raw materials is carried out refining by the metallic element ion and purify a kind of degree of depth purification process of the valuable metal material that is contained in the separation of Silver.
In order to achieve the above object, concrete processing method of the present invention is as follows;
At first, determine to contain in the raw material distribution situation of metallic element, in electrolyzer, prepare mother liquor, add quantitative silver during the preparation of mother liquor the detection of taking a sample of former material; To improve the silver ion content in the mother liquor, silver content remains on 50%-70%/L; Add quantitative acid, to improve free acid content in the mother liquor, acidity remains on 5g/L; The ON cycle system allows mother liquor circulate in groove after deployed; Thick silver is smelted into the little and uniform spray silver of particle, promptly drops into electrorefining in the electrolyzer, when electrorefining, outward current is regulated and control according to the detected result of throwing material; Be voltage control electric current or electric current control voltage; Adjustment enters the galvanic current in the groove; Along with the lengthening of life cycle, other valuable metal elements in the mother liquor also increase, and when exceeding standard if any single metallic element, just need carry out purifying treatment to mother liquor; Stirring in the mother liquor suction refining plant, add the reaction of KOH medicament, other metals of the major part in its mother liquor generate silver suboxide postprecipitations, and supernatant liquid can be put back to and add quantitative acid in the electrolyzer and just can normally use; The finished product electrolytic silver silver powder that refining parses collects, and puts into whizzer and cleans, and the situation according to silver powder during cleaning adds diluted acid; Add boiling water and clean the back drying, obtain 99.995% finished product electrolytic silver powder.
The silver suboxide that purify to produce in electrorefining production adds to contain and is made into silver soil after the reaction of CL ionic medicament generates AgCL, is smelted into spray silver and drops into electrolysis in the electrolyzer; The waste water adding that produces when cleaning contains the reaction of CL ionic medicament and generates the AgCL precipitation, takes out AgCL and is made into silver-colored soil, is smelted into spray silver and drops into electrolysis in the electrolyzer.
Adopt the processing method of invention, on the refining of thick silver is purified, purified finished product electrolytic silver powder reach 99.995% high-quality; And institute is a small amount of argentiferous waste material of generation in refining purify to be produced; Silver-containing waste water can return in the refining production link by recovery method; Other metals then are discharged into liquid waste treatment system, also can all reclaim.
Description of drawings
The processing method process flow sheet that accompanying drawing is purified for the refining of the present invention's silver.
Embodiment
The invention will be further described below in conjunction with accompanying drawing: at first thick silver sampling detects, and grasps the amount of other metallic elements in the material; The deployed mother liquor that is used for electrorefining is held the content of silver ions in the mother liquor, the acidity of mother liquor during the mother liquor preparation; Handle ionic content etc. in the mother liquor; Melted spray silver is dropped into electrolysis in the electrolyzer, adjust the electric current way of output of rectifier during electrolysis according to detected result; Electric current control voltage or voltage control electric current are controlled the parsing quality and the speed of silver ions; Mother liquor generation heat causes the acid volatilization in the mother liquor during because of production, adds the suitable electrorefining demand of content that quantitative acid guarantees free acid in the mother liquor; The increase of mother liquor duration of service, other metallic elements in its mother liquor also increase, if there is single-element to exceed standard, mother liquor just needs purifying treatment, add KOH medicament stirring reaction during mother liquor purification, precipitate upper strata, limpid back liquid and return in the electrolyzer, add quantitative acid and just can use; The silver suboxide that is settled out adds the medicament reaction generation AgCL that contains CL after adding the acid dissolving, and AgCL is made into silver soil, is smelted into spray silver and drops into electrorefining in the electrolyzer; Put into whizzer after the finished product electrolytic silver powder produced is collected and clean, with pure water clean to repeatedly do not have a nitrate radical till, dewatered and washed obtains 99.995% finished product electrolytic silver powder; The waste water that produces during cleaning adds and contains CL ionic medicament reaction generation AgCL precipitation., AgCL is made into silver soil, be smelted into electrorefining in the spray silver input electrolyzer.
Claims (2)
1. processing method that silver-colored refining is purified is characterized in that concrete processing method is: at first the detection of taking a sample of former material, determine to contain in the raw material distribution situation of metallic element; Prepare mother liquor in electrolyzer, add quantitative silver during the preparation of mother liquor, to improve the silver ion content in the mother liquor, silver content remains on 50%-70%/L; Add quantitative acid, to improve free acid content in the mother liquor, acidity remains on 5g/L; The ON cycle system allows mother liquor circulate in groove after deployed; Thick silver is smelted into the little and uniform spray silver of particle, promptly drops into electrorefining in the electrolyzer, when electrorefining, outward current is regulated and control according to the detected result of throwing material; Be voltage control electric current or electric current control voltage; Adjustment enters the galvanic current in the groove; Along with the lengthening of life cycle, other valuable metal elements in the mother liquor also increase, and when exceeding standard if any single metallic element, just need carry out purifying treatment to mother liquor; Stirring in the mother liquor suction refining plant, add the reaction of KOH medicament, other metals of the major part in its mother liquor generate silver suboxide postprecipitations, and supernatant liquid can be put back to and add quantitative acid in the electrolyzer and just can normally use; The finished product electrolytic silver silver powder that refining parses collects, and puts into whizzer and cleans, and the situation according to silver powder during cleaning adds diluted acid; Add boiling water and clean the back drying, obtain 99.995% finished product electrolytic silver powder.
2. the processing method of purifying according to the described silver-colored refining of claim 1 is characterized in that: purify the silver suboxide that produces and add to contain and be made into silver soil after the reaction of CL ionic medicament generates AgCL in electrorefining production, be smelted into spray silver and drop into electrolysis in the electrolyzer; The waste water adding that produces when cleaning contains the reaction of CL ionic medicament and generates the AgCL precipitation, takes out AgCL and is made into silver-colored soil, is smelted into spray silver and drops into electrolysis in the electrolyzer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201010176583A CN101845642A (en) | 2010-05-14 | 2010-05-14 | Process for refining and purifying silver |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201010176583A CN101845642A (en) | 2010-05-14 | 2010-05-14 | Process for refining and purifying silver |
Publications (1)
Publication Number | Publication Date |
---|---|
CN101845642A true CN101845642A (en) | 2010-09-29 |
Family
ID=42770458
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201010176583A Pending CN101845642A (en) | 2010-05-14 | 2010-05-14 | Process for refining and purifying silver |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101845642A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102605389A (en) * | 2012-03-14 | 2012-07-25 | 云南驰宏锌锗股份有限公司 | Low consumption efficient method for washing and drying of electrolytic silver powder |
CN105525310A (en) * | 2015-11-04 | 2016-04-27 | 陕西瑞凯环保科技有限公司 | Method for recovering silver from silver-containing waste materials |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6033320A (en) * | 1983-08-04 | 1985-02-20 | Nippon Mining Co Ltd | Recovery of high-purity silver from copper-electrolytic precipitate |
WO1987005591A1 (en) * | 1986-03-17 | 1987-09-24 | Eastman Kodak Company | Preparation of ultra-pure silver nitrate |
WO1998058089A1 (en) * | 1997-06-16 | 1998-12-23 | Mitsubishi Materials Corporation | Method for smelting noble metal |
RU2280086C2 (en) * | 2004-10-18 | 2006-07-20 | ОАО "Горно-металлургическая компания "Норильский никель" | Refined silver producing method |
CN1932083A (en) * | 2005-09-16 | 2007-03-21 | 灵宝市金源桐辉精炼有限责任公司 | Silver electrolyzing process |
CN1940141A (en) * | 2006-09-22 | 2007-04-04 | 江西铜业集团公司贵冶分公司 | Non-copper ionic-silver electrolyzation |
CN1974860A (en) * | 2006-11-10 | 2007-06-06 | 湖南省鑫达银业有限公司 | High purity silver preparing electrolysis process |
-
2010
- 2010-05-14 CN CN201010176583A patent/CN101845642A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6033320A (en) * | 1983-08-04 | 1985-02-20 | Nippon Mining Co Ltd | Recovery of high-purity silver from copper-electrolytic precipitate |
WO1987005591A1 (en) * | 1986-03-17 | 1987-09-24 | Eastman Kodak Company | Preparation of ultra-pure silver nitrate |
WO1998058089A1 (en) * | 1997-06-16 | 1998-12-23 | Mitsubishi Materials Corporation | Method for smelting noble metal |
RU2280086C2 (en) * | 2004-10-18 | 2006-07-20 | ОАО "Горно-металлургическая компания "Норильский никель" | Refined silver producing method |
CN1932083A (en) * | 2005-09-16 | 2007-03-21 | 灵宝市金源桐辉精炼有限责任公司 | Silver electrolyzing process |
CN1940141A (en) * | 2006-09-22 | 2007-04-04 | 江西铜业集团公司贵冶分公司 | Non-copper ionic-silver electrolyzation |
CN1974860A (en) * | 2006-11-10 | 2007-06-06 | 湖南省鑫达银业有限公司 | High purity silver preparing electrolysis process |
Non-Patent Citations (1)
Title |
---|
余建民: "《贵金属分离与精炼工艺学》", 31 August 2006, article "贵金属分离与精炼工艺学", pages: 159 - 162 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102605389A (en) * | 2012-03-14 | 2012-07-25 | 云南驰宏锌锗股份有限公司 | Low consumption efficient method for washing and drying of electrolytic silver powder |
CN105525310A (en) * | 2015-11-04 | 2016-04-27 | 陕西瑞凯环保科技有限公司 | Method for recovering silver from silver-containing waste materials |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101508426B (en) | Method for separating tellurium from tellurium slag | |
CN101575715B (en) | Method for extracting valuable metals from electronic waste | |
CN101942568B (en) | Method for recovering noble metal from waste computer and fittings thereof | |
CN103757421B (en) | The extracting method of rare precious metal in platinum palladium mud | |
CN102345140B (en) | Method for electrowinning and recovering silver from silver-containing waste catalyst | |
CN104046785A (en) | Method for processing waste copper/iron-based diamond tool bit | |
CN101514396A (en) | Method for separating tin and stibium from tin-lead anode slime | |
JP6011809B2 (en) | Method for producing gold powder with high bulk density | |
WO2011063577A1 (en) | Method of washing anode slime from lead-bismuth alloy electrolysis | |
CN103695636A (en) | Preparation method of electrolytic manganese dioxide | |
CN103572322A (en) | Method for recycling gold and copper from copper-containing oxidization gold ores | |
CN102433443A (en) | Method for recycling copper from electroplating sludge and electroplating wastewater | |
CN104108740B (en) | A kind of novel method of selectivity production high-quality copper sulfate from copper-bearing waste material | |
JP2009035801A (en) | Method for producing copper | |
CN106757179A (en) | A kind of cupric electrolysis tail washings purifies the process of decopper(ing) removal of impurities | |
CN102031371B (en) | Method for enriching germanium from wet process zinc smelting system | |
CN106282569A (en) | A kind of copper-cadmium slag puies forward the method for cadmium residue resource reclaim | |
CN106978538B (en) | Treatment method of high-bismuth lead anode mud or bismuth slag | |
CN106834691A (en) | A kind of copper anode mud wet-treating comprehensive recycling process | |
CN101845642A (en) | Process for refining and purifying silver | |
JP2010196140A (en) | Method for recovering bismuth | |
CN102260798A (en) | Method for recovering silver and bismuth in silver-zinc slags | |
CN101824546B (en) | Method for recovering silver from lead-separating liquid of silver-separating residue of copper anode slime | |
CN102776386B (en) | Method for recycling stannic oxide from tin-containing lead slag | |
CN102888624A (en) | Method for producing superfine zinc powder by performing cyclone electrolyzing on zinc-containing alkali liquor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20100929 |