CN105350017A - Method increasing rate of filtration of desorbed and electrolyzed gold mud - Google Patents
Method increasing rate of filtration of desorbed and electrolyzed gold mud Download PDFInfo
- Publication number
- CN105350017A CN105350017A CN201510852373.6A CN201510852373A CN105350017A CN 105350017 A CN105350017 A CN 105350017A CN 201510852373 A CN201510852373 A CN 201510852373A CN 105350017 A CN105350017 A CN 105350017A
- Authority
- CN
- China
- Prior art keywords
- gold mud
- filtration
- desorbed
- gelatin
- mud
- Prior art date
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Classifications
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/20—Electrolytic production, recovery or refining of metals by electrolysis of solutions of noble metals
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B11/00—Obtaining noble metals
- C22B11/04—Obtaining noble metals by wet processes
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
- C22B3/22—Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
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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
- Y02P10/20—Recycling
Abstract
The invention discloses a method increasing the rate of filtration of desorbed and electrolyzed gold mud. According to the method, gelatin and polyethyleneglycol are added into a desorbed and electrolyzed gold mud solution and then are fully stirred and mixed. After the gelatin and the polyethyleneglycol are added and fully stirred and mixed, the rate of filtration of the desorbed and electrolyzed gold mud solution is increased. Water is added into the gelatin to prepare a saturated solution. The method can remarkably increase the rate of filtration of desorbed and electrolyzed gold mud, shorten the refining working time and reduce energy consumption.
Description
Technical field
The present invention relates to a kind of method improving filtration velocity, particularly a kind of method improving desorbing electrolytic gold mud filtration velocity.
Background technology
People just started as far back as 1880 from gold-containing solution, to reclaim gold and silver with gac.But as a kind of novel process of gold of carrying until 20 century 70s are just developed rapidly and reach perfection.Since U.S.'s Homestake carbon pulp factory in 1973 is gone into operation, carbon-in-pulp process technique has worldwide become the main gold extracting method of the one generally adopted at present.
Carbon-in-pulp process is the gold utilizing charcoal absorption to leach, and after desorbing electrolytic, the gold mud of generation obtains ingot through refining again.When electrolysis, the material that negative electrode is conventional has steel wool and activated carbon fiber (charcoal felt).Carbon fibe has strengthening electrolytic deposition process, improves cathode current density, under identical electrolytic condition, much higher during the deposition rate of recovery and speed ratio steel wool with carbon fiber gold; Because carbon fiber is noble electrode, unlike steel wool, participate in redox reaction, so electrodeposition gold mud foreign matter content is out few.Based on these advantages of carbon fiber, increasing manufacturing enterprise by carbon fiber for the production of in.But be through carbon fiber electrically and amass the gold mud obtained, usually run into the problem being difficult to filter when subsequent wet refining, filtration time is short then several hours, long then tens hours.The reason of gold mud filtration difficulty, except there being gold loaded carbon not wash clean clearly, carry in the thin mud to gold mud of a part outside producing, topmost reason is that the extremely fine carbon fiber mixed in gold mud causes.Gold mud filtration difficulty causes refinery activities length consuming time, causes personnel, equipment fatigue, adds energy consumption, also bring certain hidden danger to safeguarding work simultaneously.Therefore, study a kind of method to solve desorbing electrolytic gold mud to filter difficult problem be very necessary.
Summary of the invention
The object of the present invention is to provide a kind of method improving desorbing electrolytic gold mud filtration velocity, solve the problem of gold mud filtration difficulty, shorten refining time, improve working efficiency.
The method of the present invention is: in desorbing electrolytic gold mud solution, add gelatin and polyoxyethylene glycol, be then fully uniformly mixed, and add after gelatin and polyoxyethylene glycol be fully uniformly mixed, the filtration velocity of desorbing electrolytic gold mud solution is accelerated; The filter effect of gold mud can be improved.
Described gelatin adds water and is mixed with saturated solution.
Gordian technique of the present invention is the conbined usage of gelatin and polyoxyethylene glycol.
Step of the present invention is as follows:
One, the preparation of gelatin and polyoxyethylene glycol: gelatin is added water and is mixed with saturated solution;
Two, use:
In the aqueous solution or acid treating solution of desorbing electrolytic gold mud, add gelatin saturated solution and polyoxyethylene glycol, filter after stirring.The add-on of gelatin and polyoxyethylene glycol is determined by experiment, and the gold mud consumption of different batches is different.
Beneficial effect of the present invention:
The filtration velocity of desorbing electrolytic gold mud can be significantly improved, shorten the refinery activities time, reduce energy consumption.
Embodiment
The method of the present invention is: in desorbing electrolytic gold mud solution, add gelatin and polyoxyethylene glycol, be then fully uniformly mixed, and add after gelatin and polyoxyethylene glycol be fully uniformly mixed, the filtration velocity of desorbing electrolytic gold mud solution is accelerated; The filter effect of gold mud can be improved.
Described gelatin adds water and is mixed with saturated solution.
Two kinds of gold mud are adopted and invention has been experimental study.Test adopts 2XZ-4 type vacuum pump, 2500ml filter flask, Φ 150mm Büchner funnel.
Embodiment 1:
Certain ore deposit desorbing electrolytic gold mud 1, principal element analytical results, in table 1, adopts the experimental result of different reagent in table 2.
Table 1 desorbing electrolytic gold mud 1 principal element analytical results
Element | Au | Ag | Cu | Pb | Zn | Fe |
Content (%) | 20.75 | 51.73 | 10.37 | 4.00 | 0.14 | 0.52 |
Table 2 desorbing electrolytic gold mud 1 nitric acid removal of impurities liquid filtration test result
Testing program | Do not add flocculation agent | Gelatin | Polyoxyethylene glycol | Gelatin and polyoxyethylene glycol share |
Filtration velocity | Cannot filter | Slowly | Cannot filter | Hurry up |
Embodiment 2:
Certain ore deposit desorbing electrolytic gold mud 2, principal element analytical results, in table 3, adopts the experimental result of different reagent in table 4.
Table 3 desorbing electrolytic gold mud 2 principal element analytical results
Element | Au | Ag | Cu | Pb | Zn | Fe |
Content (%) | 22.63 | 46.39 | 12.22 | 6.34 | 1.58 | 1.62 |
Table 4 desorbing electrolytic gold mud 2 nitric acid removal of impurities liquid filtration test result
Testing program | Do not add flocculation agent | Gelatin | Polyoxyethylene glycol | Gelatin and polyoxyethylene glycol share |
Filtration velocity | Filtration difficulty | Slowly | Filtration difficulty | Hurry up |
Claims (2)
1. improve a method for desorbing electrolytic gold mud filtration velocity, the method is: in desorbing electrolytic gold mud solution, add gelatin and polyoxyethylene glycol, be then fully uniformly mixed.
2. a kind of method improving desorbing electrolytic gold mud filtration velocity according to claim 1, is characterized in that: described gelatin adds water and is mixed with saturated solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510852373.6A CN105350017B (en) | 2015-11-30 | 2015-11-30 | Method increasing rate of filtration of desorbed and electrolyzed gold mud |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510852373.6A CN105350017B (en) | 2015-11-30 | 2015-11-30 | Method increasing rate of filtration of desorbed and electrolyzed gold mud |
Publications (2)
Publication Number | Publication Date |
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CN105350017A true CN105350017A (en) | 2016-02-24 |
CN105350017B CN105350017B (en) | 2017-05-03 |
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CN201510852373.6A Active CN105350017B (en) | 2015-11-30 | 2015-11-30 | Method increasing rate of filtration of desorbed and electrolyzed gold mud |
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Citations (16)
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US4013527A (en) * | 1974-08-05 | 1977-03-22 | Fuji Photo Film Co., Ltd. | Electrolytic oxidation of blix solution |
US4378285A (en) * | 1981-02-24 | 1983-03-29 | Mar Industries, Inc. | Gold recovery apparatus |
JPS6324089A (en) * | 1986-07-16 | 1988-02-01 | Tanaka Kikinzoku Kogyo Kk | Gold electrolytic solution |
CN2126853Y (en) * | 1992-06-30 | 1993-02-10 | 沈阳黄金学院 | Cyanide noble metal liquid carbon fibre electrode gold extraction slot |
CN2295765Y (en) * | 1997-01-25 | 1998-10-28 | 刘连增 | Electrolyzing tank |
FR2810681A1 (en) * | 2000-06-27 | 2001-12-28 | Claude Andre Bedjai | Recovery of precious metal, notably gold, from a variety of wastes involves electrolytic dissolution of gold and electrolytic deposition of gold from solution on an electrode |
DE10211084C1 (en) * | 2002-03-13 | 2003-08-07 | Mrut Mess Regel Umwelt Technik | Recovery of noble metal, especially gold, from production residue, e.g. sludge, dross or polishing dust, involves dissolution in aqueous thiocyanate solution by adding strong oxidant, e.g. sodium peroxydisulfate or peroxide |
CN1153850C (en) * | 2001-09-19 | 2004-06-16 | 北京大学 | Process for preparing high-purity gold by electrolyzing extracted gold-contained organic phase |
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CN100460532C (en) * | 2007-04-16 | 2009-02-11 | 中南大学 | Method of preparing high purity copper by bacteria leaching primary sulfide ore |
CN101392325A (en) * | 2008-10-21 | 2009-03-25 | 东华大学 | Method for extracting gold from waste printed circuit board |
CN101451190A (en) * | 2007-11-30 | 2009-06-10 | 灵宝市金源矿业有限责任公司 | Novel method for separating gold and silver from gold mud |
CN101550488A (en) * | 2009-05-13 | 2009-10-07 | 中南大学 | Method of preparing high pure cathode copper by using PCB acid chlorine copper etching solution sewage |
CN101942678B (en) * | 2010-09-19 | 2012-02-15 | 西南科技大学 | Preparation method of high-purity active zinc powder |
CN102071323B (en) * | 2010-12-16 | 2012-05-23 | 惠州Tcl环境科技有限公司 | Method for producing high-purity gold by utilizing electroplating waste liquid containing gold |
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2015
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Patent Citations (16)
Publication number | Priority date | Publication date | Assignee | Title |
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US4013527A (en) * | 1974-08-05 | 1977-03-22 | Fuji Photo Film Co., Ltd. | Electrolytic oxidation of blix solution |
US4378285A (en) * | 1981-02-24 | 1983-03-29 | Mar Industries, Inc. | Gold recovery apparatus |
JPS6324089A (en) * | 1986-07-16 | 1988-02-01 | Tanaka Kikinzoku Kogyo Kk | Gold electrolytic solution |
CN2126853Y (en) * | 1992-06-30 | 1993-02-10 | 沈阳黄金学院 | Cyanide noble metal liquid carbon fibre electrode gold extraction slot |
CN2295765Y (en) * | 1997-01-25 | 1998-10-28 | 刘连增 | Electrolyzing tank |
FR2810681A1 (en) * | 2000-06-27 | 2001-12-28 | Claude Andre Bedjai | Recovery of precious metal, notably gold, from a variety of wastes involves electrolytic dissolution of gold and electrolytic deposition of gold from solution on an electrode |
CN1153850C (en) * | 2001-09-19 | 2004-06-16 | 北京大学 | Process for preparing high-purity gold by electrolyzing extracted gold-contained organic phase |
DE10211084C1 (en) * | 2002-03-13 | 2003-08-07 | Mrut Mess Regel Umwelt Technik | Recovery of noble metal, especially gold, from production residue, e.g. sludge, dross or polishing dust, involves dissolution in aqueous thiocyanate solution by adding strong oxidant, e.g. sodium peroxydisulfate or peroxide |
KR20060006858A (en) * | 2006-01-04 | 2006-01-19 | 신동만 | A electroanalysis gold recovery apparatus with collector |
CN100460532C (en) * | 2007-04-16 | 2009-02-11 | 中南大学 | Method of preparing high purity copper by bacteria leaching primary sulfide ore |
US20080302671A1 (en) * | 2007-06-07 | 2008-12-11 | David Pearce | Sequential lixivation and precipitation of metals from refractory ores by utilising variable oxidation reduction potentials and a variable PH system |
CN101451190A (en) * | 2007-11-30 | 2009-06-10 | 灵宝市金源矿业有限责任公司 | Novel method for separating gold and silver from gold mud |
CN101392325A (en) * | 2008-10-21 | 2009-03-25 | 东华大学 | Method for extracting gold from waste printed circuit board |
CN101550488A (en) * | 2009-05-13 | 2009-10-07 | 中南大学 | Method of preparing high pure cathode copper by using PCB acid chlorine copper etching solution sewage |
CN101942678B (en) * | 2010-09-19 | 2012-02-15 | 西南科技大学 | Preparation method of high-purity active zinc powder |
CN102071323B (en) * | 2010-12-16 | 2012-05-23 | 惠州Tcl环境科技有限公司 | Method for producing high-purity gold by utilizing electroplating waste liquid containing gold |
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CN105350017B (en) | 2017-05-03 |
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Effective date of registration: 20170908 Address after: 011216 Inner Mongolia Xilinguole Meng Suniteyou and Zhu Zhen Patentee after: Sunite Jinxi gold mining limited liability company Address before: 130012 nanhu road, Jilin, Changchun, No. 6760 Patentee before: Changchun Gold Research Institute |
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