CN1715428A - Method for extracting metal solvent - Google Patents
Method for extracting metal solvent Download PDFInfo
- Publication number
- CN1715428A CN1715428A CNA2004101036628A CN200410103662A CN1715428A CN 1715428 A CN1715428 A CN 1715428A CN A2004101036628 A CNA2004101036628 A CN A2004101036628A CN 200410103662 A CN200410103662 A CN 200410103662A CN 1715428 A CN1715428 A CN 1715428A
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- CN
- China
- Prior art keywords
- solvent
- temperature
- dbc
- solution
- metal
- 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.)
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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
- 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
- C22B3/26—Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds
- C22B3/302—Ethers or epoxides
-
- 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
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/006—Wet processes
-
- 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
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Geology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention provides a method for extracting metal solvent which increases an extracted amount throughout a year and keeps the extracted amount. The method keeps a temperature of a DBC solvent at 25 degree or higher, and improves a phase splitting property of a solution and the solvent to enhance the extraction capability.
Description
Technical field
The invention relates to the solvent extraction method of gold.
Particularly about in the winter time or in the area of low temperature, after solvent temperature reduces, the extraction of the metal countermeasure at need that becomes.
Background technology
The extraction of gold is fast so adopting mixer-settler (mixer-settler) to carry out operate continuously because of its reaction.In mixer-settler, fractionate aqueous solutions phase and solvent phase, the dibutyl carbitol (hereinafter referred to as DBC) after the recovery extracting gold.DBC after the extracting gold with in the DBC storage tank before still being admitted to extracting gold after the gold reduction separation, sends into mixer-settler with pump of constant delivery type again in gold reduction operation, be used for the extracting operation of gold.
DBC is equivalent to the 4th class the 3rd petroleum-type, uses at normal temperatures up to now.
For this reason, the temperature that is supplied in the DBC of gold extraction is subjected to the influence of fluid temperature and temperature before the extracting gold and changes.
About the problems referred to above, to open in 2001-316735 number (Patent Document 1:0025,0046 paragraph, Fig. 1 etc.) the spy, the temperature factor when utilizing the DBC extracting gold is not unexpectedly recognized fully.
This can think that those skilled in the art do not recognize very much the influence that brings owing to temperature because of its percentage extraction height of DBC.
In addition, open in flat 02-310326 number (Patent Document 2: embodiment 2 etc.) also relevant for the record of adopting the DBC extracting gold the spy, but fully not about the record of temperature.
[Patent Document 1] spy opens 2001-316735 number
[Patent Document 2] spy opens flat 02-310326 number
Thereby recognize the winter that descends at temperature, and compare with summer, the problem that extracting power reduces, hope obtains can keep by this countermeasure the method for constant extracting power in whole 1 year.
In addition, this problem becomes even more important problem at cold district.
Summary of the invention
Present inventors reach following invention for addressing the above problem.
Be that the present invention is:
(1) a kind of solvent extraction method of metal is characterized in that: the temperature of DBC solvent is continued to remain on more than 25 ℃, make the being separated property of solution and solvent good, to improve extracting power.
(2) a kind of solvent extraction method of metal is characterized in that: in the heating method of the solvent of above-mentioned (1), solvent is heated up directly or indirectly.
(3) a kind of solvent extraction method of metal, it is characterized in that: the temperature of the process object solution that will contact with the DBC solvent, remain on more than 26 ℃ by thermophore, and the DBC solvent is contacted with the solution of above-mentioned intensification, the temperature of DBC solvent is remained on more than 25 ℃, make the being separated property of solution and solvent good, to improve extracting power.
(4) a kind of solvent extraction method of metal, it is characterized in that: the temperature of the process object solution that will contact with the DBC solvent, remain on more than 26 ℃ by heat exchanger, and the DBC solvent is contacted with the solution of above-mentioned intensification, the temperature of DBC solvent is remained on more than 25 ℃, make the being separated property of solution and solvent good, to improve extracting power.
(5) according to the solvent extraction method of the metal of record in above-mentioned (4), it is characterized in that: the solvent temperature behind the detection extracting metals, the Heating temperature of solution before the control extracting metals.
(6) according to the solvent extraction method of the metal of record in above-mentioned (4) or (5), it is characterized in that: the solution that is supplied in the washing of solvent behind the extracting metals is also heated, and the washing that the temperature with the DBC solvent is remained on more than 25 ℃ becomes possibility.
(7) a kind of solvent extraction method of metal is characterized in that: the heat exchanger of record is as thermophore with steam and/or warm water in (4)～(6).
(8) a kind of solvent extraction method of metal is characterized in that: the heat exchanger of record is a shell-tube type in (4)～(7), and interior wall liner is with tetrafluoroethylene, makes the process object liquid flow cross in the polyfluortetraethylene pipe or polyfluortetraethylene pipe is external heats.
(9) a kind of solvent extraction method of metal is characterized in that: the metal of record is a gold in above-mentioned (4)～(8).
If according to the present invention
(1) can run through and improved extracting power in 1 year, particularly in low winter of temperature or at cold district, it is bigger that extracting power improves effect.
(2) compare with snead process, utilize process object liquid to solvent indirect heating can guarantee higher security.
(3), have in order to remove lead, tellurium, the antimony in the solution, and the temperature that reduces solution is separated out the method for separating and removing above-mentioned impurity as handling form of the last procedure of golden extraction process.But in this case, the temperature of solution reaches below 5 ℃ in the winter time, and the extracting power of gold significantly lowers.But by adopting the present invention can prevent the attenuating of the extracting power of gold in advance.
Description of drawings
Fig. 1 is a form of the sketch map of the solvent heating device that is suitable for of the present invention.
A form of the golden extraction quantity when Fig. 2 represents to heat DBC and do not heat DBC.
Embodiment
Below the present invention is described in detail.
Relevant object solution of the present invention is that gold can be dissolved in acid bath wherein.For example, be hydrochloric acid acidity.The concentration of gold for example is the solution of 1～50g/L.
Employing solvent DBC extracts the gold in this solution.At this moment observations such as present inventor recognize the difference according to the temperature of solvent, the extraction quantity of gold (proportion is also different simultaneously) difference.Therefore, under the occasion that the outdoor air temperature that waits is low, special hope improves the temperature of solvent in the winter time.
In addition, by continuing to remain on more than 25 ℃, can keep certain extraction quantity, and can keep certain processing capabilities, become key element important in the business activity.
If will directly increase the temperature of solvent, will be subjected to much to limit and cause the increase of required equipment expense according to the area, so preferably with thermophore the temperature of process object liquid is raise in advance.
So-called thermophore for example, has the method for utilizing heat exchanger etc.
As shown in fig. 1, for example, the process object liquid before the extracting gold will pass through heat exchanger.
Heat exchanger, for example, as thermophore, the inwall of heat exchanger is a tetrafluoroethylene with steam and/or warm water.And can consider to adopt polyfluortetraethylene pipe, make method or with it the opposite mode of process object liquid by heating in managing.
The process object liquid that comes out from steam heat exchanger is warmed up to about 25～60 ℃.
Contact with the DBC solvent phase by the treatment solution that makes this intensification, the solvent temperature after the extraction also must remain on more than 25 ℃ in the winter time or at cold district.
Thus, for example,, in the time of 10 ℃, be 38g/L at the extraction quantity of guaranteeing the gold under the being separated property condition, in the time of 26 ℃, then be 47g/L, extracting power can improve more than 1.2 times.
In addition, with regard to the temperature of solvent, the temperature by perception extraction back solvent, perception process object liquid be in the temperature of heat exchanger outlet, and by adjusting the quantity of steam and/or the warm water of heat exchanger automatically, can carry out the management of temperature no change.
Promptly in Fig. 1, in the temperature of T2 place perception solvent, perception is in the process object temperature at T1 place, automatically the temperature or the amount of liquid of steam regulation amount and/or warm water.
[embodiment]
Below according to Fig. 1, specific examples is described.
Adopt shown in Fig. 1 and install, by the liquid warming of heat exchanger before to extracting gold, making its temperature is 26～39 ℃.
The result is as shown in table 1, and the temperature with the DBC after the extraction of the gold in the process object liquid in mixer-settler is warmed up to 26～30 ℃.
Thus, as shown in table 1 by the extraction quantity of the gold of DBC extraction, even if be 47～51g/L, also can guarantee being separated property, make operation still for may.
In addition, according to Fig. 2 as can be known, the temperature of DBC can guarantee preferred golden extraction quantity more than 25 ℃ the time.
The temperature of DBC after the extraction is measured at the T1 place, and for quantity of steam, perception process object liquid is adjusted the quantity of steam of heat exchanger in the temperature T 2 of heat exchanger outlet, so that reach constant T2 temperature, makes the homo(io)thermism of DBC.
Compare with the situation of not heating, can increase production 2 one-tenth more than.
Table 1
| DBC | DBC | |
| Temperature ℃ | Gold concentration g/L | |
| Before heating | 10 | 38 |
| 14 | 41 | |
| 18 | 43 | |
| Enforcement is heated | 26 | 47 |
| 28 | 49 | |
| 30 | 51 |
(comparative example)
Under the situation of not heating, the temperature of DBC is 10～18 ℃, if not making the extraction quantity of the gold among the DBC is below 38～43g/L, then can not guarantee being separated property and ongoing operation.
In addition, the extraction quantity of gold is low, in 1 day, because the temperature of DBC (=proportion) changes, is guaranteeing under the condition of being separated property that if will obtain the maximum extraction amount, the management of the fine setting of process object flow quantity and DBC flow seems necessary.The extraction operation also bothers.
Claims (9)
1, a kind of solvent extraction method of metal is characterized in that: the temperature of dibutyl carbitol solvent is continued to remain on more than 25 ℃, make the being separated property of solution and solvent good, to improve extracting power.
2, a kind of solvent extraction method of metal is characterized in that: in the described solvent heating method of claim 1, solvent directly or indirectly heats up.
3, a kind of solvent extraction method of metal, it is characterized in that: the temperature of the process object liquid that will contact with the DBC solvent, remain on more than 26 ℃ by thermophore, and the DBC solvent is contacted with the solution of above-mentioned intensification, the temperature of DBC solvent is remained on more than 25 ℃, make the being separated property of solution and solvent good, to improve extracting power.
4, a kind of solvent extraction method of metal, it is characterized in that: the temperature of the process object solution that will contact with the DBC solvent, remain on more than 26 ℃ by heat exchanger, and the DBC solvent is contacted with the solution of above-mentioned intensification, the temperature of DBC solvent is remained on more than 25 ℃, make the being separated property of solution and solvent good, to improve extracting power.
5, the solvent extraction method of metal according to claim 4 is characterized in that: the solvent temperature behind the detection extracting metals, the Heating temperature of solution before the control extracting metals.
6, according to the solvent extraction method of claim 4 or 5 described metals, it is characterized in that: the solution to the washing that is supplied in the solvent behind the extracting metals is also heated, and the washing that the temperature with the DBC solvent is remained on more than 25 ℃ becomes possibility.
7, a kind of solvent extraction method of metal is characterized in that: the heat exchanger of record is a thermophore with steam and/or warm water in the claim 4～6.
8, a kind of solvent extraction method of metal is characterized in that: the heat exchanger of record is the package mode in the claim 4～7, and wall liner makes the process object solution stream cross in the polyfluortetraethylene pipe or polyfluortetraethylene pipe is external heats with tetrafluoroethylene in it.
9, a kind of solvent extraction method of metal is characterized in that: the metal of record is a gold in the claim 1～8.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2004194904 | 2004-06-30 | ||
| JP2004194904A JP2006016657A (en) | 2004-06-30 | 2004-06-30 | Method for solvent-extracting metal |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1715428A true CN1715428A (en) | 2006-01-04 |
| CN100354438C CN100354438C (en) | 2007-12-12 |
Family
ID=35791198
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004101036628A Expired - Fee Related CN100354438C (en) | 2004-06-30 | 2004-12-24 | Method for extracting metal solvent |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JP2006016657A (en) |
| KR (1) | KR20060001801A (en) |
| CN (1) | CN100354438C (en) |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1011420B (en) * | 1988-06-15 | 1991-01-30 | 中国有色金属工业总公司昆明贵金属研究所 | Method using composite extractant to produce high-pure gold |
| JP3616314B2 (en) * | 2000-03-03 | 2005-02-02 | 日鉱金属株式会社 | Method for treating copper electrolytic deposits |
| JP4122715B2 (en) * | 2001-01-31 | 2008-07-23 | 住友金属鉱山株式会社 | Method for recovering organic solvent bis (2-butoxyethyl) ether |
-
2004
- 2004-06-30 JP JP2004194904A patent/JP2006016657A/en active Pending
- 2004-11-04 KR KR1020040089106A patent/KR20060001801A/en active Search and Examination
- 2004-12-24 CN CNB2004101036628A patent/CN100354438C/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP2006016657A (en) | 2006-01-19 |
| CN100354438C (en) | 2007-12-12 |
| KR20060001801A (en) | 2006-01-06 |
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| C06 | Publication | ||
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| C14 | Grant of patent or utility model | ||
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| ASS | Succession or assignment of patent right |
Owner name: JX NIPPON MINING + METALS CORPORATION Free format text: FORMER OWNER: NIPPON MINING JINYUE CORPORATION Effective date: 20110402 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20110402 Address after: Tokyo, Japan, Japan Patentee after: JX Nippon Mining & Metals Corporation Address before: Tokyo, Japan, Japan Patentee before: Japan gold moon Corporation |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071212 Termination date: 20141224 |
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| EXPY | Termination of patent right or utility model |