CN106086406A - A kind of renovation process of organic extractant - Google Patents
A kind of renovation process of organic extractant Download PDFInfo
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- CN106086406A CN106086406A CN201610747816.XA CN201610747816A CN106086406A CN 106086406 A CN106086406 A CN 106086406A CN 201610747816 A CN201610747816 A CN 201610747816A CN 106086406 A CN106086406 A CN 106086406A
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- organic extractant
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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
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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
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- Environmental & Geological Engineering (AREA)
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- Organic Chemistry (AREA)
- Extraction Or Liquid Replacement (AREA)
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Abstract
The invention discloses the renovation process of a kind of organic extractant, the method comprises the following steps: acid reaction, alkali reaction, inorganic acid reaction, Pure water preparation.Utilization part of the present invention causes metal ion that organic extractant " is poisoned " and oxalic acid or sodium carbonate or sodium bicarbonate binding ability more than the feature with organic extractant binding ability, by this part metals ion from organic extractant back extraction to aqueous phase, reach the purpose of organic extractant regeneration, metal ion in organic extractant can not only be removed by this method effectively, improve the extract and separate ability of organic extractant, but also it is short to have technological process, equipment is simple, feature easy and simple to handle, is a kind of excellent organic extractant renovation process.
Description
Technical field
The present invention relates to metallurgical technology field, be specifically related to the renovation process of a kind of organic extractant.
Background technology
In hydrometallurgy, organic extractant is different to the extracting power of different non-ferrous metal elements, therefore has
Machine extractant separates metallic element is conventional and purifies.Lanthanide series, copper, nickel, cobalt, uranium, indium, tungsten, molybdenum etc. metal unit
Element is all used organic extractant and is carried out wet separation and purification.Normal organic extractant be divided into acidic extractant, Neutral-neutral Extractants,
Amine extractant, wherein acidic extractant has P204, P507, Cyanex272, aphthenic acids etc., Neutral-neutral Extractants have TBP, P350,
TOPO etc., amine extracted have tri-n-octyl amine, N235, N503 etc..Along with organic extractant recycling in process of production, portion
The metal ion that partial volume is easily extracted and extractant define relatively stable coordination compound and are difficult to by back extraction, as copper, ferrum, hydrargyrum,
Nickel etc..These metal ions are progressively enriched with in extractant, thus reduce the extracting power of extractant, make extraction split-phase effect
It is deteriorated, even makes extraction " be poisoned " or lost efficacy.
Therefore, in order to remove the foreign ion in organic extractant, improve extract and separate effect, current inventor provides one
Plant the renovation process of organic extractant.
Summary of the invention
For solving above-mentioned technical problem, the invention provides the renovation process of a kind of organic extractant.
The present invention is achieved by the following technical programs:
A kind of renovation process of organic extractant, the method comprises the following steps:
A, acid reaction: be put in reactor by organic extractant, be added thereto to the oxalic acid solution of 0.1-1.0mol/L, grass
0.01-1.0 times that molal quantity is organic extractant molal quantity of acid, after agitated mixing 5-30min, clarification layering, by aqueous phase
Venting；
B, alkali reaction: in the organic extractant in step a, add OH-Concentration is the alkaline solution of 0.5-3.0mol/L,
The OH of alkaline solution-Molal quantity is 0.1-1.5 times of organic extractant molal quantity, after agitated mixing 5-30min, and clarification point
Layer, by aqueous phase venting；
C, inorganic acid reaction: in the organic extractant in step b, add H+Concentration is the mineral acid of 1.0-6.0mol/L,
The H of mineral acid+Molal quantity is addition OH in step b-0.5-1.5 times of molal quantity, after agitated mixing 5-30min, clarification point
Layer, by aqueous phase venting；
D, Pure water preparation: adding pure water in the organic extractant in step c, the volume of pure water is organic extractant volume
0.1-0.5 times, after agitated mixing 5-30min, clarification layering, by aqueous phase venting.
Organic extractant in described step a is the one in organophosphorus-type extractant, aphthenic acids, amine extractant.
Alkaline solution in described step b is at least one in aqueous sodium carbonate and sodium bicarbonate aqueous solution.
Mineral acid in described step c is the one in hydrochloric acid, sulphuric acid, Fluohydric acid..
The beneficial effects of the present invention is: the metal ion that utilization part of the present invention causes organic extractant " to be poisoned " and grass
Acid or sodium carbonate or sodium bicarbonate binding ability more than the feature with organic extractant binding ability, by this part metals from
Son, from organic extractant back extraction to aqueous phase, reaches the purpose of organic extractant regeneration, and this method can not only will have effectively
Metal ion in machine extractant is removed, and improves the extract and separate ability of organic extractant, but also it is short to have technological process, if
Standby simple, feature easy and simple to handle, is a kind of excellent organic extractant renovation process.
Detailed description of the invention
Below in conjunction with specific embodiment, technical scheme is further described, but claimed scope is not
It is confined to described.
Embodiment one
Being put in the reactor of 1000L by the P507 extractant that 500L concentration is 1.5mol/L, being added thereto to concentration is
The oxalic acid solution 50L of 0.8mol/L, clarification layering after stirring 5min, add OH after venting aqueous phase-Concentration is the carbon of 1.8mol/L
Acid sodium and mixed solution (weight ratio the is 3:1) 200L of sodium bicarbonate, clarification layering after stirring 10min, add H after venting aqueous phase+Concentration is the hydrochloric acid solution 100L of 5.0mol/L, clarification layering after stirring 10min, adds pure water 50L, stirring after venting aqueous phase
Clarification layering, the P507 that after venting aqueous phase, remaining organic facies is namely regenerated after 10min.
Embodiment two
The aphthenic acids extractant that 500L concentration is 0.5mol/L is put in the reactor of 1000L, is added thereto to concentration
For the oxalic acid solution 100L of 0.2mol/L, clarification layering after stirring 10min, after venting aqueous phase, add OH-Concentration is 1.5mol/L
Sodium carbonate liquor 200L, stirring 10min after clarification layering, after venting aqueous phase add H+Concentration is the hydrochloric acid solution of 3.0mol/L
80L, clarification layering after stirring 10min, add pure water 100L after venting aqueous phase, clarification layering after stirring 5min, after venting aqueous phase
The aphthenic acids that remaining organic facies is namely regenerated.
Embodiment three
Being put in the reactor of 1000L by the N235 extractant that 500L concentration is 0.3mol/L, being added thereto to concentration is
The oxalic acid solution 100L of 1.0mol/L, clarification layering after stirring 8min, add OH after venting aqueous phase-Concentration is the carbon of 0.5mol/L
Acid hydrogen sodium solution 100L, clarification layering after stirring 8min, add H after venting aqueous phase+Concentration is the hydrochloric acid solution of 5.0mol/L
50L, clarification layering after stirring 10min, add pure water 200L after venting aqueous phase, clarification layering after stirring 15min, after venting aqueous phase
The N235 that remaining organic facies is namely regenerated.
Claims (4)
1. the renovation process of an organic extractant, it is characterised in that: the method comprises the following steps:
A, acid reaction: be put in reactor by organic extractant, be added thereto to the oxalic acid solution of 0.1-1.0mol/L, oxalic acid
Molal quantity is 0.01-1.0 times of organic extractant molal quantity, and after agitated mixing 5-30min, clarification layering, by aqueous phase venting；
B, alkali reaction: in the organic extractant in step a, add OH-Concentration is the alkaline solution of 0.5-3.0mol/L, and alkalescence is molten
The OH of liquid-Molal quantity is 0.1-1.5 times of organic extractant molal quantity, and after agitated mixing 5-30min, clarification layering, by water
Phase venting；
C, inorganic acid reaction: in the organic extractant in step b, add H+Concentration is the mineral acid of 1.0-6.0mol/L, inorganic
The H of acid+Molal quantity is addition OH in step b-0.5-1.5 times of molal quantity, after agitated mixing 5-30min, clarification layering, will
Aqueous phase venting；
D, Pure water preparation: adding pure water in the organic extractant in step c, the volume of pure water is organic extractant volume
0.1-0.5 times, after agitated mixing 5-30min, clarification layering, by aqueous phase venting.
The renovation process of organic extractant the most according to claim 1, it is characterised in that: the organic extraction in described step a
Taking agent is the one in organophosphorus-type extractant, aphthenic acids, amine extractant.
The renovation process of organic extractant the most according to claim 1, it is characterised in that: the alkalescence in described step b is molten
Liquid is at least one in aqueous sodium carbonate and sodium bicarbonate aqueous solution.
The renovation process of organic extractant the most according to claim 1, it is characterised in that: the mineral acid in described step c
For the one in hydrochloric acid, sulphuric acid, Fluohydric acid..
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| CN201610747816.XA CN106086406B (en) | 2016-08-28 | 2016-08-28 | A kind of renovation process of organic extractant |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110923449A (en) * | 2019-12-11 | 2020-03-27 | 南昌航空大学 | Method for recovering P204 from waste P204 extracted organic phase |
| CN110923450A (en) * | 2019-12-13 | 2020-03-27 | 南昌航空大学 | Method for recovering C272 from waste C272 extraction organic phase |
| CN112063838A (en) * | 2020-08-07 | 2020-12-11 | 浙江天能新材料有限公司 | Method for purifying and regenerating P204 and P507 extracting agents |
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| JPS59110740A (en) * | 1982-12-14 | 1984-06-26 | Agency Of Ind Science & Technol | Recovery of metal from organic phase by oxalic acid in solvent extraction method |
| CN1936035A (en) * | 2006-09-29 | 2007-03-28 | 金川集团有限公司 | P204 deferrizing regeneration method |
| CN1944357A (en) * | 2005-10-09 | 2007-04-11 | 中国科学院过程工程研究所 | Recovery method for ionic liquid |
| CN102534213A (en) * | 2012-02-17 | 2012-07-04 | 云南五鑫实业有限公司 | Method for carrying out normalized treatment on P204 extraction poisoning |
| CN102660679A (en) * | 2012-05-24 | 2012-09-12 | 北京化工大学 | Method for eluting Fe<3+> in P204 extracting agent |
| CN103572053A (en) * | 2012-08-07 | 2014-02-12 | 深圳市格林美高新技术股份有限公司 | Wet recovery method for scrap automobiles or electroplating wastes and poisoned extractant treatment method therefor |
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| CN104805287A (en) * | 2015-04-22 | 2015-07-29 | 贵州宏达环保科技有限公司 | Regeneration method of CP180 copper extraction agent |
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| JPS59110740A (en) * | 1982-12-14 | 1984-06-26 | Agency Of Ind Science & Technol | Recovery of metal from organic phase by oxalic acid in solvent extraction method |
| CN1944357A (en) * | 2005-10-09 | 2007-04-11 | 中国科学院过程工程研究所 | Recovery method for ionic liquid |
| CN1936035A (en) * | 2006-09-29 | 2007-03-28 | 金川集团有限公司 | P204 deferrizing regeneration method |
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| CN102660679A (en) * | 2012-05-24 | 2012-09-12 | 北京化工大学 | Method for eluting Fe<3+> in P204 extracting agent |
| CN103572053A (en) * | 2012-08-07 | 2014-02-12 | 深圳市格林美高新技术股份有限公司 | Wet recovery method for scrap automobiles or electroplating wastes and poisoned extractant treatment method therefor |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110923449A (en) * | 2019-12-11 | 2020-03-27 | 南昌航空大学 | Method for recovering P204 from waste P204 extracted organic phase |
| CN110923449B (en) * | 2019-12-11 | 2021-06-22 | 南昌航空大学 | Method for recovering P204 from waste P204 extracted organic phase |
| CN110923450A (en) * | 2019-12-13 | 2020-03-27 | 南昌航空大学 | Method for recovering C272 from waste C272 extraction organic phase |
| CN110923450B (en) * | 2019-12-13 | 2021-06-22 | 南昌航空大学 | Method for recovering C272 from waste C272 extraction organic phase |
| CN112063838A (en) * | 2020-08-07 | 2020-12-11 | 浙江天能新材料有限公司 | Method for purifying and regenerating P204 and P507 extracting agents |
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| Publication number | Publication date |
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| CN106086406B (en) | 2018-05-29 |
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Address after: 542603 Wanggao Industrial Development Zone, Hezhou, the Guangxi Zhuang Autonomous Region Patentee after: China Rare Earth (Guangxi) Jinyuan rare earth new material Co., Ltd Address before: 542800 Wanggao Industrial Development Zone, Hezhou City, Hezhou City, Guangxi Zhuang Autonomous Region Patentee before: CHINALCO GUANGXI COLORED JINYUAN RARE EARTH Co.,Ltd. |