CN1858274A - New treating method for nickel oxide ore - Google Patents
New treating method for nickel oxide ore Download PDFInfo
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- CN1858274A CN1858274A CNA2006100109353A CN200610010935A CN1858274A CN 1858274 A CN1858274 A CN 1858274A CN A2006100109353 A CNA2006100109353 A CN A2006100109353A CN 200610010935 A CN200610010935 A CN 200610010935A CN 1858274 A CN1858274 A CN 1858274A
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Abstract
The new nickel oxide ore treating process has synthesized chemical metallurgy and ore dressing technology. The technological process includes crushing ore, grinding ore into ore pulp, magnetically separating out strong magnetic mineral, heating ore pulp and leaching out with concentrated sulfuric acid, adding sulfurizing agent for chemical reaction to produce nickel sulfide precipitate, and floating out nickel sulfide concentrate. The technological process is simple, low in production cost, high in nickel oxide leaching rate, effective utilization of resource and environment friendship.
Description
Technical field
The present invention relates to a kind of treatment process technology of nickel oxide ore, is the processing nickel oxide ore new process that combines chemical industry metallurgical and technique of preparing.
Technical background
The treatment process technology of nickel oxide ore is concluded three kinds of methods in the world at present, i.e. thermal process, wet processing and fiery wet method combined process.
First kind of thermal process: with ore reduction, retailoring is carried out in roasting, and thick Rhometal of output and nickelic sulphur product are sent to these work in-process the supporting processing of refinery practice again.
Second kind of wet processing: one of them is the ammonia soaking technology, and with the broken reducing roasting of nickel oxide ore, 4 stage countercurrent ammonia soak then, makes valuable metal such as nickel enter leach liquor.The leach liquor sulfide precipitation goes out alkali formula single nickel salt, is sintered into nickel oxide again, restores into nickel powder.Another kind is the method for low grade nickel ore bulk infusion extracting nickel cobalt, and it is ore reduction, the control mean particle size less than the ore of 2cm directly into heap, on ore storage, spray 5%～18% acid solution, collect leach liquor, filter out solution and add Sodium Sulphide, obtain heavy nickel nickelous sulfide.This method need constantly add water and filtration removing impurity and filtering in the nickelous sulfide process, can produce a large amount of tail washings, can cause environmental pollution.
The wet combined process method of the third fire: raw ore is levigate and fine coal mixing briquetting, nodulizing drying and high temperature reduction roasting, and roasted ore group is levigate again, and ore pulp carries out gravity concentration and magnetic concentration sub-elects Rhometal.
Therefore, generally believe in the industry that the nickel oxide ore pyrometallurgical smelting that grade is low, power charge is high is uneconomic; And ammonia leaching method also exists reduction to wait problems such as process energy consumption height, reagent cost height; The dump leaching method is obviously more inadvisable, and its leaching yield is too low, waste resource, the big and contaminate environment of raffinate amount.So above method is not to handle the best approach of nickel oxide ore.
Summary of the invention
Technical problem to be solved by this invention provides a kind of comprehensive multinomial technology; extract the novel process of nickel oxide ore; its technology is simple; production cost is low; can improve the leaching yield of nickel oxide ore greatly; effectively utilize limited resources, solved to soak and draw and be difficult to filtering technical barrier, and can favourable protection environment.
Solving the technical scheme that technical problem of the present invention adopts is: ore reduction, ore grinding are become ore pulp, magneticly elect strongly magnetic mineral; Ore pulp is heated and is added the vitriol oil and leaches, and adds vulcanizing agent then and carries out chemical reaction, the sedimentary nickelous sulfide of output; All solid, liquid products are sent into floatation equipment, floatingly select nickel sulfide concentrate.
Concrete processing method is as follows:
1. raw ore preparation: nickel oxide ore is carried out fragmentation, ore grinding and magnetic separation, make pulp granularity be less than 150 orders, the ore pulp liquid-solid ratio is 2.5～3: in 1 the scope, deviate from strongly magnetic mineral;
2. the ore pulp that 1 step was prepared joins the pond that has whipping appts or has in the reactor of whipping appts, add the steam and the vitriol oil when stirring ore pulp, strengthen and leach the nickel cobalt mineralss, endpoint pH is between 1.5～2, temperature is controlled between 80 ℃～100 ℃, and extraction time is 1 hour～2 hours.
3. add sulfur agent solution in 2 reaction tanks that go on foot or reactor, carry out chemical reaction, be settled out nickelous sulfide, reacted pH value is 3～4.
4. all nickel solutions and the slag of 3 steps in the ponds joined and carry out flotation in the floatation equipment, add flotation reagent and floatingly select high-grade high-quality nickel sulfide concentrate.
The present invention has following advantage and effect:
1. owing at first adopted, add acid and add medium-temperature reinforced leaching to crushing raw ore, ore grinding, magnetic separation, the leaching yield of nickel can reach more than 80%, reached the purpose of effectively utilizing the nickel oxide resource, and the leaching yield of existing wet method bulk infusion extracting nickel cobalt method only can reach about 30%, though the existing pyrogenic process rate of recovery is higher, cost approximately will exceed 2～3 times.
2. leach product and do not need filtration washing, directly add the heavy nickel of vulcanizing agent original position, solved and soaked a solid-liquid separation difficult problem that draws and be difficult to filter out.
3. behind the heavy nickel, solution and slag also need not to filter, and all directly add emersion nickel sulfide concentrate in the floatation equipment, make technology obtain simplifying, and the loss of nickel seldom.
4. this technology nickel ore concentrate rate of recovery height, technology is simple, and production cost is low, and tail washings is few, helps saving and the protection environment.The rate of recovery for raw ore nickel can reach about 70%, and the prior art of wet method is generally 20%～30%.
5. this technology is handled any low-grade nickel oxide mineral, and the only suitable higher-grade nickel minerals of traditional method alive.
Description of drawings
Fig. 1 is a process flow sheet of the present invention.
Embodiment
Embodiment 1
Get 2 kilograms of Yunnan Yuanjiang River red soil nickel ores (femic mixing ore deposit), through broken, ore grinding is that pulp granularity accounts for 85% less than 150 orders, the ore pulp liquid-solid ratio is 2.5, be fed in the reactor, be heated to 80 ℃, add the vitriol oil and stirred by force 1 hour, the control endpoint pH reaches 2, add vulcanizing agent sodium sulphite and carry out chemical reaction, reacted pH value is 3, the sedimentary nickelous sulfide of output.Then the total overall reaction thing in the reactor is delivered in the agitation vat, added the flotation reagent butyl xanthate and go into agitation vat and stir, ore pulp is rendered to floatingly selected nickel sulfide concentrate in the flotation column then.Give the nickeliferous grade 1.19% in ore deposit, the nickeliferous grade 24～25% of concentrate, nickel recovery 66～70%.
Embodiment 2
Get 100 kilograms of Yunnan Yuanjiang River red soil nickel ores (femic mixing ore deposit), through broken, ore grinding is that pulp granularity accounts for 80% less than 150 orders, the ore pulp liquid-solid ratio is 2.8, deviate from ferromagnetic substance with magnetic separator after, be fed in the reactor, be heated to 90 ℃, add the vitriol oil and stirred by force 100 minutes, the control endpoint pH reaches 1.5, adds vulcanizing agent hydrogen sulfide and carries out chemical reaction, reacted pH value is 3.5, the sedimentary nickelous sulfide of output.Then the total overall reaction thing in the reactor is delivered in the agitation vat, added the flotation reagent ethyl xanthogenate and go into agitation vat and stir, ore pulp is rendered to floatingly selected nickel sulfide concentrate in the flotation machine then.Give the nickeliferous grade 1.25% in ore deposit, the nickeliferous grade 24～25% of concentrate, nickel recovery 63～66%.
Embodiment 3
Get 400 kilograms of Yunnan Yuanjiang River red soil nickel ores (femic mixing ore deposit), through broken, ore grinding is that pulp granularity accounts for 86% less than 150 orders, the ore pulp liquid-solid ratio is 3, deviate from ferromagnetic substance with magnetic separator after, be fed in the reactor, be heated to 95 ℃, add the vitriol oil and stirred by force 120 minutes, the control endpoint pH reaches 1.8, adds the vulcanizing agent potassium sulphide and carries out chemical reaction, reacted pH value is 4, the sedimentary nickelous sulfide of output.Then the total overall reaction thing in the reactor is delivered in the agitation vat, added the flotation reagent pine tar and go into agitation vat and stir, ore pulp is rendered to floatingly selected nickel sulfide concentrate in the flotation cell then.Give the nickeliferous grade 1.22% in ore deposit, the nickeliferous grade 24～25% of concentrate, nickel recovery 64～67%.
Claims (3)
1. the New Method for Processing of a nickel oxide ore is characterized in that: technological process is, ore reduction, ore grinding are become ore pulp, magneticly elects strongly magnetic mineral; Ore pulp is heated and is added the vitriol oil and leaches, and adds vulcanizing agent then and carries out chemical reaction, the sedimentary nickelous sulfide of output; All solid, liquid products are sent into floatation equipment, floatingly select nickel sulfide concentrate.
2. the New Method for Processing of nickel oxide ore as claimed in claim 1, it is characterized in that: the pulp granularity behind (1) ore grinding is less than 150 orders, and the ore pulp liquid-solid ratio is 2.5～3: 1, and it is 1.5～2 that the vitriol oil and ore pulp leach the back endpoint pH; (2) the reacted pH value of sulphuric leachate and vulcanizing agent is 3～4.
3, the New Method for Processing of nickel oxide ore as claimed in claim 2 is characterized in that: ore pulp feeds steam simultaneously and stirs in the process that sulfuric acid leaches, temperature is controlled at 80 ℃～100 ℃, and the time is 1 hour～2 hours.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CNB2006100109353A CN100371471C (en) | 2006-06-02 | 2006-06-02 | New treating method for nickel oxide ore |
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| CNB2006100109353A CN100371471C (en) | 2006-06-02 | 2006-06-02 | New treating method for nickel oxide ore |
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| CN1858274A true CN1858274A (en) | 2006-11-08 |
| CN100371471C CN100371471C (en) | 2008-02-27 |
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| CNB2006100109353A Expired - Fee Related CN100371471C (en) | 2006-06-02 | 2006-06-02 | New treating method for nickel oxide ore |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101073790B (en) * | 2006-12-22 | 2010-05-19 | 昆明贵金属研究所 | Reduction-mill concentration treatment for different-type red-clay nickel mine |
| CN101928826A (en) * | 2010-09-03 | 2010-12-29 | 罗光臣 | Agitation leaching method for ore paste |
| CN102773150A (en) * | 2011-05-12 | 2012-11-14 | 云南锡业集团（控股）有限责任公司 | Polymetallic (iron, tin and zinc) ore comprehensive recovery beneficiation method |
| CN103030182A (en) * | 2012-12-26 | 2013-04-10 | 田飞 | Purification method of NiO nanocube particles synthesized with laser method |
| CN106824552A (en) * | 2016-12-21 | 2017-06-13 | 广西睿桂涵农业有限公司 | A kind of beneficiation method of lateritic nickel ore |
| CN108374089A (en) * | 2018-02-22 | 2018-08-07 | 中国恩菲工程技术有限公司 | The method of concentrating cobalt and nickel from nickeliferous cobalt liquor |
| CN108467951A (en) * | 2018-02-22 | 2018-08-31 | 中国恩菲工程技术有限公司 | The method of concentrating cobalt and nickel from nickeliferous cobalt liquor |
| CN109536706A (en) * | 2018-12-02 | 2019-03-29 | 六盘水中联工贸实业有限公司 | One kind handling nickel ore method based on magnetic field |
| CN114672641A (en) * | 2022-04-15 | 2022-06-28 | 西北矿冶研究院 | Dressing and smelting combined process for refractory dip-dyed copper-nickel oxide ore |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1023718C (en) * | 1990-06-16 | 1994-02-09 | 徐有生 | New method for processing of nickel oxide ore |
| JP4525428B2 (en) * | 2004-05-13 | 2010-08-18 | 住友金属鉱山株式会社 | Method for hydrometallizing nickel oxide ore |
-
2006
- 2006-06-02 CN CNB2006100109353A patent/CN100371471C/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101073790B (en) * | 2006-12-22 | 2010-05-19 | 昆明贵金属研究所 | Reduction-mill concentration treatment for different-type red-clay nickel mine |
| CN101928826A (en) * | 2010-09-03 | 2010-12-29 | 罗光臣 | Agitation leaching method for ore paste |
| CN102773150A (en) * | 2011-05-12 | 2012-11-14 | 云南锡业集团（控股）有限责任公司 | Polymetallic (iron, tin and zinc) ore comprehensive recovery beneficiation method |
| CN103030182A (en) * | 2012-12-26 | 2013-04-10 | 田飞 | Purification method of NiO nanocube particles synthesized with laser method |
| CN103030182B (en) * | 2012-12-26 | 2014-10-22 | 田飞 | Purification method of NiO nanocube particles synthesized with laser method |
| CN106824552A (en) * | 2016-12-21 | 2017-06-13 | 广西睿桂涵农业有限公司 | A kind of beneficiation method of lateritic nickel ore |
| CN106824552B (en) * | 2016-12-21 | 2019-05-14 | 广西睿桂涵农业有限公司 | A kind of beneficiation method of lateritic nickel ore |
| CN108374089A (en) * | 2018-02-22 | 2018-08-07 | 中国恩菲工程技术有限公司 | The method of concentrating cobalt and nickel from nickeliferous cobalt liquor |
| CN108467951A (en) * | 2018-02-22 | 2018-08-31 | 中国恩菲工程技术有限公司 | The method of concentrating cobalt and nickel from nickeliferous cobalt liquor |
| CN109536706A (en) * | 2018-12-02 | 2019-03-29 | 六盘水中联工贸实业有限公司 | One kind handling nickel ore method based on magnetic field |
| CN114672641A (en) * | 2022-04-15 | 2022-06-28 | 西北矿冶研究院 | Dressing and smelting combined process for refractory dip-dyed copper-nickel oxide ore |
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| Publication number | Publication date |
|---|---|
| CN100371471C (en) | 2008-02-27 |
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Effective date of registration: 20161221 Address after: 661000 Yunnan, Gejiu City, Jinhu East Road, No. 121 Patentee after: Yunnan Tin Company Group (Holding) Co., Ltd. Address before: 661000 Yunnan, Gejiu City, Jinhu East Road, No. 121 Patentee before: Yunnan Tin Company Group Limited |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080227 Termination date: 20160602 |