CN102441483A - Process for recovering superfine tantalum-niobium minerals from tantalum-niobium ores - Google Patents
Process for recovering superfine tantalum-niobium minerals from tantalum-niobium ores Download PDFInfo
- Publication number
- CN102441483A CN102441483A CN2011102945115A CN201110294511A CN102441483A CN 102441483 A CN102441483 A CN 102441483A CN 2011102945115 A CN2011102945115 A CN 2011102945115A CN 201110294511 A CN201110294511 A CN 201110294511A CN 102441483 A CN102441483 A CN 102441483A
- Authority
- CN
- China
- Prior art keywords
- tantalum
- tantalum niobium
- niobium concentrate
- niobium
- magnetic separation
- 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
- RHDUVDHGVHBHCL-UHFFFAOYSA-N niobium tantalum Chemical compound [Nb].[Ta] RHDUVDHGVHBHCL-UHFFFAOYSA-N 0.000 title claims abstract description 117
- 238000000034 method Methods 0.000 title abstract description 12
- 229910001729 niobium mineral Inorganic materials 0.000 title abstract 5
- 239000012141 concentrate Substances 0.000 claims abstract description 86
- 238000007885 magnetic separation Methods 0.000 claims abstract description 43
- 238000011084 recovery Methods 0.000 claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 claims abstract description 9
- 239000013067 intermediate product Substances 0.000 claims abstract description 8
- 238000005516 engineering process Methods 0.000 claims description 27
- 230000005484 gravity Effects 0.000 claims description 12
- 239000006148 magnetic separator Substances 0.000 claims description 11
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 8
- 239000011707 mineral Substances 0.000 claims description 8
- 229910052629 lepidolite Inorganic materials 0.000 claims description 6
- 238000005119 centrifugation Methods 0.000 claims description 4
- 230000005307 ferromagnetism Effects 0.000 claims description 4
- 238000000227 grinding Methods 0.000 claims description 4
- 230000002787 reinforcement Effects 0.000 claims description 4
- 230000007613 environmental effect Effects 0.000 abstract description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000047 product Substances 0.000 abstract description 3
- 239000002253 acid Substances 0.000 abstract description 2
- 239000012535 impurity Substances 0.000 abstract description 2
- 229910052742 iron Inorganic materials 0.000 abstract description 2
- 238000002386 leaching Methods 0.000 abstract description 2
- 239000010419 fine particle Substances 0.000 abstract 2
- 238000006477 desulfuration reaction Methods 0.000 abstract 1
- 230000023556 desulfurization Effects 0.000 abstract 1
- 238000005188 flotation Methods 0.000 abstract 1
- 229910052715 tantalum Inorganic materials 0.000 description 9
- 230000000694 effects Effects 0.000 description 2
- 229910052758 niobium Inorganic materials 0.000 description 2
- 239000010955 niobium Substances 0.000 description 2
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000010433 feldspar Substances 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 230000005389 magnetism Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Landscapes
- Manufacture And Refinement Of Metals (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
The invention discloses a process for recovering superfine tantalum-niobium minerals from tantalum-niobium ores, which comprises the following steps: recovering fine tantalum-niobium minerals by using the primary fine mud or the secondary fine mud, and recovering the fine tantalum-niobium minerals by using the tantalum-niobium ore tailings, wherein the primary fine mud or the secondary fine mud is separated by a centrifugal machine, and is treated by a table concentrator to obtain fine tantalum-niobium concentrate; removing strong-magnetic iron from the tantalum-niobium ore tailings by low-intensity magnetic separation, then obtaining a low-magnetic intermediate product containing tantalum-niobium ore by high-intensity magnetic separation, and performing flotation, desulfurization and acid leaching on the intermediate product to obtain superfine tantalum-niobium ore concentrate. Aiming at primary or secondary fine mud in the production of the tantalum-niobium ore and micro-fine particle tantalum-niobium minerals in tailings, the invention adopts a combined process of weak magnetic separation and strong magnetic separation and a centrifuge pre-enrichment process to effectively remove impurities and obtain a micro-fine particle tantalum-niobium concentrate product. The method has the characteristics of simple process, high environmental benefit, good economic benefit, safety, environmental protection, maximum recovery of the tantalum-niobium rare resource, realization of comprehensive utilization of the resource and the like.
Description
Technical field
The present invention relates to a kind of technology that from tantalum niobium concentrate, reclaims fine tantalum niobium concentrate thing.
Background technology
Tantalum and niobium have fusing point height (tantalum is 2996 ℃, and niobium is 2468 ℃), ductility is good, steam forces down, corrosion resistance is strong and good characteristic such as thermal conductivity height, are the important source material of industry such as electronics, atomic energy, space travel, iron and steel, chemical industry.According to the statistics of international tantalum niobium research center (TIC), the 1996-1999 world is about 8% to tantalum niobium growth of requirement speed, and the growth rate of 2000-2002 is about 12%, estimates that 5-10 can keep the growth more than 15% from now on.In order to satisfy continuous growth, must handle poor, thin, assorted tantalum niobium concentrate stone to tantalum niobium demand.It is the technical barrier that domestic and international ore dressing circle needs to be resolved hurrily that the micro-size fraction heavy mineral reclaims, and makes full use of limited mineral resources, improves tantalum niobium concentrate thing recovery rate in ore-dressing, is efficiently to develop tantalum niobium concentrate resource development in future road.
Summary of the invention
The object of the present invention is to provide a kind of technology simple, environmental benefit is high, the good in economic efficiency technology that from tantalum niobium concentrate, reclaims fine tantalum niobium concentrate thing.
For realizing above-mentioned purpose; A kind of technology that from tantalum niobium concentrate, reclaims fine tantalum niobium concentrate thing of the present invention; Comprise: utilize primary thin mud or secondary thin mud to reclaim fine tantalum niobium concentrate thing and utilize the tantalum niobium concentrate gravity tailings to reclaim fine tantalum niobium concentrate thing; Wherein, primary thin mud or secondary thin mud are handled through shaking table and are obtained fine tantalum-niobium concentrate through the centrifuge sorting; The tantalum niobium concentrate gravity tailings is removed the ferromagnetism irony through low intensity magnetic separation earlier, obtains the intermediate products that weak magnetic contains the tantalum niobium concentrate thing with high intensity magnetic separation again, and these intermediate products obtain fine tantalum-niobium concentrate through floatation desulphurization, acidleach.
Further, said primary thin mud is the thin mud that tantalum niobium concentrate Shi Po is produced in broken, and said secondary thin mud is the thin mud that grinding operation produces.
Further, said centrifuge is meant the preparation equipment of various employing centrifugal force reinforcement centrifugations used in the mineral manufacture field.
Further, said mine tailing is that tantalum niobium concentrate is through mine tailing after the gravity treatment or the mine tailing after coarse grain tantalum niobium concentrate, floatation recovery lepidolite are reclaimed in gravity treatment.
Further, the magnetic field intensity scope of said low intensity magnetic separation is 0.1T～0.6T.
Further, the low intensity magnetic separation machine of said low intensity magnetic separation employing comprises various dry type low intensity magnetic separation machines, wet type low intensity magnetic separation machine.
Further, the magnetic field intensity scope of said high intensity magnetic separation is 0.6T～1.6T.
Further, the intensity magnetic separator of said high intensity magnetic separation employing comprises various dry high-magnetic separation machines, Wet-type strong magnetic separator, high gradient magnetic separator.
The present invention is directed to primary or secondary thin mud and the microfine tantalum niobium concentrate thing in mine tailing of tantalum niobium concentrate in producing, adopt first low intensity magnetic separation, the sorting process of high intensity magnetic separation group technology, and centrifuge more effectively to remove impurity, obtain the tantalum-niobium concentrate product of micro-size fraction.It is simple to have technology, and environmental benefit is high, and good in economic efficiency, safety and environmental protection reclaims tantalum niobium scarce resource to greatest extent, realizes characteristics such as comprehensive utilization of resources.
Description of drawings
Fig. 1 utilizes the tantalum niobium concentrate mine tailing to reclaim the process chart of fine tantalum niobium concentrate thing;
Fig. 2 utilizes primary thin mud or secondary thin mud to reclaim the process chart of fine tantalum niobium concentrate thing.
The specific embodiment
Below, with reference to accompanying drawing, the present invention is more comprehensively explained, exemplary embodiment of the present invention has been shown in the accompanying drawing.Yet the present invention can be presented as multiple multi-form, and should not be construed as the exemplary embodiment that is confined to narrate here.But, these embodiment are provided, thereby make the present invention, and scope of the present invention is fully conveyed to those of ordinary skill in the art comprehensively with complete.
Like Fig. 1, shown in Figure 2, a kind of technology that from tantalum niobium concentrate, reclaims fine tantalum niobium concentrate thing of the present invention comprises: utilize primary thin mud or secondary thin mud to reclaim fine tantalum niobium concentrate thing and utilize the tantalum niobium concentrate mine tailing to reclaim fine tantalum niobium concentrate thing.
Wherein, When utilizing the tantalum niobium concentrate mine tailing to reclaim fine tantalum niobium concentrate thing; The tantalum niobium concentrate mine tailing is that coarse grain tantalum niobium concentrate thing or the mine tailing after coarse grain tantalum niobium concentrate thing, floatation recovery lepidolite are reclaimed in gravity treatment are reclaimed in gravity treatment; This mine tailing is removed the ferromagnetism irony through low intensity magnetic separation earlier, and the magnetic field intensity scope of low intensity magnetic separation is 0.1T～0.6T; Obtain the intermediate products that weak magnetic contains the tantalum niobium concentrate thing with high intensity magnetic separation again, the magnetic field intensity scope of high intensity magnetic separation is 0.6T～1.6T; Intermediate products obtain fine tantalum-niobium concentrate through floatation desulphurization, acidleach.
The low intensity magnetic separation machine that low intensity magnetic separation is adopted comprises various dry type low intensity magnetic separation machines, wet type low intensity magnetic separation machine, and the intensity magnetic separator that high intensity magnetic separation adopts comprises various dry high-magnetic separation machines, Wet-type strong magnetic separator, high gradient magnetic separator etc.
When utilizing primary thin mud or secondary thin mud to reclaim fine tantalum niobium, primary thin mud is the thin mud that tantalum niobium concentrate stone is produced in fragmentation, and secondary thin mud is the thin mud that grinding operation produces.Primary thin mud or secondary thin mud are handled through shaking table and are obtained fine tantalum-niobium concentrate through the centrifuge sorting.Employed centrifuge is meant the centrifuge of various employing centrifugal force reinforcement centrifugations used in the mineral manufacture field.
Process characteristic of the present invention is following:
2. primary or secondary thin mud is reclaimed technology through centrifuge, shaking table, obtain the micro-size fraction tantalum-niobium concentrate;
4. high intensity magnetic separation be variously do, Wet-type strong magnetic separator and high gradient magnetic separator;
5. centrifuge refers to the centrifugation apparatus of various employing centrifugal force reinforcement separating effects used in the mineral manufacture field.
6. technology is simple, and production cost is low; The tantalum niobium rate of recovery is high.
Technology applicable object of the present invention:
tantalum niobium concentrate resource comprehensive is recycled;
The recycling of tantalum niobium resource in the primary or secondary thin mud of
tantalum niobium concentrate;
The comprehensive utilization of the various mineral resources of
association tantalum niobium.
Case history:
(1) the Jiangxi tantalum niobium concentrate is tantalum niobium association lepidolite and feldspar, and tantalum niobium grade is low, belongs to the inhomogeneous embedding cloth of thickness, is main with particulate.Existing production technology adopts stage grinding stage grading technology sorting tantalum niobium.The capital equipment that reclaims the employing of tantalum niobium is spiral chute and shaking table, and optimum recovery grade scope is-0.2mm+0.038mm, and the following micro-size fraction tantalum niobium concentrate of right-0.038mm thing recovering effect extreme difference.Therefore; The tantalum niobium that in the recovery tantalum niobium in this ore deposit and the mine tailing behind the lepidolite, loses surpasses 90% and is fine tantalum niobium concentrate thing;--------flotation----acid leaching process reclaims fine tantalum niobium concentrate thing to high intensity magnetic separation, is 0.0138% Ta to head grade to the low intensity magnetic separation in this mine tailing employing technology of the present invention
2O
5Mine tailing, obtain fine tantalum-niobium concentrate grade 22.56% Ta
2O
5, operation recovery is greater than 75%.
(2) Fujian tantalum niobium concentrate industry company has the highest tantalum niobium concentrate mountain of domestic grade, its head grade＞0.03%Ta
2O
5, the tantalum-niobium concentrate grade and the rate of recovery that the said firm produces all are in domestic higher level, obtain technical indicator and economic benefit preferably.But because tantalum niobium resource itself exists the mineral disseminated grain size inhomogeneous, than great, property is crisp, very easily produces thin mud in the production process.Production technology is difficult to the fine tantalum niobium concentrate thing in these thin mud is effectively reclaimed at present.Adopting centrifuge the sorting----shaking table among the present invention to reclaim technology, is 0.013% Ta for primary thin mud grade
2O
5, can obtain tantalum-niobium concentrate grade 29.10% Ta
2O
5, the rate of recovery 41.44%; For secondary thin mud head grade 0.014%Ta
2O
5, obtain tantalum-niobium concentrate grade 12.06% Ta
2O
5, the rate of recovery 46.02%.
To sum up two examples it is thus clear that this technology can effectively improve the rate of recovery of fine tantalum niobium concentrate thing, realize the comprehensive recovery of tantalum niobium resource.
Claims (8)
1. technology that from tantalum niobium concentrate, reclaims fine tantalum niobium; It is characterized in that; This technology comprises: utilize primary thin mud or secondary thin mud to reclaim fine tantalum niobium concentrate thing and utilize the tantalum niobium concentrate gravity tailings to reclaim fine tantalum niobium concentrate thing; Wherein, primary thin mud or secondary thin mud are handled through shaking table and are obtained fine tantalum-niobium concentrate through the centrifuge sorting; The tantalum niobium concentrate gravity tailings is removed the ferromagnetism irony through low intensity magnetic separation earlier, obtains the intermediate products that weak magnetic contains the tantalum niobium concentrate thing with high intensity magnetic separation again, and these intermediate products obtain fine tantalum-niobium concentrate through floatation desulphurization, acidleach.
2. the technology that from tantalum niobium concentrate, reclaims fine tantalum niobium concentrate thing as claimed in claim 1 is characterized in that, said primary thin mud is the thin mud that tantalum niobium concentrate Shi Po is produced in broken, and said secondary thin mud is the thin mud that grinding operation produces.
3. the technology that from tantalum niobium concentrate, reclaims fine tantalum niobium concentrate thing as claimed in claim 2 is characterized in that, said centrifuge is meant the equipment of various employing centrifugal force reinforcement centrifugations used in the mineral manufacture field.
4. the technology that from tantalum niobium concentrate, reclaims fine tantalum niobium concentrate thing as claimed in claim 1 is characterized in that, said tantalum niobium concentrate mine tailing is to reclaim coarse grain tantalum niobium or the mine tailing after coarse grain tantalum niobium concentrate thing, floatation recovery lepidolite are reclaimed in gravity treatment through gravity treatment.
5. the technology that from tantalum niobium concentrate, reclaims fine tantalum niobium concentrate thing as claimed in claim 4 is characterized in that the magnetic field intensity scope of said low intensity magnetic separation is 0.1T～0.6T.
6. the technology that from tantalum niobium concentrate, reclaims fine tantalum niobium as claimed in claim 4 is characterized in that the low intensity magnetic separation machine that said low intensity magnetic separation is adopted comprises various dry type low intensity magnetic separation machines, wet type low intensity magnetic separation machine.
7. the technology that from tantalum niobium concentrate, reclaims fine tantalum niobium concentrate thing as claimed in claim 4 is characterized in that the magnetic field intensity scope of said high intensity magnetic separation is 0.6T～1.6T.
8. the technology that from tantalum niobium concentrate, reclaims fine tantalum niobium concentrate thing as claimed in claim 4 is characterized in that the intensity magnetic separator that said high intensity magnetic separation adopts comprises various dry high-magnetic separation machines, Wet-type strong magnetic separator, high gradient magnetic separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011102945115A CN102441483A (en) | 2011-09-28 | 2011-09-28 | Process for recovering superfine tantalum-niobium minerals from tantalum-niobium ores |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011102945115A CN102441483A (en) | 2011-09-28 | 2011-09-28 | Process for recovering superfine tantalum-niobium minerals from tantalum-niobium ores |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102441483A true CN102441483A (en) | 2012-05-09 |
Family
ID=46004711
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011102945115A Pending CN102441483A (en) | 2011-09-28 | 2011-09-28 | Process for recovering superfine tantalum-niobium minerals from tantalum-niobium ores |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102441483A (en) |
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102836777A (en) * | 2012-09-18 | 2012-12-26 | 镇康县金宏矿业有限公司 | Ore dressing technology for comprehensively recovering lean and fine wiikite |
| CN103846154A (en) * | 2012-12-05 | 2014-06-11 | 核工业北京地质研究院 | Method of recycling tin, niobium and tantalum from smelted tailings |
| CN105057091A (en) * | 2015-09-23 | 2015-11-18 | 江西金辉环保科技有限公司 | Method for recycling niobium-tantalum concentrate from niobium-tantalum waste ore |
| CN105080705A (en) * | 2015-09-23 | 2015-11-25 | 江西金辉环保科技有限公司 | Method for preparing various minerals from tantalum-niobium ores through combined magnetic separation |
| CN105126993A (en) * | 2015-08-21 | 2015-12-09 | 西北矿冶研究院 | Comprehensive recovery process for associated tantalum-niobium ore |
| CN105251606A (en) * | 2014-12-29 | 2016-01-20 | 江西金辉环保科技有限公司 | Refining process for lepidolite in tantalum-niobium ore waste rocks |
| CN105312147A (en) * | 2014-12-29 | 2016-02-10 | 江西金辉环保科技有限公司 | A method for extracting minute quantities (Ta, nb)2O5from TaNb ore gangue |
| RU2574089C1 (en) * | 2014-12-10 | 2016-02-10 | Закрытое акционерное общество "ТЕХНОИНВЕСТ АЛЬЯНС" | Enrichment of tantalum-niobium ores by gravitational and magnetic method |
| CN105964401A (en) * | 2016-04-28 | 2016-09-28 | 中国地质科学院矿产综合利用研究所 | Mineral separation process for high-iron nepheline ore |
| CN106216087A (en) * | 2016-07-07 | 2016-12-14 | 张宝臣 | A kind of method using magnetic separator enrichment copper-lead zinc in mine tailing |
| CN106378254A (en) * | 2016-12-09 | 2017-02-08 | 江西金辉再生资源股份有限公司 | Method for removing magnetic impurities from tantalum-niobium waste ores by utilizing combined magnetic separation |
| CN106423554A (en) * | 2016-12-09 | 2017-02-22 | 江西金辉再生资源股份有限公司 | Method using tailing sand united concentration to prepare potassium-sodium feldspar powder |
| CN104437825B (en) * | 2013-09-18 | 2017-03-15 | 北京有色金属研究总院 | A kind of ore-dressing technique for processing the niobium minerals of particulate containing mud |
| CN106583051A (en) * | 2016-12-23 | 2017-04-26 | 中国地质科学院矿产综合利用研究所 | Method for full-sludge flotation co-enrichment recovery of lithium niobium tantalum multi-metal resources |
| CN107243406A (en) * | 2016-08-29 | 2017-10-13 | 赣州金环磁选设备有限公司 | A kind of method of the feldspar of niobium containing tantalum tailing resource recycling |
| CN108787158A (en) * | 2018-05-22 | 2018-11-13 | 北京矿冶科技集团有限公司 | The recycling beneficiation method of fine- disseminated ore in a kind of uranium-bearing polymetallic ore |
| CN109127117A (en) * | 2018-11-01 | 2019-01-04 | 中钢集团马鞍山矿山研究院有限公司 | A kind of beneficiation method of spodumene ore |
| CN109290049A (en) * | 2018-09-25 | 2019-02-01 | 内蒙古扎鲁特旗鲁安矿业有限公司 | A kind of radioactive beneficiation method of quartzy feldspar concentrate of removal |
| CN111068898A (en) * | 2019-12-06 | 2020-04-28 | 核工业北京化工冶金研究院 | Method for producing bulk concentrate by mineral separation from polymetallic ore |
| CN112452532A (en) * | 2020-11-04 | 2021-03-09 | 湖北省地质实验测试中心(国土资源部武汉矿产资源监督检测中心) | Comprehensive recovery process of low-grade fine-grain niobium-tantalum ore |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101658816A (en) * | 2009-09-16 | 2010-03-03 | 中国瑞林工程技术有限公司 | Mineral separating process for electively recovering tantalum-niobium ores |
| CN101733191A (en) * | 2008-11-13 | 2010-06-16 | 常福松 | Oredressing method for tantalum-niobium ore |
-
2011
- 2011-09-28 CN CN2011102945115A patent/CN102441483A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101733191A (en) * | 2008-11-13 | 2010-06-16 | 常福松 | Oredressing method for tantalum-niobium ore |
| CN101658816A (en) * | 2009-09-16 | 2010-03-03 | 中国瑞林工程技术有限公司 | Mineral separating process for electively recovering tantalum-niobium ores |
Non-Patent Citations (3)
| Title |
|---|
| 周晓彤等: "钨细泥重-浮-重选矿新工艺的研究", 《材料研究与应用》 * |
| 熊上暤: "某难选钽铌钨铍多金属矿石的选矿研究", 《江西有色金属》 * |
| 高玉德: "细粒钽铌矿浮选研究", 《中国优秀博硕士学位论文（硕士工程科技I辑）》 * |
Cited By (27)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102836777A (en) * | 2012-09-18 | 2012-12-26 | 镇康县金宏矿业有限公司 | Ore dressing technology for comprehensively recovering lean and fine wiikite |
| CN102836777B (en) * | 2012-09-18 | 2013-11-27 | 镇康县金宏矿业有限公司 | Ore dressing technology for comprehensively recovering leand fine wiikite |
| CN103846154A (en) * | 2012-12-05 | 2014-06-11 | 核工业北京地质研究院 | Method of recycling tin, niobium and tantalum from smelted tailings |
| CN104437825B (en) * | 2013-09-18 | 2017-03-15 | 北京有色金属研究总院 | A kind of ore-dressing technique for processing the niobium minerals of particulate containing mud |
| RU2574089C1 (en) * | 2014-12-10 | 2016-02-10 | Закрытое акционерное общество "ТЕХНОИНВЕСТ АЛЬЯНС" | Enrichment of tantalum-niobium ores by gravitational and magnetic method |
| CN105251606B (en) * | 2014-12-29 | 2017-11-21 | 江西金辉环保科技有限公司 | The refining technique of lepidolite in a kind of tantalum niobium concentrate barren rock |
| CN105251606A (en) * | 2014-12-29 | 2016-01-20 | 江西金辉环保科技有限公司 | Refining process for lepidolite in tantalum-niobium ore waste rocks |
| CN105312147A (en) * | 2014-12-29 | 2016-02-10 | 江西金辉环保科技有限公司 | A method for extracting minute quantities (Ta, nb)2O5from TaNb ore gangue |
| CN105126993A (en) * | 2015-08-21 | 2015-12-09 | 西北矿冶研究院 | Comprehensive recovery process for associated tantalum-niobium ore |
| CN105057091A (en) * | 2015-09-23 | 2015-11-18 | 江西金辉环保科技有限公司 | Method for recycling niobium-tantalum concentrate from niobium-tantalum waste ore |
| CN105080705A (en) * | 2015-09-23 | 2015-11-25 | 江西金辉环保科技有限公司 | Method for preparing various minerals from tantalum-niobium ores through combined magnetic separation |
| CN105964401A (en) * | 2016-04-28 | 2016-09-28 | 中国地质科学院矿产综合利用研究所 | Mineral separation process for high-iron nepheline ore |
| CN105964401B (en) * | 2016-04-28 | 2017-05-10 | 中国地质科学院矿产综合利用研究所 | Mineral separation process for high-iron nepheline ore |
| CN106216087B (en) * | 2016-07-07 | 2018-04-24 | 张宝臣 | A kind of method for being enriched with copper-lead zinc using magnetic separator in tailing |
| CN106216087A (en) * | 2016-07-07 | 2016-12-14 | 张宝臣 | A kind of method using magnetic separator enrichment copper-lead zinc in mine tailing |
| CN107243406A (en) * | 2016-08-29 | 2017-10-13 | 赣州金环磁选设备有限公司 | A kind of method of the feldspar of niobium containing tantalum tailing resource recycling |
| CN106423554A (en) * | 2016-12-09 | 2017-02-22 | 江西金辉再生资源股份有限公司 | Method using tailing sand united concentration to prepare potassium-sodium feldspar powder |
| CN106378254A (en) * | 2016-12-09 | 2017-02-08 | 江西金辉再生资源股份有限公司 | Method for removing magnetic impurities from tantalum-niobium waste ores by utilizing combined magnetic separation |
| CN106583051A (en) * | 2016-12-23 | 2017-04-26 | 中国地质科学院矿产综合利用研究所 | Method for full-sludge flotation co-enrichment recovery of lithium niobium tantalum multi-metal resources |
| CN106583051B (en) * | 2016-12-23 | 2019-08-23 | 中国地质科学院矿产综合利用研究所 | Method for full-sludge flotation co-enrichment recovery of lithium niobium tantalum multi-metal resources |
| CN108787158B (en) * | 2018-05-22 | 2020-09-25 | 北京矿冶科技集团有限公司 | Recovery beneficiation method for micro-fine particle ore in uranium-containing polymetallic ore |
| CN108787158A (en) * | 2018-05-22 | 2018-11-13 | 北京矿冶科技集团有限公司 | The recycling beneficiation method of fine- disseminated ore in a kind of uranium-bearing polymetallic ore |
| CN109290049A (en) * | 2018-09-25 | 2019-02-01 | 内蒙古扎鲁特旗鲁安矿业有限公司 | A kind of radioactive beneficiation method of quartzy feldspar concentrate of removal |
| CN109290049B (en) * | 2018-09-25 | 2021-01-26 | 内蒙古扎鲁特旗鲁安矿业有限公司 | Beneficiation method for removing radioactivity of quartz feldspar concentrate |
| CN109127117A (en) * | 2018-11-01 | 2019-01-04 | 中钢集团马鞍山矿山研究院有限公司 | A kind of beneficiation method of spodumene ore |
| CN111068898A (en) * | 2019-12-06 | 2020-04-28 | 核工业北京化工冶金研究院 | Method for producing bulk concentrate by mineral separation from polymetallic ore |
| CN112452532A (en) * | 2020-11-04 | 2021-03-09 | 湖北省地质实验测试中心(国土资源部武汉矿产资源监督检测中心) | Comprehensive recovery process of low-grade fine-grain niobium-tantalum ore |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102441483A (en) | Process for recovering superfine tantalum-niobium minerals from tantalum-niobium ores | |
| CN102489386B (en) | Method for separating fine cassiterite | |
| CN108525843A (en) | Utilize the method for difficult mine solid waste recycling tantalum niobium, lepidolite and feldspar powder | |
| CA2899283C (en) | Method for separating a defined mineral phase of value from a ground ore | |
| Zhu et al. | Recovery of high-grade copper from waste printed circuit boards by mechanical-grinding assisted flotation | |
| CN106378254A (en) | Method for removing magnetic impurities from tantalum-niobium waste ores by utilizing combined magnetic separation | |
| WO2012167519A1 (en) | Comprehensive process for reclaiming metallic copper from high-grade furnace slag containing copper | |
| CN102631977A (en) | Beneficiation method for ultrafine fraction cassiterite | |
| CN105251606A (en) | Refining process for lepidolite in tantalum-niobium ore waste rocks | |
| CN104437825B (en) | A kind of ore-dressing technique for processing the niobium minerals of particulate containing mud | |
| CN105312148A (en) | Beneficiation and enrichment method suitable for associated scheelite in molybdenite flotation tailings | |
| CN105478232B (en) | A kind of beneficiation method from graphite mould navajoite enrichment vanadic anhydride | |
| CN103962232A (en) | Rare earth ore beneficiation method | |
| CN107583764B (en) | Beneficiation method for recovering mica from copper ore tailings | |
| CN103567051A (en) | Small-scale lean hematite separation technology | |
| CN102259053A (en) | Method for recovering iron resources in reverse flotation tailings | |
| WO2014063211A1 (en) | Iron ore concentration process with grinding circuit, dry desliming and dry or mixed (dry and wet) concentration | |
| CN102861662A (en) | Ore dressing method of micro-fine particle tantalum-niobium ores | |
| CN106583023A (en) | Beneficiation method for microgranular cassiterite | |
| CN104190533B (en) | Method for recovering quartz in iron tailing and quartz mine prepared by same | |
| CN105233977B (en) | Magnetic separation recovery mine tailing technique is regrinded in magnetic separation circulation roasting | |
| CN104437833A (en) | Physical upgrading method for enrichment of carbonaceous shale type vanadium ore | |
| CN110813517A (en) | Beneficiation method for recycling wolframite from tailings | |
| CN107149979A (en) | A kind of method that iron is reclaimed in the revolution kiln slag from zinc hydrometallurgy | |
| CN104190528A (en) | Method for recycling ultra-fine fraction titanic iron ore and production method for titanium concentrate |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20120509 |