CN1477217A - Leaching process of zinc oxide ore - Google Patents
Leaching process of zinc oxide ore Download PDFInfo
- Publication number
- CN1477217A CN1477217A CNA021336636A CN02133663A CN1477217A CN 1477217 A CN1477217 A CN 1477217A CN A021336636 A CNA021336636 A CN A021336636A CN 02133663 A CN02133663 A CN 02133663A CN 1477217 A CN1477217 A CN 1477217A
- Authority
- CN
- China
- Prior art keywords
- zinc oxide
- leaching
- oxide ore
- neutral
- zinc
- 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.)
- Granted
Links
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 title claims abstract description 51
- 239000011787 zinc oxide Substances 0.000 title claims abstract description 25
- 238000002386 leaching Methods 0.000 title claims description 19
- 238000000034 method Methods 0.000 title abstract description 11
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 28
- 239000011701 zinc Substances 0.000 claims abstract description 28
- 239000007788 liquid Substances 0.000 claims abstract description 21
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 18
- 230000007935 neutral effect Effects 0.000 claims abstract description 18
- 239000002253 acid Substances 0.000 claims abstract description 10
- 238000003756 stirring Methods 0.000 claims abstract description 9
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 7
- 239000002699 waste material Substances 0.000 claims abstract description 7
- 238000000926 separation method Methods 0.000 claims description 10
- 238000005516 engineering process Methods 0.000 claims description 9
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 5
- 239000011593 sulfur Substances 0.000 claims description 5
- 229910052717 sulfur Inorganic materials 0.000 claims description 5
- 229910000010 zinc carbonate Inorganic materials 0.000 claims description 5
- 239000011021 lapis lazuli Substances 0.000 claims description 3
- 230000035484 reaction time Effects 0.000 claims description 2
- 239000002562 thickening agent Substances 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 24
- 239000002893 slag Substances 0.000 abstract description 19
- 229910052742 iron Inorganic materials 0.000 abstract description 13
- 239000000463 material Substances 0.000 abstract 1
- 229920001296 polysiloxane Polymers 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 21
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 10
- 229910052710 silicon Inorganic materials 0.000 description 10
- 239000010703 silicon Substances 0.000 description 10
- 238000011084 recovery Methods 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 4
- 230000003472 neutralizing effect Effects 0.000 description 4
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 4
- 229960001763 zinc sulfate Drugs 0.000 description 4
- 229910000368 zinc sulfate Inorganic materials 0.000 description 4
- 229910004298 SiO 2 Inorganic materials 0.000 description 3
- 239000005083 Zinc sulfide Substances 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 230000007062 hydrolysis Effects 0.000 description 3
- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 235000010755 mineral Nutrition 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- DRDVZXDWVBGGMH-UHFFFAOYSA-N zinc;sulfide Chemical compound [S-2].[Zn+2] DRDVZXDWVBGGMH-UHFFFAOYSA-N 0.000 description 3
- FMRLDPWIRHBCCC-UHFFFAOYSA-L Zinc carbonate Chemical compound [Zn+2].[O-]C([O-])=O FMRLDPWIRHBCCC-UHFFFAOYSA-L 0.000 description 2
- 239000004110 Zinc silicate Substances 0.000 description 2
- 229910052793 cadmium Inorganic materials 0.000 description 2
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 2
- 230000003301 hydrolyzing effect Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- -1 iron ion Chemical class 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000011667 zinc carbonate Substances 0.000 description 2
- 235000004416 zinc carbonate Nutrition 0.000 description 2
- XSMMCTCMFDWXIX-UHFFFAOYSA-N zinc silicate Chemical compound [Zn+2].[O-][Si]([O-])=O XSMMCTCMFDWXIX-UHFFFAOYSA-N 0.000 description 2
- 235000019352 zinc silicate Nutrition 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
- 238000005363 electrowinning Methods 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 238000009854 hydrometallurgy Methods 0.000 description 1
- 239000003978 infusion fluid Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000002620 method output Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 229910052984 zinc sulfide Inorganic materials 0.000 description 1
Classifications
-
- 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 present invention relates to a leaching-out method of zinc ore containing high iron and silicone. It includes the following steps: (1). neutral leaching-out, simultaneously adding zinc oxide powder and solution containing sulfuric acid and stirring, progressively raising pH value to 5-5.2 from initial 3.0-3.5, and purifying the reacted neutral leach and using it for electrolysis, and using the leached slag make next leaching-out; (2). low acid leaching-out, in the leached slag adding sulfuric acid solution and stirring, controlling pH value and making it progressively be reduced to 1.5-3.0 from 5-5.2; and (3). circulating waste liquor, solid-liquid separating second leached material, and returning the waste liquor contaiing sulfuric acid into neutral leaching-out stage of zinc oxide ore.
Description
Technical field
The invention belongs to and belong to hydrometallurgical technology, particularly contain the leaching method of the zinc ore of high ferro, silicon.
Technical background
When tradition adopted hydrometallurgy from ore lixiviate zinc, generally all adopting zinc sulfide ore was raw material, and rate is higher because it contains zinc, and lixiviate is easier to relatively.Along with exploitation all the year round, the source in this ore deposit is fewer and feweri, and grade also reduces gradually, and people have now begun to note the utilization of zinc oxide ore.But it is lower that zinc oxide ore contains the zinc rate usually, and complicated component, how to exist with smithsonite and lapis calaminaris, and the iron in the ore deposit, silicon, calcium contents are many, and lixiviate is difficulty.Both at home and abroad be mostly in recent years to the method (as the method for Kunming Inst. of Metallurgy Du Shu branch) of the lixiviate of zinc oxide ore, with the solution of zinc sulfate that contains strong acid zinc oxide ore is leached, terminal point is controlled at PH1, make compositions such as zinc in the ore deposit, iron, silicon enter in the solution in a large number, and then with the neutralization of limestone powder or lime, remove iron, silicon in the solution, when being neutralized to PH5.2, silicon and iron sink in the slag, output " desiliconization slag " and solution of zinc sulfate are removed electrodeposition output electricity zinc behind the impurity in the solution with zinc powder." desiliconization slag " of this method output is quite loose, heavy clear poor-performing, and the water ratio that filters the back slag is very high, so zinc is also very big with the loss amount of slag; If reclaim zinc in the slag with washing methods, then water consumption is very big; Though the zinc leaching rate height of this method, but the iron, the silicon amount that enter solution are also high, in the hydrolysis of neutralization stage along with iron ion, can produce acid again, this needs this part acid that neutralizes of more neutralizing agent again, and the result is a large amount of gypsum of output again, have both increased the quantity of slag, also increased neutralizing agent and vitriolic consumption, so the zinc oxide ore that this art breading is siliceous, iron is high is uneconomic.Many metallargists both domestic and external think, zinc content is lower than 20% zinc oxide ore should not be handled with the wet method extract technology separately.
Summary of the invention
Technical problem to be solved by this invention provides a kind of extract technology of zinc oxide ore, can be lower than 20% zinc oxide ore and leach containing zinc with wet method, production cost is low, the sulfuric acid consumption is few, do not consume neutralizing agent, leach liquor can be recycled, and can obtain to contain the high solution of zinc sulfate of zinc, the leaching yield height of zinc.
Solving the technological step that technical problem of the present invention adopts is:
(1) the neutral leaching, add in the leaching vat simultaneously zinc oxide breeze and sulfur acid solution and stirring, the pH value that adds solution during beginning is 3.0～3.5, the pH value of solution gradually rises, finally reach PH5～5.2, reacted neutral leach liquor is made electrolysis usefulness for clean liquid, and leached mud carries out next step and leaches;
(2) hang down acidleach and go out, add sulfuric acid liquid and stirring in leached mud, the control pH value descends gradually, drops to PH1.5～3.0 by PH5～5.2 that begin;
(3) circulate soln carries out solid-liquid separation to the secondary extract, contains the neutrality leaching stage that the vitriolic waste liquid returns zinc oxide ore again.The neutral leach liquor of also available part returns neutral the leaching after adding sulfuric acid, by the circulation of solution, improves zinc ion concentration in the solution, with purification and the electrolysis that adapts to next step.
In the technical scheme of above-mentioned proposition, main component contained in the zinc oxide ore is smithsonite and lapis calaminaris, and the zinc rate that contains in the ore is 〉=15%.
Reaction times in the neutral leaching stage of zinc oxide breeze is 120～180 minutes, and the time that low acidleach goes out the stage is 120～240 minutes.
The neutrality of technology of the present invention leaches to be preferably in the continuously arranged leaching vat carries out continuously, leaches the back solid-liquid separation and adopts thickener to carry out.
In neutral leaching the of the present invention, the pH value of having controlled infusion solution rises to final PH5～5.2 gradually by initial PH3.0～3.5, under this pH value, most zinc contained in the ore is leached, iron and silicon hydrolytic precipitation promptly again under such condition simultaneously, this has just been avoided impurity such as silicon, iron to enter solution, for electrowinning process provides qualified solution of zinc sulfate, and has avoided in the ordinary method neutralizing agent and vitriolic consumption; In for the second time the low acidleach of leached mud being gone out, pH value drops to final PH1.5～3.0 gradually by initial PH5～5.2 again, and zinc is leached more up hill and dale, under the state of beginning solution partial neutral, in the slag the iron of hydrolysis can precipitate, avoided iron ion to enter in the leach liquor SiO in a large number
2Then become " crystal seed ", combine, precipitate, suppress it and enter solution in a large number,, the zinc that remains in the slag is leached again, thereby improve the leaching yield of zinc greatly when pH value reduces when getting off with the silicon of new hydrolysis.Solution after low acidleach goes out contains a certain amount of sulfuric acid, can return neutral extracting stage again and recycle, and contained minor amount of silicon and iron can very fast hydrolytic precipitation when neutrality leaches in the solution.
Embodiment
Embodiment 1: choose zinc oxide ore, its chemical ingredients is Zn26.55%, Fe18.20%, SiO
27.94%, wherein the zinc thing coordinates and is divided into, zinc carbonate 24.23%, zinc silicate 1.25%, zinc sulphide 0.73%, automolite 0.34%, behind the mineral pulverizing and jevigating, carrying out neutrality with waste electrolyte leaches, be that condition is that initial value is PH3, terminal point PH5.2 evenly stirs minutes 120～180 minutes; Carry out solid-liquid separation, leach liquor is made electrolysis usefulness for clean liquid, adds sulfur acid solution in the leached mud and hang down acidleach and goes out, and pH value drops to PH1.5 gradually by the PH5.2 that begins, solid-liquid separation again, and supernatant liquor returns neutral extracting stage and recycles.Each leading indicator is as follows:
Zinc leaches the rate of recovery: 91.88%
Cadmium leaches the rate of recovery: 95.86%
Slag rate: 55.45%
Slag contains zinc: 3.89%
Slag filtration velocity: 52.5kg/m
2h
Embodiment 2: choose high siliceous zinc oxide ore, its chemical ingredients is Zn21.68%, Fe17.95%, SiO
218.91%, CaO6.65% as the same example, behind the mineral pulverizing and jevigating, carries out neutrality with waste electrolyte and leaches, and promptly condition is that initial value is PH3, and terminal point PH5.2 evenly stirs minutes 120～180 minutes; Carry out solid-liquid separation, leach liquor is made electrolysis usefulness for clean liquid, adds sulfur acid solution in the leached mud and hang down acidleach and goes out, and pH value drops to PH2.0 gradually by the PH5.2 that begins, solid-liquid separation again, and supernatant liquor returns neutral extracting stage and recycles.Each leading indicator is as follows:
Zinc leaches the rate of recovery: 89.7%
Acid leaching ore pulp filtration velocity: 606.2L/m
2h
Slag rate: 64.5%
Slag contains zinc: 3.46%
Embodiment 3: choose zinc oxide concentrate, its chemical ingredients is Zn26.55%, Fe18.20%, SiO
27.94%, wherein the zinc thing coordinates and is divided into, zinc carbonate 24.23%, zinc silicate 1.25%, zinc sulphide 0.73%, automolite 0.34%, behind the mineral pulverizing and jevigating, carrying out neutrality with waste electrolyte leaches, be that condition is that initial value is PH3, terminal point PH5.2 evenly stirs minutes 120～180 minutes; Carry out solid-liquid separation, leach liquor is made electrolysis usefulness for clean liquid, adds sulfur acid solution in the leached mud and hang down acidleach and goes out, and pH value drops to PH1.5 gradually by the PH5.2 that begins, solid-liquid separation again, and supernatant liquor returns neutral extracting stage and recycles.Each leading indicator is as follows:
Zinc leaches the rate of recovery: 91.88%
Cadmium leaches the rate of recovery: 95.86%
Slag rate: 55.45%
Slag contains zinc: 3.89%
Slag filtration velocity: 52.5kg/m
2h
Claims (4)
1, a kind of extract technology of zinc oxide ore is characterized in that step is as follows:
(1) the neutral leaching, add in the leaching vat simultaneously zinc oxide breeze and sulfur acid solution and stirring, the pH value that adds sulfuric acid liquid during beginning is 3.0～3.5, the pH value of solution gradually rises, finally reach PH5～5.2, reacted neutral leach liquor is made electrolysis usefulness for clean liquid, and leached mud carries out next step and leaches;
(2) hang down acidleach and go out, add sulfuric acid liquid and stirring in leached mud, the control pH value descends gradually, drops to PH1.5～3.0 by PH5～5.2 that begin;
(3) circulate soln carries out solid-liquid separation to the secondary extract, contains the neutrality leaching stage that the vitriolic waste liquid returns zinc oxide ore again.
2, by the extract technology of the described zinc oxide ore of claim 1, it is characterized in that the main component of the zinc oxide ore that adopted is smithsonite and lapis calaminaris, the zinc rate that contains in the ore is 15%～40%.
3, by the extract technology of the described zinc oxide ore of claim 2, it is characterized in that the neutral reaction times of leaching is 120～180 minutes, the time that low acidleach goes out is 120～240 minutes.
4, by the extract technology of the described zinc oxide ore of claim 3, it is characterized in that neutral the leaching carry out continuously in continuously arranged leaching vat, leach the back solid-liquid separation and adopt thickener.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021336636A CN1236081C (en) | 2002-08-24 | 2002-08-24 | Leaching process of zinc oxide ore |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021336636A CN1236081C (en) | 2002-08-24 | 2002-08-24 | Leaching process of zinc oxide ore |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1477217A true CN1477217A (en) | 2004-02-25 |
| CN1236081C CN1236081C (en) | 2006-01-11 |
Family
ID=34145630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB021336636A Expired - Lifetime CN1236081C (en) | 2002-08-24 | 2002-08-24 | Leaching process of zinc oxide ore |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1236081C (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101838745A (en) * | 2010-04-15 | 2010-09-22 | 赤峰中色库博红烨锌业有限公司 | Zinc hydrometallurgy process with high yield by precipitating alum and removing iron |
| CN101713031B (en) * | 2009-10-26 | 2011-05-18 | 德阳市南邡有色金属有限公司 | Method for removing impurities by oxidation in process of zinc hydrometallurgy |
| CN102703694A (en) * | 2012-06-15 | 2012-10-03 | 广西金山铟锗冶金化工有限公司 | Method for treating low-grade zinc oxide ores by wet method |
| CN102703690A (en) * | 2012-06-15 | 2012-10-03 | 广西金山铟锗冶金化工有限公司 | Method for separating high-ferrosilicon complex zinc oxide lean ores through combined treatment |
| CN103911518A (en) * | 2012-12-31 | 2014-07-09 | 北京有色金属研究总院 | Method for efficiently fully leaching zinc from dust caused by making steel from waste galvanized plates |
| CN104131176A (en) * | 2014-08-01 | 2014-11-05 | 昆明理工大学 | Method for recovery of zinc by ultrasonic neutral leaching of zinc oxide flue dust |
| US9512502B2 (en) | 2012-09-25 | 2016-12-06 | Sichuan Xinhong Technology Co., Ltd | Method for producing a high-purity nanometer zinc oxide from low-grade zinc oxide ore by ammonia decarburization |
| CN108642280A (en) * | 2018-07-16 | 2018-10-12 | 四环锌锗科技股份有限公司 | A method of improving comprehensive recovery system zinc recovery |
| CN111485120A (en) * | 2020-04-03 | 2020-08-04 | 河南豫光锌业有限公司 | Method for reducing tin content in zinc oxide solution |
| CN111519040A (en) * | 2020-05-12 | 2020-08-11 | 云南金鼎锌业有限公司 | Zinc oxide concentrate leaching equipment and leaching mode thereof |
| CN112690289A (en) * | 2020-12-25 | 2021-04-23 | 南昌大学 | Antibacterial mildew preventive and preparation method thereof |
-
2002
- 2002-08-24 CN CNB021336636A patent/CN1236081C/en not_active Expired - Lifetime
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101713031B (en) * | 2009-10-26 | 2011-05-18 | 德阳市南邡有色金属有限公司 | Method for removing impurities by oxidation in process of zinc hydrometallurgy |
| CN101838745A (en) * | 2010-04-15 | 2010-09-22 | 赤峰中色库博红烨锌业有限公司 | Zinc hydrometallurgy process with high yield by precipitating alum and removing iron |
| CN102703694A (en) * | 2012-06-15 | 2012-10-03 | 广西金山铟锗冶金化工有限公司 | Method for treating low-grade zinc oxide ores by wet method |
| CN102703690A (en) * | 2012-06-15 | 2012-10-03 | 广西金山铟锗冶金化工有限公司 | Method for separating high-ferrosilicon complex zinc oxide lean ores through combined treatment |
| US9512502B2 (en) | 2012-09-25 | 2016-12-06 | Sichuan Xinhong Technology Co., Ltd | Method for producing a high-purity nanometer zinc oxide from low-grade zinc oxide ore by ammonia decarburization |
| CN103911518B (en) * | 2012-12-31 | 2016-03-30 | 北京有色金属研究总院 | A kind of efficient method fully leaching zinc in waste galvanized plate fume from steel making |
| CN103911518A (en) * | 2012-12-31 | 2014-07-09 | 北京有色金属研究总院 | Method for efficiently fully leaching zinc from dust caused by making steel from waste galvanized plates |
| CN104131176A (en) * | 2014-08-01 | 2014-11-05 | 昆明理工大学 | Method for recovery of zinc by ultrasonic neutral leaching of zinc oxide flue dust |
| CN104131176B (en) * | 2014-08-01 | 2016-09-21 | 昆明理工大学 | A kind of ultrasound wave neutrality leaches the method that zinc oxide fumes reclaims zinc |
| CN108642280A (en) * | 2018-07-16 | 2018-10-12 | 四环锌锗科技股份有限公司 | A method of improving comprehensive recovery system zinc recovery |
| CN111485120A (en) * | 2020-04-03 | 2020-08-04 | 河南豫光锌业有限公司 | Method for reducing tin content in zinc oxide solution |
| CN111519040A (en) * | 2020-05-12 | 2020-08-11 | 云南金鼎锌业有限公司 | Zinc oxide concentrate leaching equipment and leaching mode thereof |
| CN112690289A (en) * | 2020-12-25 | 2021-04-23 | 南昌大学 | Antibacterial mildew preventive and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1236081C (en) | 2006-01-11 |
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Owner name: YUNNAN XIANGYUN FEILONG REGENERATION TECHNOLOGY CO Free format text: FORMER NAME: YUNNAN XIANGYUN FEILONG NONFERROUS METALS CO., LTD.;XIAMEN STARMEM TECHNOLOGY CO., LTD. |
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Denomination of invention: Leaching process of zinc oxide ore Effective date of registration: 20140613 Granted publication date: 20060111 Pledgee: China Development Bank Co. Pledgor: YUNNAN XIANGYUN FEILONG RECYCLING TECHNOLOGY Co.,Ltd. Registration number: 2014530000003 |
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