CN1030794A - The method of manufacturing zinc sulfate from sicica-rich zine oxide - Google Patents
The method of manufacturing zinc sulfate from sicica-rich zine oxide Download PDFInfo
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- CN1030794A CN1030794A CN87102024A CN87102024A CN1030794A CN 1030794 A CN1030794 A CN 1030794A CN 87102024 A CN87102024 A CN 87102024A CN 87102024 A CN87102024 A CN 87102024A CN 1030794 A CN1030794 A CN 1030794A
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- zinc sulfate
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Abstract
With the method for manufacturing zinc sulfate from sicica-rich zine oxide, belong to a kind of method of wet zinc smelter.
Method of the present invention is characterized in that, has adopted silicon to hinder molten acid leaching process in the acidleach operation, has set up the silica removal operation in oxidation and before removal of impurities operation and the exsiccation operation.Use method of the present invention, can utilize silicon oxide-containing to produce zinc sulfate for the zinc oxide ore of 10-30%, realize ordinary production, quality product reaches domestic standard laid down by the ministries or commissions of the Central Government secondary or primary standard.
The present invention utilizes chemical universaling equipment, less investment, and economic benefit is considerable, and this plays active and effective effect for the development and use that improve ore resource, and reduces the cost of producing zinc sulfide white and other zinc salt on the market with zinc sulfate greatly.
Description
The present invention relates to a kind of method of wet zinc smelter, be widely used in the abundant place of zinc ore reserves, especially the development and use of the zinc oxide ore that silicon content is high, thereby the economic worth of raising ore resource, and help reducing the cost of producing zinc sulfide white and other zinc salt with zinc sulfate greatly.
Produce zinc sulfate from metallurgical method, mainly be divided into pyrogenic process, wet method two classes.Present domestic zinc sulfate factory majority utilizes pyrometallurgical smelting, volatilization is collected, the zinc oxide fumes or the secondary zinc oxide that have separated silicate, borrow the acidleach of wet zinc smelter technological principle to become solution of zinc sulfate with purifying, for producing zinc sulfide white, or further with its evaporation concentration, crystallisation by cooling, centrifuge dehydration, to obtain the zinc sulfate finished product.Shortcomings such as pyrogenic process exists needs low silicon ore deposit, zinc recovery is low, energy consumption is high, the ore deposit consumption is big, economic benefit is low.
Chinese yunnan province Jianshui County chemical plant Zhang Xingping and Zhu Zijia have reported " research of zinc oxide ore direct production zinc sulfate ", and they directly leach lead-zinc with sulfuric acid, produce zinc sulfate.Fig. 1 is seen in its Production Flow Chart:
Fig. 1 is that chemical plant, Jianshui County lead-zinc is produced the zinc sulfate synoptic diagram:
Zinc ore by ore grinding (1), screening (2), get 120 purpose breezes, with concentration is that 20% sulfuric acid carries out acidleach (3), leach liquor is discharged slag through filtering (4) back, filtrate input removal of impurity operation (5), in trash separator (5), employing atmospheric oxidation neutralization, and add a certain amount of flocculation agent, gelatine reaches except that F
e, As, Si purifying zinc sulfate purpose.By filtering operation (6), gained filtrate is imported secondary removal of impurities operation (7) to ore deposit liquid after the processing more again, is to remove metallic impurity such as Cu, Cd, Ni with 120 purpose zinc dust precipitations.The treatment solution of gained enters exsiccation (10) at last and just obtains the solid sulphuric acid zinc product by filtering (8), filtrate input thickener (9) evaporation concentration, concentrating once more.
Above processing method only suitablely contains silicon-dioxide in the soluble silicate less than 10% zinc ore, and solution filters does not have difficulty, need not to do special silica removal in the technology and handles, and quality product meets industrial requirements.But if raw ore changes, dioxide-containing silica was greater than 10% o'clock, and the technical process of " building aquation factory " report just can not realize suitability for industrialized production, because siliceous high zinc ore and the material behind the sulfuric acid reaction can produce the gelling phenomenon, cause filtration difficulty, not only influence the leaching amount of zinc, reduce the utilization ratio of zinc ore greatly, and contained insolubles must surpass quality index in the product, even whole material gelling caking when causing zinc ore and sulfuric acid reaction, can't leach, can't filter, can't organize production.Reaction equation as follows:
Positive silicic acid H
4SiO
4Be a kind of almost water-fast binary weak acid, but the positive silicic acid that reaction generates does not precipitate immediately, the unit molecule silicic acid water soluble that begins to form, but the prolongation with the time of increasing along with the molten amount of soaking, and the rising of reaction soln temperature, unit molecule silicic acid carries out polyreaction and generates gelatinous multi-silicate, makes the solution filtration difficulty.
Here it is, and the high zinc oxide ore of silicon content is directly made the where the shoe pinches of zinc sulfate.
Purpose of the present invention, provide a kind of method with manufacturing zinc sulfate from sicica-rich zine oxide, this method is widely used in siliceous zinc oxide ore up to 10-30%, realizes ordinary production, quality product meets domestic standard laid down by the ministries or commissions of the Central Government secondary product, even reaches the first class product specification of quality.
The present invention is achieved in that in conjunction with the accompanying drawings and 2 is described as follows:
Fig. 2 is the present invention's manufacturing zinc sulfate from sicica-rich zine oxide synoptic diagram.
The zinc ore that will contain high silicon at first grinds by ore grinding (11), and the mineral aggregate after grinding is through screening (12), get 80-100 purpose breeze with sulfuric acid by acidleach operation (13), in acidleach (13), the present invention adopts silicon to hinder molten acid leaching process, and its processing condition are as follows:
A, gradation add acid on a small quantity in breeze, add sour 3-4 time/still;
B, low temperature slow reaction: T=40-60 ℃, the best is 45-55 ℃,
T 〉=48 hour/still;
C, sulfuric acid concentration: 30-45%, the best is 30-35%;
D, leach liquor concentration control: PH=4.5-5;
Reduce water consumption in e, the acidleach as far as possible;
F, shortening are leached and filtration time.
Before the acidleach breeze, with the wetting breeze that is soaked of less water, general 250 kg of water/ton breeze.Because zinc oxide and sulfuric acid reaction are thermopositive reaction, in order to make the unlikely rising of dip temperature, adopt gradation to add acid on a small quantity, suitably note stirring, reach the low temperature slow reaction, prevent that unit molecule silicic acid from carrying out the purpose of polyreaction.In the acidleach process, note the pH value of sampling check leach liquor at any time.It is very fast to rise as pH value, and PH in 36 hours 〉=5 o'clock then can add acid in right amount, during PH ≈ 5, illustrates that solution reaction is near terminal point after the reaction times reaches 48 hours.In this operation, can design the relation curve of pH value and leaching time, grasp the change state of pH value at any time.By zinc content * 1.5～1.8 in 100% sulfuric acid consumption=ore deposit.
When PH=4.8-5, carry out vacuum suction filter (14) immediately, with an amount of tap water or the washings of reactor last time, wash slag (15) fast, when the washing lotion ratio weighs 1.18-1.25, immediately washing lotion is incorporated in the filtrate of suction strainer (14), enter silica removal operation (16), in silica removal operation (16), be provided with silica removal still and vacuum filter, when filtrate enters in the silica removal still, intensification is controlled at 90-102 ℃, and constant temperature 2-6 hour, during PH=4.5-5.2, can make silicic acid polymerization become the multi-silicate throw out to separate out, when PH=5.0-5.2, gluing is more complete, for white asbestos wadding condensate is separated out, through vacuum filtration, reach the purpose of basic silica removal again.Contained impurity mainly is F in the raw material
e, A
s, oxide compounds such as Cu, Cd, Ni, also generate vitriol with sulfuric acid reaction, become the impurity in the solution of zinc sulfate, must be purified and be removed.Filtrate enters (17), when filtrate is heated to 80-90 ℃, under whipped state, adds potassium permanganate solution slowly, makes ferrous iron, manganese be oxidized into the filtering of brownish black throw out, at this moment A
SBy ironic hydroxide adsorption precipitation:
The free acid that reaction is separated out can add zinc oxide or milk of lime, and pH value is transferred to 5.1, and after reaction 2 hours, operation (18) is filtered after filtration, and filtrate is sent displacement slot (19), under ℃ condition of T≤50, removes beavy metal impurities such as Cu, Cd, Ni with zinc dust precipitation.Then by filtering (20), filtrate enters enrichment process (21), before the exsiccation operation, the present invention is provided with a silica removal operation (22), in silica removal operation (22), after controlled temperature is 104 ℃, insolubless such as micro-multi-silicate may appear, through disposable centrifugation, separate the refining concentrated solution of back gained water white transparency and just enter exsiccation operation (23) once more, get the solid sulphuric acid zinc product at last.
Products obtained therefrom quality of the present invention is as follows:
Use method of the present invention, can utilize siliceously to be higher than 10%, even produce zinc sulfate up to 30% zinc oxide ore, realize ordinary production, quality product reaches domestic standard laid down by the ministries or commissions of the Central Government secondary standard.The present invention utilizes the universalization construction equipment, less investment, good in economic efficiency, and this will play positive useful effect for development and use that improve ore resource and reduction zinc sulfate cost.
Embodiment:
Be 27% containing zinc, contain SiO
2Be that 16.7% zinc ore powder is got 80-100 order 1000 grams through sieving, gradation adds 35% sulfuric acid 1157 grams, the limit adds sour limit and stirs, controlled temperature≤55 ℃, after treating to add bubble that acid produces at every turn and falling, slowly add second hypo acid again, the entire reaction material is dense thick dark yellow soup compound, and proportion is about 1.72.Stirred 3-4 minute in per 2 hours, react after 24 hours, PH=3-3.5 is when reaction times to 48 hour, then about pH value=4-4.5, when PH=4.5-5.0, add water 2000-2500 milliliter, behind the stirring several minutes, vacuum suction filter gets proportion 1.15-1.18 zinc sulfate coarse filtration liquid 2200-2700 milliliter (control filtrate proportion 〉=1.18 during industrial production), use the cold water washing filter residue more twice or thrice, till final filtrate proportion 1.01-1.02.Merge each time filtrate, heating evaporation to 102 ℃ on electric furnace, separate out white silicic acid throw out, kept constant temperature 2-4 hour, get clear liquid 1-2 and drip, splash into more than 80 ℃ in the distilled water, if any white opacity, illustrate that silica removal not to the greatest extent, should continue constant temperature and make the silicic acid polymerization sedimentation, till not having muddiness to duplicate test, suction strainer while hot.Clear liquid adds 20% potassium permanganate solution 10-30 milliliter in the time of 80-90 ℃, constantly stir, and till being blush and not taking off to reaction solution, then, suction strainer is removed brownish black hydration ferrimanganic arsenic throw out.Filter clear liquid under≤50 ℃ of conditions, add zinc powder 3-5 gram, continuously stirring reaction 5-6 hour, getting the logical hydrogen sulfide of clear liquid, not have muddy variable color qualified for the displacement heavy metal.Clear liquid is concentrated to 104 ℃, separates out as finding the adularescent thing, should be incubated the centrifugation throw out while hot, just obtain refining concentrated solution, after exsiccation makes Zinc Sulphate Heptahydrate 950-1050 gram, quality product can reach domestic standard laid down by the ministries or commissions of the Central Government secondary product.
If system first class product, can carry out secondary the filtrate after zinc dust precipitation is removed Cu, Cd, Ni metallic impurity and add potassium permanganate except that Fe, As, use zinc dust precipitation Cu, Cd, Ni once more, filter back gained refined liquid and send into exsiccation (23) and 40 ℃ of warm air dryings, gained zinc sulfate meets domestic standard laid down by the ministries or commissions of the Central Government first grade standard.
During general ordinary production, raw material consumption quota (in 1 ton of zinc sulfate)
27% zinc oxide ore: 1.0-1.1 ton;
98% sulfuric acid: 0.41-0.43 ton;
99.5% potassium permanganate: 4-6 kilogram;
99.5% zinc powder: 3-5 kilogram.
Claims (4)
1, the method for manufacturing zinc sulfate from sicica-rich zine oxide comprises ore grinding (1), screening (2), acidleach (3), filters in (4), the oxidation and the removal of impurity (5), filter (6), concentrate (7), exsiccation operations such as (8), it is characterized in that:
A, in acidleach (3), adopt silicon to hinder molten acid leaching process, processing condition are as follows:
A, gradation add acid on a small quantity in breeze: add sour 3-4 time/still;
B, low temperature slow reaction: T=40-60 ℃, t 〉=48 hour/still;
C, sulfuric acid concentration: 30-45%;
D, shorten to leach and filter time as far as possible.
The filtrate of B, filtration (4), in entering oxidation and the removal of impurity (5) operation before and exsiccation (8) before, set up the silica removal operation respectively.
2, the method for manufacturing zinc sulfate from sicica-rich zine oxide according to claim 1 is characterized in that, temperature of reaction the best that silicon hinders in the molten acid leaching process is 45-55 ℃, and sulfuric acid concentration the best is 30-35%, reduces water consumption in the acidleach process as far as possible.
3, the method for manufacturing zinc sulfate from sicica-rich zine oxide according to claim 1, it is characterized in that, in oxidation and removal of impurities operation (5) before, be provided with the silica removal operation, the silica removal operation is to be about 1.2 zinc sulfate clear liquid with proportion, in the input silica removal still, and is heated to 90-102 ℃, time 2-6 hour, enter vacuum filter behind the PH=4.5-5.2 of control solution and filter.
4, the method for manufacturing zinc sulfate from sicica-rich zine oxide according to claim 1, it is characterized in that being provided with the silica removal operation before in exsiccation operation (8), the silica removal operation is after the heating of the solution of zinc sulfate after the removal of impurity is concentrated to 104 ℃, to carry out disposable centrifugation again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN87102024A CN1006634B (en) | 1987-05-16 | 1987-05-16 | Process for manufacturing zinc sulfate from sicica-rich zine oxide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN87102024A CN1006634B (en) | 1987-05-16 | 1987-05-16 | Process for manufacturing zinc sulfate from sicica-rich zine oxide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1030794A true CN1030794A (en) | 1989-02-01 |
| CN1006634B CN1006634B (en) | 1990-01-31 |
Family
ID=4813734
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN87102024A Expired CN1006634B (en) | 1987-05-16 | 1987-05-16 | Process for manufacturing zinc sulfate from sicica-rich zine oxide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1006634B (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106337129A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Willemite leaching method |
| CN106337122A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Copper orthosilicate leaching method |
| CN106337128A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Copper orthosilicate leaching method |
| CN106337127A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Garnierite leaching method |
| CN106337121A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Garnierite leaching method |
| CN106337126A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Garnierite leaching method |
| CN106337124A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Copper orthosilicate leaching method |
| CN106337125A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Willemite leaching method |
| 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 |
| CN112578077A (en) * | 2020-11-11 | 2021-03-30 | 韶关凯鸿纳米材料有限公司 | Zinc recovery method for silicon dioxide detection |
-
1987
- 1987-05-16 CN CN87102024A patent/CN1006634B/en not_active Expired
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106337129A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Willemite leaching method |
| CN106337122A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Copper orthosilicate leaching method |
| CN106337128A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Copper orthosilicate leaching method |
| CN106337127A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Garnierite leaching method |
| CN106337121A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Garnierite leaching method |
| CN106337126A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Garnierite leaching method |
| CN106337124A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Copper orthosilicate leaching method |
| CN106337125A (en) * | 2016-08-09 | 2017-01-18 | 四川师范大学 | Willemite leaching method |
| 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 |
| CN112578077A (en) * | 2020-11-11 | 2021-03-30 | 韶关凯鸿纳米材料有限公司 | Zinc recovery method for silicon dioxide detection |
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| Publication number | Publication date |
|---|---|
| CN1006634B (en) | 1990-01-31 |
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