CN88102610A - From smithsonite oxygenerating zinc technology - Google Patents
From smithsonite oxygenerating zinc technology Download PDFInfo
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- CN88102610A CN88102610A CN88102610.7A CN88102610A CN88102610A CN 88102610 A CN88102610 A CN 88102610A CN 88102610 A CN88102610 A CN 88102610A CN 88102610 A CN88102610 A CN 88102610A
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- zinc
- smithsonite
- zinc oxide
- leaching
- ammonia
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Abstract
A kind of ammonia-ammonium method is directly produced the zinc oxide technology from smithsonite, through leaching, after removal of impurities, pyrolysis, four technical process of calcining, the quality of zinc oxide is greater than 99.7%, and the total recovery of zinc has raw materials and fuel and consumes low greater than 80%, the advantage that factory cost is low and technical process is short, the employing construction equipment that routinizes then has plant investment few, and is easy to control and produce stable characteristics.
Description
The present invention relates to a kind of chemical industry technology, be applicable to and produce inorganic chemical industry zinc salt-zinc oxide product.
Zinc oxide is a kind of broad-spectrum inorganic chemical product, and along with industrial expansion, every profession and trade increases year by year to the demand of zinc oxide.The method of producing zinc oxide at present is more, mainly contains the zinc ingot metal method, tutty method and zinc salt decomposition method, these methods can be produced high-purity zinc oxide, but all be with zinc ingot metal and tutty as raw material, consume a large amount of zinc ingot metals, then the cost height can not satisfy the demand of country.The processing method of zinc oxide is produced in russian patent 1178786 propositions from tutty with ammonia azanium method in the eighties, but this processing method is produced zinc oxide and is also had (1), cost height, (2), ore increases energy consumption through 800 ℃ of left and right sides high-temperature calcinations, and contains C in the tutty after calcining
The oxide compound of O and other solubilities causes the impurity removal process complexity.(3), leaching agent NH
3: CO
2Ratio low, cause carbon ammonium consumption big, therefore, seek new resource and complete processing and be development zinc salt product, particularly zinc oxide product, be a problem that presses for solution at present.
The purpose of this invention is to provide a kind of with ammonia azanium method directly from smithsonite＜without calcining produce the technology method of zinc oxide.
Processing method of the present invention be with the smithsonite powder through leaching, removal of impurities, pyrolysis, four flow processs of calcining, its principle is:
1, leaching
Zinc mainly exists with the zinc carbonate form in the smithsonite, leaches with ammonia-ammonium mixing solutions through levigated smithsonite material.Its reaction formula is as follows:
Zinc and various associated metal form the ammonium complex ion or the ammonia complex of high ligancy, also enter solution thereupon, and its reaction formula is as follows:
The general formula of metal ammonium complex ion is:
Me（NH
3）
m n
The m value can be by 1 to 6 in the formula, but with 2～4 the most common, temperature is bigger to the influence of m value under the identical situation of other condition, and elevated temperature will make the quantity of low m value complex ion increase the then corresponding minimizing of high m value.The ammonia concentration that increases solution will obtain opposite result.In order to obtain stable high m value complex ion, must guarantee that solution has enough ammonia concentration, guarantee the ratio NH of amino molecule and atoms metal to be leached
3/ Me is more than a certain numerical value.Therefore select suitable value for use, make zinc become stable Zn(NH
3)
2 4Complex compound enters solution.
2, purify:
Zinc enters the leaching liquid of solution, need carry out purifying treatment, can obtain purified zinc solution, its reaction:
3, pyrolysis
Solution after purifying treatment, heating pyrolyze are that its reaction of zinc subcarbonate is as follows:
4, calcining
After filtration, the zinc subcarbonate after the washing, calcining at high temperature makes zinc oxide product.Its reaction is as follows:
From the technical process of smithsonite oxygenerating zinc is (figure one):
Smithsonite is after single toggle jaw crusher (1) carries out fragmentation, and is levigate less than 80 orders with XWI43 type selection by winnowing beater grinder (2), delivers to material collecting tank (3) with wind, when leaching groove (4) is put in the breeze metering, adds ammonia-ammonium solution, this solution NH
3: CO
2Ratio is greater than 19.6, and optimum ratio is 26.1, liquid: Gu=3.5～4.5, optimum ratio is 4, and 250 rev/mins of stirring velocitys stirred leaching time after 2～3 hours, deliver to flame filter press (6) with pump (5) and filter, filter residue discards.Filter pump (7) is delivered to deblending slot (8) and carries out removal of impurities, by 3～5 times of total impurities, the best is 4.4 extraordinarily to go into the sulfide cleaner, stir and left standstill in 1～2 hour 4～6 hours, the clear liquid filtering-depositing that comes down in torrents, delivering to pressure filter (6) through pump (9) again filters ， And and the removal of impurities slag is reclaimed is used to extract useful element.Filtrate is delivered to pyrolysis groove (10) and is carried out thermal degradation (80～100 ℃ of Heating temperatures), and zinc content is about 1 grams per liter in the control pyrolysis mother liquor, and ammonia is introduced ammonia accumulator tank (11) water and absorbed, and its temperature is controlled at below 35 ℃.Returning leaching groove (4) through pump (12) then recycles.Precipitation and mother liquor are put into link-suspended basket centrifuge (13) and are filtered, and mother liquor inflow mother liquor tank (14) is delivered to ammonia accumulator tank (11) with pump (16) and recycled.Filter cake is delivered to rotary kiln (15), and 800～820 ℃ of controlled temperature, charging capacity 12～15Kg/ hour, material was sintered into zinc oxide product 80～90 minutes high-temperature zone residence time under the condition that widely different converter rotating speed is 1.2～1.5 rev/mins.
Effect of the present invention is: adopt ammonia azanium method directly to produce zinc oxide product from smithsonite, in control condition: leaching NH
3: CO
2Ratio is greater than 19.6, liquid: Gu=4, granularity is less than or equal to 100 orders, 25～40 ℃ of temperature, extraction time was not less than 2.5 hours, extraordinarily went into the sulfide cleaner by 4.4 of total impurities, and impurities removing efficiency reaches 100%, pyrolysis temperature is at 80～100 ℃, ammonia absorption liquid temperature is lower than 35 ℃, and calcining temperature is at 800～820 ℃, under 80～90 minutes the construction equipment that routinizes of residence time of material, obtain the zinc oxide quality and reach more than 99.7%, the total recovery of zinc is greater than 80%.Technical process is short, and is easy to operate, easy to control, produces and stablizes, and adopts the construction equipment that routinizes to realize that easily suitability for industrialized production ， And uses equipment few, reduced investment.Domestic have an abundant zinc resource, compares with zinc ingot metal, and starting material are inexpensive, and raw material can leach at normal temperatures without calcining, and the energy of consumption is little.In process of production can recycling use ammonia and pyrolysis mother liquor, there is not the waste liquid exhaust gas emission substantially, have the value that develop and spread is used.
Figure one produces the zinc oxide process flow sheet from smithsonite.
Embodiments of the invention are to adopt Hanyuan, Sichuan smithsonite, and zinc content 38.26～41.61% contains 28% with industrial ammonium water, proportion 0.895, and agricultural ammonium hydrogencarbonate and sulfide cleaner are raw material.
Drop into smithsonite raw material 1010Kg, containing zinc and be 38.26% is the heavy 386.426Kg of zinc.
1, leaching: in condition, leaching HN
3: CO
2=26.1, liquid: Gu=250 rev/mins of 4 stirring velocitys, stir leaching time and must soak the heavy 174.7Kg of slag after 2.5 hours, by containing zinc 7.88%, pay zinc 13.77Kg.
2, the removal of impurity: in condition, the sulfide cleaner of preparation is extraordinarily gone into deblending slot by 4.4 of total impurities, and impurities removing efficiency reaches 100% and gets the heavy 20.12Kg of the removal of impurity, by zinc content 37.34%, pays zinc 7.51Kg.
3, pyrolysis: in condition, 80～100 ℃ of pyrolysis temperatures obtain the heavy 590.88Kg of zinc subcarbonate, and by containing zinc 57.35%, zinc is 338.87Kg, and mother liquor adds always pays zinc 5.12Kg in the washing water.
4, calcining: in condition, calcining temperature is at 800～820 ℃, residence time of material 80～90 minutes, the heavy 382.27Kg of zinc oxide, by zinc content 80.26% then the zinc amount be 306.81Kg.The total recovery of zinc is 79.4%.
Claims (4)
1, a kind ofly produces the zinc oxide technology, produce the zinc oxide technology by ammoniacal liquor-ammonium bicarbonate method and form, it is characterized in that in the leaching groove, the smithsonite powder being added ammonia-ammonium solution, NH from smithsonite
3: CO
2Greater than 19.6; In deblending slot, add cleaner, with after whizzer separates, obtain zinc subcarbonate, in the widely different converter of 800～820 ℃ of controlled temperature, be sintered into the technology of zinc oxide product through the pyrolysis groove.
2, technology according to claim 1 is characterized in that smithsonite pulverized by crusher and pulverizer, obtains granularity less than 80 purpose smithsonite powder.
3, technology according to claim 1 is characterized in that in leaching process, adds liquid in the leaching groove: Gu=3.5～4.5 times, the best is 4 times, wherein ammonia-ammonium solution, i.e. NH
3: CO
2Optimum ratio be 26.1, stirred leaching time 2～3 hours.
4, technology according to claim 1 is characterized in that the temperature in the heating tank is controlled at 80～100 ℃, and ammonia absorption liquid temperature is lower than 35 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88102610 CN1009359B (en) | 1988-04-30 | 1988-04-30 | Production technology of zink oxide from smithosonite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88102610 CN1009359B (en) | 1988-04-30 | 1988-04-30 | Production technology of zink oxide from smithosonite |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN88102610A true CN88102610A (en) | 1988-12-28 |
| CN1009359B CN1009359B (en) | 1990-08-29 |
Family
ID=4832225
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 88102610 Expired CN1009359B (en) | 1988-04-30 | 1988-04-30 | Production technology of zink oxide from smithosonite |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1009359B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106431387A (en) * | 2016-07-29 | 2017-02-22 | 柳州豪祥特科技有限公司 | Technology for preparing AZO target |
| CN110205489A (en) * | 2018-07-24 | 2019-09-06 | 重庆东群科技有限公司 | A method of it is handled with zincic acid barium route of synthesis containing zinc ore crude |
| WO2020019777A1 (en) * | 2018-07-24 | 2020-01-30 | 重庆东群科技有限公司 | Method for producing zinc-containing complex or zinc oxide using zinc-containing raw ore via intermediate step for synthesis of calcium zincate |
| WO2020019834A1 (en) * | 2018-07-24 | 2020-01-30 | 重庆东群科技有限公司 | Mineral processing method for low-grade zinc-containing raw ore |
| WO2020019854A1 (en) * | 2018-07-24 | 2020-01-30 | 重庆东群科技有限公司 | Method for producing zinc oxide by means of double leaching |
-
1988
- 1988-04-30 CN CN 88102610 patent/CN1009359B/en not_active Expired
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106431387A (en) * | 2016-07-29 | 2017-02-22 | 柳州豪祥特科技有限公司 | Technology for preparing AZO target |
| CN110205489A (en) * | 2018-07-24 | 2019-09-06 | 重庆东群科技有限公司 | A method of it is handled with zincic acid barium route of synthesis containing zinc ore crude |
| WO2020019777A1 (en) * | 2018-07-24 | 2020-01-30 | 重庆东群科技有限公司 | Method for producing zinc-containing complex or zinc oxide using zinc-containing raw ore via intermediate step for synthesis of calcium zincate |
| WO2020019834A1 (en) * | 2018-07-24 | 2020-01-30 | 重庆东群科技有限公司 | Mineral processing method for low-grade zinc-containing raw ore |
| WO2020019854A1 (en) * | 2018-07-24 | 2020-01-30 | 重庆东群科技有限公司 | Method for producing zinc oxide by means of double leaching |
| CN110896643A (en) * | 2018-07-24 | 2020-03-20 | 重庆东群科技有限公司 | Method for producing zinc-containing compound or zinc oxide from zinc-containing raw ore through intermediate step of calcium zincate synthesis |
| CN110972479A (en) * | 2018-07-24 | 2020-04-07 | 重庆东群科技有限公司 | Method for producing zinc oxide by twice leaching method |
| CN110205489B (en) * | 2018-07-24 | 2020-12-11 | 重庆东群科技有限公司 | Method for treating zinc-containing raw ore by barium zincate synthesis way |
| CN110972479B (en) * | 2018-07-24 | 2022-05-06 | 重庆东群科技有限公司 | Method for producing zinc oxide by twice leaching method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1009359B (en) | 1990-08-29 |
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