CN108559841B - Method for preparing tungsten product by acid decomposition of scheelite and scheelite mixed ore - Google Patents

Method for preparing tungsten product by acid decomposition of scheelite and scheelite mixed ore Download PDF

Info

Publication number
CN108559841B
CN108559841B CN201810360985.7A CN201810360985A CN108559841B CN 108559841 B CN108559841 B CN 108559841B CN 201810360985 A CN201810360985 A CN 201810360985A CN 108559841 B CN108559841 B CN 108559841B
Authority
CN
China
Prior art keywords
tungsten
acid
hydrogen peroxide
tungstic acid
reaction
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.)
Active
Application number
CN201810360985.7A
Other languages
Chinese (zh)
Other versions
CN108559841A (en
Inventor
陈星宇
赵中伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Central South University
Original Assignee
Central South University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Central South University filed Critical Central South University
Priority to CN201810360985.7A priority Critical patent/CN108559841B/en
Publication of CN108559841A publication Critical patent/CN108559841A/en
Application granted granted Critical
Publication of CN108559841B publication Critical patent/CN108559841B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/04—Extraction of metal compounds from ores or concentrates by wet processes by leaching
    • C22B3/06—Extraction of metal compounds from ores or concentrates by wet processes by leaching in inorganic acid solutions, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions
    • C22B3/08—Sulfuric acid, other sulfurated acids or salts thereof
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/04—Extraction of metal compounds from ores or concentrates by wet processes by leaching
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/44—Treatment or purification of solutions, e.g. obtained by leaching by chemical processes
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B34/00—Obtaining refractory metals
    • C22B34/30—Obtaining chromium, molybdenum or tungsten
    • C22B34/36—Obtaining tungsten
    • 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 invention relates to a method for preparing tungsten products by acid decomposition of mixed black-white tungsten ores, which takes the mixed black-white tungsten ores as raw materials and comprises the following steps: (1) leaching reaction; (2) filtering and washing; (3) extracting and decomposing hydrogen peroxide to extract tungsten; (4) dissolving and decomposing hydrogen peroxide for multiple times to purify tungstic acid; (5) calcining pure tungstic acid to prepare tungsten trioxide; (6) and (3) preparing tungsten oxide and tungsten powder by spray pyrolysis of a peroxytungstic acid solution. The method only consumes cheap and easily-obtained sulfuric acid, thereby greatly reducing the decomposition cost of the black-white tungsten mixed ore; the decomposition slag is gypsum which can be used as building materials, no hazardous waste alkali cooking slag is generated, and the production and operation cost of enterprises is greatly reduced; hydrogen peroxide is used as an extractant of tungstic acid, ammonia nitrogen wastewater is not generated, a process for generating ammonia nitrogen wastewater for years in tungsten smelting is eliminated, and the environmental protection cost is greatly reduced; directly produce various tungsten end products and tungsten powder, and improve the added value of products of tungsten smelting enterprises.

Description

Method for preparing tungsten product by acid decomposition of scheelite and scheelite mixed ore
Technical Field
The invention relates to the field of chemical production, in particular to a method for preparing a tungsten product by acid decomposition of a black-white tungsten mixed ore.
Background
At present, the mainstream technology for industrially treating the mixed ore of the black tungsten and the white tungsten is to firstly use sodium hydroxide to carry out pressure boiling to obtain a crude sodium tungstate solution and alkaline boiling slag. The crude sodium tungstate solution is diluted by adding a large amount of water and then converted into an ammonium tungstate solution by an ion exchange technology, and the ammonium tungstate solution is also converted by adopting a solvent extraction method. This mainstream technology currently faces several serious problems: firstly, alkali such as sodium hydroxide or sodium carbonate is consumed for alkali pressure cooking, the price of the reagents is high at present, particularly the price of the sodium hydroxide reaches 5000-6000 yuan/ton, and therefore the decomposition cost of the tungsten black and white mixed ore is high; secondly, alkaline pressure boiling generates alkaline boiling slag which is listed as a national hazardous waste catalogue at present, tungsten smelting enterprises cannot process the alkaline boiling slag randomly and must give the alkaline boiling slag to qualified enterprises for paid processing, and the country also collects 2000 yuan/ton of environment-friendly tax on the generated dangerous alkaline boiling slag, so that the cost of tungsten smelting is greatly increased; thirdly, in order to produce tungsten products with qualified impurity content, ammonia reagents such as ammonia water or ammonium chloride and the like are also required to be used as transformation reagents in the existing tungsten smelting process, so that a large amount of ammonia nitrogen wastewater is inevitably generated in the production process, and the environment is polluted. In order to solve the economic and environmental problems faced by the current tungsten smelting, a new tungsten smelting technology needs to be developed urgently.
In order to reduce the decomposition cost of tungsten ore and not to adopt an alkaline reagent to decompose the mixed black-white tungsten ore without generating dangerous waste alkali cooking slag, only an acidic reagent is adopted to decompose the tungsten ore. In fact, hydrochloric acid and nitric acid are used for decomposing black-white tungsten mixed ore for a long time, but the decomposition effect is limited; the bin and the like adopt sulfuric acid to decompose the mixed black-white tungsten ore, and the mixed black-white tungsten ore can be mostly decomposed under optimized experimental conditions. Tungsten ore is converted into tungstic acid after acid decomposition. In order to prepare a qualified tungsten product, the tungstic acid generated by conversion is usually dissolved by ammonia water to obtain an ammonium tungstate solution, and ammonium carbonate is also used for dissolving the tungstic acid to obtain the ammonium tungstate solution. When the acid decomposition residue is subjected to ammonia or ammonium carbonate dissolution washing, ammonia-nitrogen-containing wastewater is inevitably generated. Ammonium tungstate obtained by dissolution is dissolved and then is evaporated and crystallized to prepare APT, a large amount of ammonia-containing steam is generated in the process, and a special device is needed for absorbing ammonia gas. Some enterprises adopt hydrochloric acid to absorb ammonia gas and then merge the ammonia gas into the wastewater to form high-concentration ammonia nitrogen wastewater. The crystallization mother liquor is a saturated ammonium tungstate solution, and ammonia nitrogen wastewater can be generated when tungsten is treated and recovered. At present, the environmental protection is extremely strict to the discharge control of the ammonia nitrogen wastewater in tungsten smelting, the discharge of the ammonia nitrogen wastewater reaching the standard is required, the input of ammonia nitrogen wastewater treatment is required to be increased, and the production cost of enterprises is inevitably increased. In addition, in order to produce the subsequent tungsten product (tungsten oxide), tungsten powder or tungsten carbide, the initial product APT of tungsten must be subjected to a calcination process. And a large amount of ammonia-containing waste gas is generated in the calcining process, the air can be directly polluted without treatment, and the ammonia-containing waste gas can be discharged after being absorbed by a special device and subjected to harmless treatment. Therefore, the existing tungsten smelting process cannot avoid the generation of ammonia nitrogen, so that the ammonia nitrogen pollution is inevitably caused to a certain extent.
In the traditional tungsten smelting process based on the acid method, ammonia is introduced to facilitate the separation of tungstic acid from other impurities. The ammonia water or ammonium carbonate is a weak base, so that other impurities are difficult to dissolve while the tungstic acid is dissolved, and the selective dissolution of the tungstic acid is facilitated. Since ammonia causes ammonia nitrogen pollution and cannot be used, there is a method for selectively dissolving tungstic acid without other reagents? Research has long shown that hydrogen peroxide has strong complexing ability to tungsten, so that some people add a certain amount of hydrogen peroxide to form soluble peroxytungstic acid in the process of acid decomposition of tungsten ore, thereby avoiding the influence of tungstic acid coating formed in the decomposition process on the acid decomposition of tungsten black and white mixed ore. Patent document CN105200246A describes that a mixed solution of sodium tungstate and sodium molybdate can be dissolved and acid-decomposed with hydrogen peroxide to obtain a mixed acid of tungstic acid and molybdic acid. The tungstic acid and molybdic acid dissolved by the hydrogen peroxide are relatively pure, only contain sodium ions which are not easy to wash, and have no other impurities, so the hydrogen peroxide is relatively easy to dissolve. The invention mainly aims to separate tungsten and molybdenum according to the stability difference of peroxytungstic acid and peroxymolybdic acid in an acid solution, and a tungsten purification method is not involved.
The Fengguan and the like are prepared by adding a certain amount of hydrogen peroxide into a sodium tungstate solution, regulating the acidity of the solution, and then decomposing peroxytungstate radicals, and then preparing tungstic acid, Guo-jin and the like are prepared by mixing tungstic acid and hydrogen peroxide into a precursor solution with the concentration of only 0.005 mol/L, and then the precursor solution is sprayed onto an ITO glass substrate at 250 ℃ through ultrasonic spray pyrolysis to obtain a tungstic acid film firstly, and then the tungstic acid film can be obtained through subsequent heat treatment at 550 ℃, and the essence of the process is a method for preparing the tungstic acid film through spray pyrolysis.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provides a method for preparing a tungsten product by acid decomposition of a scheelite and scheelite mixed ore.
Specifically, the flow diagram of the method for preparing tungsten products by acid decomposition of scheelite and scheelite mixed ore provided by the invention can be referred to as fig. 1.
The method comprises the following steps:
(1) leaching reaction: adding the mixed ore of the black and white tungsten into a sulfuric acid solution for leaching reaction;
(2) filtering and washing: filtering the reaction product obtained in the step (1) to obtain decomposition slag and leachate; supplementing sulfuric acid into the leachate, and returning to the step (1) to be used as a raw material for leaching reaction;
(3) hydrogen peroxide extraction-decomposition extraction of tungsten: washing the decomposition residue obtained in the step (2), mixing the decomposition residue with a hydrogen peroxide solution to perform tungsten extraction reaction, and filtering a reaction product to obtain a peroxytungstic acid solution and gypsum; heating the peroxytungstic acid solution or introducing SO2Until the peroxytungstic acid is completely decomposed to separate out tungstic acid;
(4) extracting hydrogen peroxide for multiple times, decomposing and purifying tungstic acid: detecting the impurity content in the tungstic acid obtained in the step (3), directly using the tungstic acid in the subsequent step if the impurity content meets the standard requirement, adding a hydrogen peroxide solution and repeating the operation of the step (3) at least once if the impurity content exceeds the standard requirement until the tungstic acid with the impurity content meeting the standard requirement is obtained;
treating the tungstic acid with the impurity content meeting the standard requirement by adopting the following steps (5) or steps (6) to (7):
(5) calcining pure tungstic acid to prepare tungsten trioxide: calcining tungstic acid with impurity content meeting the standard requirement to obtain powdery tungsten trioxide;
(6) spray pyrolysis of a peroxytungstic acid solution to prepare tungsten oxide and tungsten powder: dissolving impurities in accordance with a standard to perform tungsten extraction reaction to obtain a pure peroxytungstic acid solution;
(7) carrying out ultrasonic spray pyrolysis on the pure peroxytungstic acid solution under a non-reducing condition to obtain superfine spherical tungsten trioxide; and/or carrying out ultrasonic spray pyrolysis on the pure peroxytungstic acid solution under a reducing condition to obtain superfine spherical blue tungsten oxide, purple tungsten oxide and/or tungsten powder.
The raw material of the mixed black-white tungsten ore has the grade of 10-65% and the granularity of less than 300 mu m.
In the leaching reaction in the step (1), the concentration of the sulfuric acid solution is 50-500 g/L. During the reaction, a certain amount of solid tungstic acid can be added, and a certain amount of CaSO can be added4As seed crystals, the solid tungstic acid and CaSO4The addition amount of the tungsten oxide is 0-20% of the mass of the tungsten oxide and tungsten oxide mixed ore; during the reaction, a certain amount of oxidant may be added to promote the reaction, such as oxygen, nitric acid, hydrogen peroxide, sodium hypochlorite, etc. The liquid-solid ratio of the reaction in the step is preferably 3: 1-10: 1. As a preferable scheme, the reaction in the step (1) can be carried out at 50-250 ℃ and 0-10 Mpa, and the reaction time is preferably 1-6 hours.
In the filtration washing in the step (2) of the present invention: adding a certain amount of acid into the leachate to make the concentration of the acid liquor the same as that of the acid adopted in the step (1), and then returning to the step (1) to be used as a raw material for leaching reaction.
In the step (3) of extracting and decomposing the tungsten by using the hydrogen peroxide, the method comprises the following steps: the mass concentration of the hydrogen peroxide solution is 5-30%; the preferred molar ratio of the added amount of the hydrogen peroxide to the tungstic acid in the decomposition residue is 0.5-2: 1. As a preferable scheme, the extraction reaction is carried out for 10min to 2.0h at the temperature of 10 to 40 ℃. After the extraction reaction is finished, filtering the product to obtain a peroxytungstic acid solution and calcium sulfate slag (namely gypsum). Then heating the peroxytungstic acid solution to 50-90 ℃, or directly introducing SO into the peroxytungstic acid solution2And controlling the concentration of sulfuric acid in the solution to be 0.1 mol/L-2.0 mol/L until the peroxytungstic acid is completely decomposed, and then the tungstic acid can be separated out.
The operation of dissolving and decomposing the hydrogen peroxide for multiple times to purify the tungstic acid in the step (4) of the invention can be seen in different repetition times of the raw materials. When the grade of the black-white tungsten mixed ore is high, the impurity content in the tungstic acid crystal obtained in the step (3) can directly meet the standard requirement, and the tungstic acid is directly used in the subsequent step, so that the purification process can be directly omitted; and (3) when the grade of the black-white tungsten mixed ore is low, if the content of impurities in the tungstic acid obtained in the step (3) exceeds the standard requirement, adding a hydrogen peroxide solution into the tungstic acid, repeating the step (3) at least once, namely purifying by using hydrogen peroxide until the tungstic acid with the content of impurities meeting the standard requirement is obtained. According to the invention, after the impurity content in the tungstic acid is controlled in the step (4), the subsequent steps are carried out for calcination or pyrolysis, so that the final product has good yield and purity, the energy is saved, and the equipment is protected.
The standard of the impurity content can be manually made according to industrial production specifications or actual requirements of products, and the invention is not particularly limited.
As a preferable scheme of the invention, when the content of impurity elements in the obtained tungstic acid meets the national standard GB/T10116-2007, the tungstic acid can be qualified.
The qualified tungstic acid prepared by the steps has two optional modes for preparing the tungsten oxide product. Wherein, in the first mode, as described in the step (5), the tungsten trioxide is directly obtained by calcination; in the second mode, tungsten oxide and tungsten powder are prepared by spray pyrolysis as described in steps (6) to (7).
In the preparation of tungsten trioxide by calcining pure tungstic acid in the step (5) of the invention: the calcining temperature is 750-900 ℃. In the step, tungstic acid with impurity content meeting the standard requirement is calcined to prepare the powdery tungsten trioxide.
In the preparation of tungsten oxide and tungsten powder by spray pyrolysis of the peroxytungstic acid solution in the step (6) of the invention: adding the tungstic acid with the impurity content meeting the standard requirement into the hydrogen peroxide solution again (the mass concentration is 5-30%), and reacting to obtain the pure peroxytungstic acid solution (wherein WO)3The concentration is about 10 to 350 g/L).
In the step (7), the pure peroxytungstic acid solution is subjected to ultrasonic spray pyrolysis to obtain a superfine spherical product. Specifically, the ultrasonic spray pyrolysis can be carried out under non-reducing conditions to obtain ultrafine spherical tungsten trioxide; or under the reducing condition to obtain the superfine spherical blue tungsten oxide, or purple tungsten oxide, or tungsten powder.
In practical operation, inert gas (such as nitrogen or argon) can be introduced during ultrasonic spray pyrolysis, and the purpose of introducing the inert gas is to carry the inert gas into the solution for pyrolysis, as a preferable scheme, the spraying speed is 10-200 ml/min, the gas flow rate is 150-600 ml/L, the pyrolysis temperature is 500-900 ℃, and the superfine spherical tungsten trioxide powder can be obtained.
In practical operation, reducing gas (such as hydrogen) can be introduced during ultrasonic spray pyrolysis, so that pyrolysis is carried out under the reducing condition, as a preferred scheme, the spraying rate is 10-200 ml/min, the hydrogen flow rate is 50-600 ml/L, the pyrolysis temperature is 500-900 ℃, and ultrafine spherical purple tungsten oxide powder or ultrafine spherical blue oxide powder can be obtained.
The invention provides a brand-new method for preparing tungsten products by decomposing black-white tungsten mixed ores with acid, which has the following main advantages:
firstly, the cheap and easily-obtained decomposition reagent sulfuric acid is adopted, the price is 200-500 yuan/ton, and is only 10% of the cost of the sodium hydroxide reagent, so that the tungsten ore decomposition cost is greatly reduced;
secondly, the black-white tungsten mixed ore is decomposed by sulfuric acid, the decomposition slag is gypsum and can be used as a building material, no dangerous waste alkali cooking slag is generated, and the production and operation cost of an enterprise is greatly reduced;
thirdly, hydrogen peroxide is used as an extractant of the tungstic acid, ammonia nitrogen wastewater is not generated, the process of continuously generating ammonia nitrogen wastewater for many years in tungsten smelting is eliminated, and the environmental protection cost is greatly reduced;
fourthly, the invention directly produces various tungsten end products (tungsten oxide and tungsten powder), and improves the added value of products of tungsten smelting enterprises.
Drawings
FIG. 1 is a flow chart of the method of the present invention; in the drawings, the dashed arrows and the dashed boxes represent alternative parallel process routes.
Detailed Description
The following examples are intended to illustrate the invention but are not intended to limit the scope of the invention.
Example 1
The embodiment provides a method for preparing a tungsten product by acid decomposition of a mixed ore of black and white tungsten, which adopts raw materials of the mixed ore of black and white tungsten with the grade of 40% and the granularity of 120 μm, and specifically comprises the following steps:
(1) leaching reaction, namely adding the black-white tungsten mixed ore into a sulfuric acid solution with the concentration of 200 g/L, wherein the liquid-solid ratio of the system is 6:1, and performing leaching reaction for 3 hours at the temperature of 150 ℃ and under the pressure of 0.5Mpa to convert 99.2 percent of tungsten into tungstic acid;
(2) filtering and washing: filtering the reaction product obtained in the step (1) to obtain decomposition slag and leachate; supplementing sulfuric acid into the leachate, and returning to the step (1) to be used as a raw material for leaching reaction;
(3) hydrogen peroxide extraction-decomposition extraction of tungsten: washing the decomposition residue obtained in the step (2), mixing the decomposition residue with a hydrogen peroxide solution with the mass concentration of 20%, wherein the molar ratio of the added hydrogen peroxide to tungstic acid in the decomposition residue is 1.5:1, carrying out tungsten extraction reaction for 1h at the temperature of 25 ℃, and filtering the reaction product to obtain a peroxytungstic acid solution and gypsum; heating the peroxytungstic acid solution to 80 ℃ until the peroxytungstic acid is completely decomposed to separate out tungstic acid; through detection, the content of impurity elements in the obtained tungstic acid meets the national standard GB/T10116-;
(4) washing the tungstic acid obtained in the step (3), and mixing the tungstic acid with a hydrogen peroxide solution with the mass concentration of 30% at the temperature of 25 ℃ for reaction for 1h to obtain a pure peroxytungstic acid solution again;
(5) and (3) carrying out ultrasonic spray pyrolysis on the pure peroxytungstic acid solution obtained in the step (4) under the conditions of introducing nitrogen, spraying speed of 120ml/min, nitrogen flow rate of 400 ml/L and pyrolysis temperature of 700 ℃ to obtain ultrafine spherical tungsten trioxide powder, wherein the content of impurities in the tungsten trioxide is detected to meet the requirements of national standard GB/T3457-grade 2013 (0-grade product).
Example 2
The embodiment provides a method for preparing a tungsten product by acid decomposition of a mixed ore of black and white tungsten, which adopts raw materials of the mixed ore of black and white tungsten with the grade of 52% and the granularity of 50 μm, and specifically comprises the following steps:
(1) leaching reaction, namely adding the black-white tungsten mixed ore into a sulfuric acid solution with the concentration of 400 g/L, adding calcium sulfate accounting for 5% of the mass of the black-white tungsten mixed ore, wherein the liquid-solid ratio of the system is 10:1, and performing leaching reaction for 1 hour at the temperature of 200 ℃ and the pressure of 1.85MPa to convert 99.3% of tungsten into tungstic acid;
(2) filtering and washing: filtering the reaction product obtained in the step (1) to obtain decomposition slag and leachate; supplementing sulfuric acid into the leachate, and returning to the step (1) to be used as a raw material for leaching reaction;
(3) hydrogen peroxide extraction-decomposition extraction of tungsten: washing the decomposition residue obtained in the step (2), mixing the decomposition residue with a hydrogen peroxide solution with the mass concentration of 30%, wherein the molar ratio of the added hydrogen peroxide to tungstic acid in the decomposition residue is 1:1, carrying out tungsten extraction reaction for 10min at the temperature of 40 ℃, and filtering the reaction product to obtain a tungstic acid peroxide solution and gypsum; directly introducing SO into peroxytungstic acid solution2Controlling the concentration of sulfuric acid in the solution to be 1.5 mol/L until the peroxytungstic acid is completely decomposed to separate out tungstic acid;
(4) dissolving hydrogen peroxide for multiple times, decomposing and purifying tungstic acid: adding a hydrogen peroxide solution with the mass concentration of 30% into the tungstic acid obtained in the step (3), and repeating the operation of the step (3) once to obtain the tungstic acid with the impurity content meeting the standard requirement; when the content of impurity elements in the obtained tungstic acid meets the national standard GB/T10116-;
(5) washing the tungstic acid obtained in the step (4), mixing the tungstic acid with a hydrogen peroxide solution with the mass concentration of 25% for reaction for 1h at the temperature of 30 ℃ to obtain a pure peroxytungstic acid solution again, and (6) carrying out ultrasonic spray pyrolysis on the pure peroxytungstic acid solution obtained in the step (5) under the conditions of introducing hydrogen, the spray rate of 120ml/min, the hydrogen flow rate of 350 ml/L and the pyrolysis temperature of 500 ℃ to obtain superfine spherical blue tungsten oxide powder, wherein the content of impurities in the blue tungsten trioxide meets the requirements of national standard GB/T3457-2013 (0-grade product) through detection.
Example 3
The embodiment provides a method for preparing a tungsten product by acid decomposition of a mixed ore of black and white tungsten, which adopts raw materials of the mixed ore of black and white tungsten with the grade of 55% and the granularity of 100 mu m, and specifically comprises the following steps:
(1) leaching reaction, namely adding the black-white tungsten mixed ore into sulfuric acid solution with the concentration of 250 g/L, introducing oxygen, wherein the liquid-solid ratio of the system is 3:1, and performing leaching reaction for 4 hours at 180 ℃ and under the pressure of 2.5Mpa to convert 99.3 percent of tungsten into tungstic acid;
(2) filtering and washing: filtering the reaction product obtained in the step (1) to obtain decomposition slag and leachate; supplementing sulfuric acid into the leachate, and returning to the step (1) to be used as a raw material for leaching reaction;
(3) hydrogen peroxide extraction-decomposition extraction of tungsten: washing the decomposition residue obtained in the step (2), mixing the decomposition residue with a hydrogen peroxide solution with the mass concentration of 5%, wherein the molar ratio of the added hydrogen peroxide to tungstic acid in the decomposition residue is 1:1, carrying out tungsten extraction reaction for 2h at the temperature of 10 ℃, and filtering the reaction product to obtain a tungstic acid peroxide solution and gypsum; directly introducing SO into peroxytungstic acid solution2The concentration of sulfuric acid in the solution is controlled to be 0.5 mol/L until the peroxytungstic acid is completely decomposed to separate out the tungstic acid, and the content of impurity elements in the obtained tungstic acid is detected to accord with the national standard GB/T10116-2007 and can be directly used in the subsequent steps;
(4) washing the tungstic acid obtained in the step (3), and mixing the tungstic acid with a hydrogen peroxide solution with the mass concentration of 30% at the temperature of 35 ℃ for reaction for 1h to obtain a pure peroxytungstic acid solution again;
(5) and (3) carrying out ultrasonic spray pyrolysis on the pure peroxytungstic acid solution obtained in the step (4) under the conditions of introducing hydrogen, the spray rate of 110ml/min, the hydrogen flow rate of 600 ml/L and the pyrolysis temperature of 1050 ℃ to obtain superfine spherical tungsten powder, wherein the content of impurities in the tungsten powder meets the requirements of national standard GB/T3458-.
Example 4
The embodiment provides a method for preparing a tungsten product by acid decomposition of a mixed ore of black and white tungsten, which adopts raw materials of the mixed ore of black and white tungsten with the grade of 45% and the granularity of 150 μm, and specifically comprises the following steps:
(1) leaching reaction, namely adding the black-white tungsten mixed ore into sulfuric acid solution with the concentration of 300 g/L, adding 50 g/L of sodium hypochlorite with the liquid-solid ratio of the system being 5:1, and performing leaching reaction for 4 hours at the temperature of 90 ℃ and the pressure of 0Mpa to convert 99.1 percent of tungsten into tungstic acid;
(2) filtering and washing: filtering the reaction product obtained in the step (1) to obtain decomposition slag and leachate; supplementing sulfuric acid into the leachate, and returning to the step (1) to be used as a raw material for leaching reaction;
(3) hydrogen peroxide extraction-decomposition extraction of tungsten: washing the decomposition residue obtained in the step (2), mixing the decomposition residue with a hydrogen peroxide solution with the mass concentration of 5%, wherein the molar ratio of the added hydrogen peroxide to tungstic acid in the decomposition residue is 1:1, carrying out tungsten extraction reaction for 2h at the temperature of 10 ℃, and filtering the reaction product to obtain a tungstic acid peroxide solution and gypsum; directly introducing SO into peroxytungstic acid solution2The concentration of sulfuric acid in the solution is controlled to be 0.1 mol/L until the peroxytungstic acid is completely decomposed to separate out the tungstic acid, and the content of impurity elements in the obtained tungstic acid is detected to accord with the national standard GB/T10116-2007 and can be directly used in the subsequent steps;
(4) washing the tungstic acid obtained in the step (3), and mixing the tungstic acid with a hydrogen peroxide solution with the mass concentration of 30% at the temperature of 35 ℃ for reaction for 1h to obtain a pure peroxytungstic acid solution again;
(5) and (3) carrying out ultrasonic spray pyrolysis on the pure peroxytungstic acid solution obtained in the step (4) under the conditions of introducing hydrogen, the spray rate being 150ml/min, the hydrogen flow rate being 400 ml/L and the pyrolysis temperature being 800 ℃ to obtain ultrafine spherical purple tungsten oxide powder, wherein the content of impurities in the purple tungsten oxide meets the requirements of national standard GB/T3457-.
Example 5
The embodiment provides a method for preparing a tungsten product by acid decomposition of a mixed ore of black and white tungsten, which adopts raw materials of the mixed ore of black and white tungsten with the grade of 35% and the granularity of 80 μm, and specifically comprises the following steps:
(1) leaching reaction, namely adding the black-white tungsten mixed ore into sulfuric acid solution with the concentration of 250 g/L, adding tungstic acid accounting for 10% of the mass of the black-white tungsten mixed ore, simultaneously adding nitric acid of 100 g/L, wherein the liquid-solid ratio of the system is 3:1, and performing leaching reaction for 4 hours at the temperature of 120 ℃ and the pressure of 1.5Mpa to convert 99.3% of tungsten into tungstic acid;
(2) filtering and washing: filtering the reaction product obtained in the step (1) to obtain decomposition slag and leachate; supplementing sulfuric acid into the leachate, and returning to the step (1) to be used as a raw material for leaching reaction;
(3) hydrogen peroxide extraction-decomposition extraction of tungsten: washing the decomposition residue obtained in the step (2), mixing the decomposition residue with a hydrogen peroxide solution with the mass concentration of 5%, wherein the molar ratio of the added hydrogen peroxide to tungstic acid in the decomposition residue is 1:1, carrying out tungsten extraction reaction for 2h at the temperature of 10 ℃, and filtering the reaction product to obtain a tungstic acid peroxide solution and gypsum; directly introducing SO into peroxytungstic acid solution2The concentration of sulfuric acid in the solution is controlled to be 0.5 mol/L until the peroxytungstic acid is completely decomposed to separate out the tungstic acid, and the content of impurity elements in the obtained tungstic acid is detected to accord with the national standard GB/T10116-2007 and can be directly used in the subsequent steps;
(4) and (4) washing the tungstic acid obtained in the step (3), and calcining at 800 ℃ for 5.0h to obtain yellow tungsten oxide. The detected impurity content in the yellow tungsten trioxide meets the requirements of the national standard GB/T3457-2013 (0-grade product).
Example 6
The embodiment provides a method for preparing a tungsten product by acid decomposition of a mixed ore of black and white tungsten, which adopts raw materials of the mixed ore of black and white tungsten with the grade of 48% and the granularity of 250 μm, and specifically comprises the following steps:
(1) leaching reaction, namely adding the black-white tungsten mixed ore into a sulfuric acid solution with the concentration of 400 g/L, adding hydrogen peroxide, wherein the liquid-solid ratio of the system is 5:1, and performing leaching reaction for 5 hours at 160 ℃ and 2.0Mpa to convert 99.5 percent of tungsten into tungstic acid;
(2) filtering and washing: filtering the reaction product obtained in the step (1) to obtain decomposition slag and leachate; supplementing sulfuric acid into the leachate, and returning to the step (1) to be used as a raw material for leaching reaction;
(3) hydrogen peroxide extraction-decomposition extraction of tungsten: washing the decomposition residue obtained in the step (2), mixing the decomposition residue with a hydrogen peroxide solution with the mass concentration of 30%, wherein the molar ratio of the added hydrogen peroxide to tungstic acid in the decomposition residue is 1.5:1, carrying out tungsten extraction reaction for 2 hours at the temperature of 30 ℃, and filtering the reaction product to obtain a peroxytungstic acid solution and gypsum; directly heating the peroxytungstic acid solution to 90 ℃ until the peroxytungstic acid is completely decomposed to separate out tungstic acid; through detection, the content of impurity elements in the obtained tungstic acid meets the national standard GB/T10116-;
(4) washing the tungstic acid obtained in the step (3), and mixing the tungstic acid with a hydrogen peroxide solution with the mass concentration of 30% at the temperature of 35 ℃ for reaction for 1h to obtain a pure peroxytungstic acid solution again;
(5) and (3) carrying out ultrasonic spray pyrolysis on the pure peroxytungstic acid solution obtained in the step (4) under the conditions of introducing argon gas, the spraying speed being 120ml/min, the argon gas flow rate being 400 ml/L and the pyrolysis temperature being 850 ℃ to obtain superfine spherical tungsten trioxide powder, wherein the content of impurities in the tungsten trioxide is detected to meet the requirements of national standard GB/T3457-2013 (0-level product).
Although the invention has been described in detail hereinabove by way of general description, specific embodiments and experiments, it will be apparent to those skilled in the art that many modifications and improvements can be made thereto based on the invention. Accordingly, such modifications and improvements are intended to be within the scope of the invention as claimed.

Claims (8)

1. The method for preparing the tungsten product by acid decomposition of the scheelite and scheelite mixed ore is characterized by comprising the following steps of:
(1) leaching reaction: adding the mixed ore of the black and white tungsten into a sulfuric acid solution for leaching reaction;
the grade of the tungsten black and white mixed ore is 10-65%; the granularity of the black-white tungsten mixed ore is less than 300 mu m;
the reaction is carried out at 50-250 ℃ and 0.5-10 Mpa;
adding solid tungstic acid which accounts for 0-20% of the mass of the scheelite and wolframite mixed ore in the reaction process for reaction; and/or adding calcium sulfate which is 0-20% of the mass of the scheelite and wolframite mixed ore as a seed crystal in the reaction process;
adding an oxidant in the reaction process to promote the reaction, wherein the oxidant is selected from one or more of oxygen, nitric acid, hydrogen peroxide and sodium hypochlorite;
(2) filtering and washing: filtering the reaction product obtained in the step (1) to obtain decomposition slag and leachate; supplementing sulfuric acid into the leachate, and returning to the step (1) to be used as a raw material for leaching reaction;
(3) hydrogen peroxide extraction-decomposition extraction of tungsten: washing the decomposition residue obtained in the step (2), mixing the decomposition residue with a hydrogen peroxide solution to perform tungsten extraction reaction, and filtering a reaction product to obtain a peroxytungstic acid solution and gypsum; heating the peroxytungstic acid solution to 50-90 ℃ or introducing SO2Until the peroxytungstic acid is completely decomposed to separate out tungstic acid; said introduction of SO2The concentration of sulfuric acid in the solution should be controlled to be 0.1 mol/L-2.0 mol/L
(4) Extracting hydrogen peroxide for multiple times, decomposing and purifying tungstic acid: detecting the impurity content in the tungstic acid obtained in the step (3), directly using the tungstic acid in the subsequent step if the impurity content meets the standard requirement, adding a hydrogen peroxide solution and repeating the operation of the step (3) at least once if the impurity content exceeds the standard requirement until a tungstic acid crystal with the impurity content meeting the standard requirement is obtained;
treating the tungstic acid with the impurity content meeting the standard requirement by adopting the following steps (5) or steps (6) to (7):
(5) calcining pure tungstic acid to prepare tungsten trioxide: calcining tungstic acid with impurity content meeting the standard requirement to obtain powdery tungsten trioxide;
(6) spray pyrolysis of a peroxytungstic acid solution to prepare tungsten oxide and tungsten powder: mixing and dissolving tungstic acid with impurity content meeting the standard requirement and a hydrogen peroxide solution to obtain a pure peroxytungstic acid solution;
(7) carrying out ultrasonic spray pyrolysis on the pure peroxytungstic acid solution under a non-reducing condition to obtain superfine spherical tungsten trioxide; and/or carrying out ultrasonic spray pyrolysis on the pure peroxytungstic acid solution under a reducing condition to obtain superfine spherical blue tungsten oxide, purple tungsten oxide and/or tungsten powder.
2. The method according to claim 1, wherein in the step (1), the concentration of the sulfuric acid is 50-500 g/L;
and/or, the reaction is carried out at 50-250 ℃ and 0.5-2.5 Mpa.
3. The method according to claim 1 or 2, characterized in that in the step (3), the mass concentration of the hydrogen peroxide solution is 5-30%, the molar ratio of the amount of hydrogen peroxide in the hydrogen peroxide solution to tungstic acid in the decomposition residue is 0.5-2: 1;
and/or the extraction reaction is carried out at the temperature of 10-40 ℃.
4. The method according to claim 2, characterized in that in the step (3), the mass concentration of the hydrogen peroxide solution is 5-30%, the molar ratio of the amount of hydrogen peroxide in the hydrogen peroxide solution to tungstic acid in the decomposition residue is 0.5-2: 1;
and/or the extraction reaction is carried out at the temperature of 10-40 ℃.
5. The method according to any one of claims 1, 2 and 4, wherein the temperature of the calcination in the step (5) is 750-900 ℃.
6. The method according to any one of claims 1, 2 and 4, wherein inert gas is introduced during the ultrasonic spray pyrolysis in the step (7), the spraying rate is 10-200 ml/min, the gas flow rate is 150-600 ml/L, and the pyrolysis temperature is 500-900 ℃ to obtain the ultrafine spherical tungsten trioxide powder.
7. The method according to any one of claims 1, 2 and 4, wherein hydrogen is introduced during the ultrasonic spray pyrolysis in the step (7), the spraying rate is 10-200 ml/min, the hydrogen flow rate is 50-600 ml/L, and the pyrolysis temperature is 500-900 ℃, so that the ultrafine spherical purple tungsten oxide powder and/or the ultrafine spherical blue tungsten oxide powder are/is obtained.
8. The method according to any one of claims 1, 2 and 4, wherein hydrogen is introduced during the ultrasonic spray pyrolysis in the step (7), the spraying rate is 10-200 ml/min, the hydrogen flow rate is 100-800 ml/L, and the pyrolysis temperature is 900-1100 ℃, so that the ultrafine spherical tungsten powder is obtained.
CN201810360985.7A 2018-04-20 2018-04-20 Method for preparing tungsten product by acid decomposition of scheelite and scheelite mixed ore Active CN108559841B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810360985.7A CN108559841B (en) 2018-04-20 2018-04-20 Method for preparing tungsten product by acid decomposition of scheelite and scheelite mixed ore

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810360985.7A CN108559841B (en) 2018-04-20 2018-04-20 Method for preparing tungsten product by acid decomposition of scheelite and scheelite mixed ore

Publications (2)

Publication Number Publication Date
CN108559841A CN108559841A (en) 2018-09-21
CN108559841B true CN108559841B (en) 2020-07-14

Family

ID=63535993

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810360985.7A Active CN108559841B (en) 2018-04-20 2018-04-20 Method for preparing tungsten product by acid decomposition of scheelite and scheelite mixed ore

Country Status (1)

Country Link
CN (1) CN108559841B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109680148B (en) * 2019-01-31 2020-10-13 北京科技大学 Method for extracting tungsten by decomposing scheelite
CN110564962B (en) * 2019-10-14 2020-12-22 中南大学 Smelting method of black-white tungsten mixed ore
CN117401716A (en) * 2023-11-01 2024-01-16 中南大学 Method for preparing tungsten trioxide from tungsten ore

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1177944C (en) * 2002-11-15 2004-12-01 自贡硬质合金有限责任公司 Method of producing tungstic acid by closed type hydrochloric acid decompose tunstite
CN103484694A (en) * 2013-08-25 2014-01-01 云南锡业集团有限责任公司研究设计院 Method for extracting bismuth from copper-bismuth concentrate
CN104593605A (en) * 2015-01-09 2015-05-06 北京矿冶研究总院 Method for processing multi-metal alloy
CN105200246B (en) * 2015-10-22 2018-06-29 中南大学 A kind of method for detaching tungsten
CN105271413B (en) * 2015-10-22 2017-03-15 中南大学 A kind of method for extracting tungsten from phosphotungstic acid/phosphotungstate solution
CN105925823A (en) * 2016-05-20 2016-09-07 江钨高技术开发应用有限公司 Method for processing scheelite concentrate through sulfuric acid to prepare tungstate solution
CN106670505A (en) * 2017-01-13 2017-05-17 昆明理工大学 Method for preparing tungsten-cobalt-carbon composite powder through spray pyrolysis method

Also Published As

Publication number Publication date
CN108559841A (en) 2018-09-21

Similar Documents

Publication Publication Date Title
CN108640156B (en) Method for preparing tungsten oxide and tungsten powder from scheelite
CN108642276B (en) Method for preparing tungsten oxide and tungsten powder by acid decomposition of scheelite
CN108425010B (en) Method for extracting tungsten and molybdenum by acid decomposition of high-molybdenum scheelite
CN108425011B (en) Method for extracting tungsten and molybdenum from high-molybdenum scheelite
CN108441629B (en) Method for preparing tungsten oxide and tungsten powder by acid decomposition of scheelite and scheelite mixed ore
CN101705380B (en) Method for recovering rare earth from rare earth-containing aluminum-silicon materials
CN108559841B (en) Method for preparing tungsten product by acid decomposition of scheelite and scheelite mixed ore
CN102424914B (en) Method for comprehensively recovering aluminum and potassium from vanadium extraction from stone coal
CN108677037B (en) Method for extracting tungsten by acid decomposition of wolframite
CN110002415B (en) Method for recovering phosphate radicals and sulfate radicals from iron phosphate production wastewater
CN108516588B (en) Method for preparing tungsten product from crude sodium tungstate solution
CN114774701B (en) Resource utilization method of industrial waste salt and waste denitration catalyst
CN102534233A (en) Vanadium extraction technology of low-grade high-calcium vanadium-containing steel slag
CN104003443A (en) Method for preparing ammonium metavanadate by adding seed crystals
CN102828037A (en) Method of preparing low-silicon low-phosphorus potassium metavanadate solution from vanadium slag
CN108611503B (en) Method for decomposing wolframite and preparing tungsten oxide and tungsten powder by oxygen pressure
CN110972479B (en) Method for producing zinc oxide by twice leaching method
CN110512095B (en) Method for extracting and stabilizing arsenic from tungsten metallurgy phosphorus arsenic slag
CN109336177B (en) Method for cleanly producing high-purity vanadium pentoxide by using hydrogen peroxide and ammonia water
CN113120938A (en) Method for preparing calcium fluoride by using fluorine-containing wastewater
CN108728674B (en) Method for extracting molybdenum from crude molybdic acid and preparing molybdenum product
CN116143174B (en) Method for preparing ammonium paratungstate by scheelite short process
CN110331297B (en) Method for preparing vanadium pentoxide from vanadium slag in short process
CN105803198A (en) Method of extracting high-purity V2O5 in dilute sulfuric acid leaching solution of stone coal vanadium ore calcine by adopting normal-temperature direct precipitation method
CN111893326B (en) Method for extracting tungsten by two-step acid decomposition method

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant