CN101020238A - Method of eliminating potassium impurity from molybdenum powder - Google Patents
Method of eliminating potassium impurity from molybdenum powder Download PDFInfo
- Publication number
- CN101020238A CN101020238A CN 200710020651 CN200710020651A CN101020238A CN 101020238 A CN101020238 A CN 101020238A CN 200710020651 CN200710020651 CN 200710020651 CN 200710020651 A CN200710020651 A CN 200710020651A CN 101020238 A CN101020238 A CN 101020238A
- Authority
- CN
- China
- Prior art keywords
- molybdenum powder
- molybdenum
- potassium
- potassium impurity
- impurity
- 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
Landscapes
- Manufacture And Refinement Of Metals (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Abstract
The method of eliminating potassium impurity from molybdenum powder includes the following steps: the first hydrogen reduction of ammonium molybdate to produce molybdenum dioxide, sieving and the secondary hydrogen reduction to produce molybdenum powder; water washing or acid pickling molybdenum powder, solid-liquid separation, stoving and sieving to obtain the molybdenum powder product. One third hydrogen reduction step may be also added after stoving. The technological process is simple and has obvious effect of eliminate potassium impurity.
Description
Technical field
The present invention relates to the preparation method of metal molybdenum, relate in particular to the process of removing potassium impurity in the molybdenum powder.
Background technology
Metal molybdenum has excellent physics and chemical properties such as high-melting-point, high-wearing feature, good heat-conductivity conducting performance and low-expansion coefficient because of it, have a wide range of applications on industrial production such as electronics, electric light source, metallurgy and metal processing industry.And molybdenum powder is a material of producing various molybdenum products, under the service condition, requires it to have higher purity to molybdenum and molybdenum powder on using mostly.
Traditional molybdenum powder preparation technology is to be raw material with the ammonium molybdate, generates molybdenum dioxide through a low temperature hydrogen reduction, carries out the secondary high-temperature hydrogen reduction after the screening, criticizes out finished product molybdenum powder through screening, combined group again.The molybdenum powder quality that above-mentioned traditional handicraft method is produced, depend on the raw material quality of ammonium molybdate to a great extent, and potassium just is the highest impurity element of content in the ammonium molybdate product, and existing molybdenum powder production technology can not effectively be removed potassium impurity, and the residual ratio of its potassium is very high.
Because potassium is the low melting point alkali metal, its fusing point has only 63 ℃, 774 ℃ of boiling points; Potassium can be combined to potassium oxide with oxygen, dissolves readily in the water, and very easily moisture absorption generation has the very potassium hydroxide of severe corrosive in air, is one of the strongest alkali.Thereby in high temperature sintering (sintering temperature is more than the 1900 ℃) process of molybdenum or as electric source material the time, potassium can evaporate with gaseous state, is bonded on the devices such as high-temperature heating element or heating light-emitting component; Or influence the insulating properties of electrical equipment after the moisture absorption, or with the corrosion of highly basic form heater element, refractory material and insulation material, polluted product surface; Even if molybdenum is as the additive of alloy or stainless steel etc., because the molybdenum of high potassium content, can bring potassium in the materials such as alloy or stainless steel into, and potassium a kind of often harmful or people in these materials do not wish the element that its exists, and directly affect the machinery and the physical property of alloy or stainless steel etc.Therefore, be badly in need of low-potassium molybdenum powder on the market.
Summary of the invention
In order to overcome the existing existing above-mentioned deficiency of process, the technical problem to be solved in the present invention provides a kind of method of removing that can remove potassium impurity in the molybdenum powder and the rational potassium impurity from molybdenum powder of technology effectively.
In order to solve the problems of the technologies described above, the method of removing of potassium impurity from molybdenum powder of the present invention, comprise hydrogen reducing of ammonium molybdate is generated molybdenum dioxide, then molybdenum dioxide is sieved, again molybdenum dioxide is carried out the secondary hydrogen reducing and generate molybdenum powder,, wash or pickling the molybdenum powder that described secondary hydrogen reducing generates, and, sieve the molybdenum powder that gets product again through Separation of Solid and Liquid and oven dry.
Process of the present invention has utilized dexterously that molybdenum does not dissolve in water or acid, molybdenum powder fine size, specific surface are big; And the easy water-soluble or sour characteristics of potassium.After molybdenum powder forms, a washing or pickling process have been increased, like this in washing or acid cleaning process, potassium impurity, and other easy molten impurity will dissolve and enter liquid phase and separate, thereby removed the impurity component in the molybdenum powder effectively, improved the purity of molybdenum greatly, molybdenum powder is best in quality, and serviceability is better.On the other hand, because the activity of potassium in ammonium molybdate is very strong, it is generally acknowledged in the practice, potassium can quicken the fission of ammonium molybdate when reduction, thereby improves the casting yield of reduction efficiency and molybdenum, and the potassium process of removing of the present invention seems very reasonable, it is to go to remove potassium behind hydrogen reducing again, this had both made full use of the advantage of potassium in ammonium molybdate hydrogen reducing process, had removed potassium impurity in the finished product molybdenum powder again, had dual technique effect.
The further technical scheme of the present invention is after Separation of Solid and Liquid and oven dry, molybdenum powder to be carried out hydrogen reducing three times.Because oxygen content is still higher in the molybdenum powder that forms after the pickling through hydrogen reducing and washing, through after the hydrogen reducing operation for the third time, can remove the oxygen element in the molybdenum powder effectively, further improved the purity of molybdenum powder.
In described washing or the pickling, the washing weight ratio of molybdenum powder and water or watery hydrochloric acid is between 1: 2～5.Described pickling cleaning solution is that concentration is 0～10% watery hydrochloric acid.Adopt water or watery hydrochloric acid as washing agent, select suitable washing weight ratio simultaneously for use, make that not only washing procedure is simple and convenient, and have desirable detersive efficiency.
40～95 ℃ of the washing reaction temperature of described water or pickling, 1～8 hour washing reaction time.Help improving dust removal rate like this, stablize impurity-eliminating effect, improve the purity of molybdenum powder.
The specific embodiment
Embodiment 1
Get potassium content and be 0.04% ammonium molybdate 1000Kg and use the multitube reduction furnace to carry out the low temperature hydrogen reduction, 400-650 ℃ of reaction warm area, ammonium molybdate push away fast 3 boats/0.5 hour, 2.5 cubic meters/hours of every pipe hydrogen flowing quantities.The molybdenum dioxide that the reduction back generates sieves, by the screen cloth in 175um aperture.Molybdenum powder is produced in the hydrogen reduction of using four pipe reduction furnaces to carry out molybdenum dioxide subsequently, and 800-980 ℃ of reaction warm area, molybdenum dioxide push away fast 1 boat/0.5 hour, 10.0 cubic meters/hours of every pipe hydrogen flowing quantities.Molybdenum powder is analyzed potassium content and is still reached 0.038%.
Get above-mentioned molybdenum powder 500kg again through the secondary hydrogen reduction, be added in the reaction pot of the strap clamp cover that is placed with the 1500Kg pure water, under stirring condition, be heated to 90 ℃, kept 3 hours, emit suction filtration, behind pure water washing secondary, put into baking oven in 80 ℃ of oven dry 10 hours, screening is by the screen cloth in 350um aperture.Certainly except that oven dry, also can adopt other common solid-liquid separating method, or solid-liquid separating method is dried etc. again.
Use four pipe hydrogen reduction furnaces to carry out high temperature reduction three times, 800-1000 ℃ of reaction warm area, molybdenum powder push away fast 2 boats/0.5 hour, 8.0 cubic meters/hours of every pipe hydrogen flowing quantities.The molybdenum powder screening is by the screen cloth in 60um aperture.Mixing equipment is the V-type batch mixer, and mixing time is 2 hours.Capable more at this moment molybdenum powder sample analysis, oxygen content 0.04%, potassium content 0.0025%.
Through above-mentioned technical process, the potassium in the molybdenum powder, oxygen major part are removed, and molybdenum powder has reached higher purity, contain assorted declining to a great extent, thus the properties of product and the result of use of the molybdenum powder that improves greatly.
Embodiment 2
In the present embodiment, the process of preparation molybdenum powder is same as the previously described embodiments.After the secondary hydrogen reduction made molybdenum powder, the molybdenum powder 500kg of the secondary hydrogen reduction of learning from else's experience was added in the reaction pot of the strap clamp cover that is placed with 1500Kg pure water and 100Kg hydrochloric acid, under stirring condition, be heated to 90 ℃, kept 3 hours, emit suction filtration, after pure water washing four times, water lotion PH≤4.Put into baking oven in 80 ℃ of oven dry 10 hours, screening is by the screen cloth in 350um aperture.
Use three high temperature reductions of four pipe hydrogen reduction furnaces, 800-1000 ℃ of reaction warm area, molybdenum powder push away fast 2 boats/0.5 hour, 8 cubic meters/hours of every pipe hydrogen flowing quantities.The molybdenum powder screening is by the screen cloth in 60um aperture.Mixing equipment is the V-type batch mixer, and mixing time is 2 hours.Carry out the molybdenum powder sample analysis, oxygen content 0.04%, potassium content 0.0022%.
Above-mentionedly enumerated two embodiments of the present invention, but above-mentioned embodiment of the present invention can only think all can not limit the present invention to explanation of the present invention, claims have been pointed out scope of the present invention.Therefore, under the situation of basic thought of the present invention,, all should think to fall within the scope of protection of the present invention as long as adopted washing or pickling process.
Claims (8)
1, a kind of method of removing of potassium impurity from molybdenum powder, comprise hydrogen reducing of ammonium molybdate is generated molybdenum dioxide, then molybdenum dioxide is sieved, carry out the secondary hydrogen reducing again and generate molybdenum powder, it is characterized in that: to the molybdenum powder of described secondary hydrogen reducing generation, wash or pickling, and, sieve the molybdenum powder that gets product again through Separation of Solid and Liquid and oven dry.
2, the method for removing of potassium impurity from molybdenum powder according to claim 1 is characterized in that: after Separation of Solid and Liquid and oven dry, molybdenum powder is carried out hydrogen reducing three times.
3, the method for removing of potassium impurity from molybdenum powder according to claim 1 is characterized in that: in described washing or the pickling, the washing weight ratio of molybdenum powder and water or watery hydrochloric acid is between 1: 2～5.
4, the method for removing of potassium impurity from molybdenum powder according to claim 1 is characterized in that: described pickling cleaning solution is that concentration is 0～10% watery hydrochloric acid.
5, according to the method for removing of claim 1,3 or 4 described potassium impurity from molybdenum powder, it is characterized in that: 40～95 ℃ of the washing reaction temperature of described washing or pickling, 1～10 hour washing reaction time.
6, the method for removing of potassium impurity from molybdenum powder according to claim 1 is characterized in that: 400～650 ℃ of the reaction warm areas of a described hydrogen reducing.
7, the method for removing of potassium impurity from molybdenum powder according to claim 1 is characterized in that: 800～980 ℃ of the reaction warm areas of described secondary hydrogen reducing.
8, the method for removing of potassium impurity from molybdenum powder according to claim 1 is characterized in that: 800～1000 ℃ of the reaction warm areas of described three hydrogen reducings.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100206517A CN100464902C (en) | 2007-03-19 | 2007-03-19 | Method of eliminating potassium impurity from molybdenum powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100206517A CN100464902C (en) | 2007-03-19 | 2007-03-19 | Method of eliminating potassium impurity from molybdenum powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101020238A true CN101020238A (en) | 2007-08-22 |
| CN100464902C CN100464902C (en) | 2009-03-04 |
Family
ID=38708159
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2007100206517A Expired - Fee Related CN100464902C (en) | 2007-03-19 | 2007-03-19 | Method of eliminating potassium impurity from molybdenum powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100464902C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105200231A (en) * | 2015-09-28 | 2015-12-30 | 昆明理工大学 | Method for preparing molybdenum powder and sulfur from molybdenite concentrate |
| CN106735193A (en) * | 2016-12-23 | 2017-05-31 | 西安瑞福莱钨钼有限公司 | A kind of preparation method of low potassium content molybdenum plate blank |
| CN110919020A (en) * | 2019-12-10 | 2020-03-27 | 河南科技大学 | Preparation method of molybdenum powder with large particle size |
| CN112338198A (en) * | 2020-10-29 | 2021-02-09 | 中国科学院过程工程研究所 | Micron-sized molybdenum powder and preparation method and application thereof |
| CN114833349A (en) * | 2022-07-04 | 2022-08-02 | 成都虹波实业股份有限公司 | Method for manufacturing low-potassium large-particle-size molybdenum powder |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57171603A (en) * | 1981-04-14 | 1982-10-22 | Nippon Tungsten Co Ltd | Production of tungsten powder of good fluidity |
| JPS6345310A (en) * | 1986-08-12 | 1988-02-26 | Tokyo Tungsten Co Ltd | Molybdenum powder and its production |
| CN1013352B (en) * | 1988-06-09 | 1991-07-31 | 天津大学冶金分校 | Manufacturing technique of supper-fine molybdenum powder |
| CN1203950C (en) * | 2003-07-22 | 2005-06-01 | 株洲硬质合金集团有限公司 | Method for preparing molybednum powder |
-
2007
- 2007-03-19 CN CNB2007100206517A patent/CN100464902C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105200231A (en) * | 2015-09-28 | 2015-12-30 | 昆明理工大学 | Method for preparing molybdenum powder and sulfur from molybdenite concentrate |
| CN106735193A (en) * | 2016-12-23 | 2017-05-31 | 西安瑞福莱钨钼有限公司 | A kind of preparation method of low potassium content molybdenum plate blank |
| CN110919020A (en) * | 2019-12-10 | 2020-03-27 | 河南科技大学 | Preparation method of molybdenum powder with large particle size |
| CN110919020B (en) * | 2019-12-10 | 2022-10-11 | 河南科技大学 | Preparation method of molybdenum powder with large particle size |
| CN112338198A (en) * | 2020-10-29 | 2021-02-09 | 中国科学院过程工程研究所 | Micron-sized molybdenum powder and preparation method and application thereof |
| CN114833349A (en) * | 2022-07-04 | 2022-08-02 | 成都虹波实业股份有限公司 | Method for manufacturing low-potassium large-particle-size molybdenum powder |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100464902C (en) | 2009-03-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100464902C (en) | Method of eliminating potassium impurity from molybdenum powder | |
| CN101648702B (en) | Method for preparing tellurium dioxide by using crude tellurium as raw material | |
| CN102161101B (en) | A method of preparing high purity tungsten material used for very large scale integrated circuits | |
| CN106517256A (en) | Method for producing lithium hydroxide monohydrate from lithium carbonate | |
| CN109336116A (en) | A method of photovoltaic high purity quartz emery dust is prepared containing feldspar ore type quartzite | |
| CN102674372A (en) | Purification method for high-purity quartz with ultra-low metal elements | |
| CN110294473B (en) | Preparation process for purifying microcrystalline graphite by organic acid catalysis | |
| CN101020239A (en) | Low potassium molybdenum powder preparing process | |
| CN113293306A (en) | Preparation method of raw material for producing cupronickel B30 from copper-nickel slag | |
| CN103539123A (en) | Acid washing purification method of submicron-sized silicon carbide micro-powder | |
| CN106745134A (en) | A kind of method of sapphire diamond wire cutting waste material recycling | |
| CN113716559A (en) | Strong acid method scale graphite purification process and device | |
| CN101347839A (en) | Method for purifying molybdenum powder | |
| CN111422890A (en) | Preparation method of high-purity beryllium hydroxide and nuclear pure-grade beryllium oxide | |
| CN102583420A (en) | Circulating preparation method for producing simple substance boron and synchronously producing sodium cryolite based on sodium fluoborate as intermediate raw material | |
| JP2009298647A (en) | Nickel oxide and production method of the same | |
| CN102616773A (en) | Method for purifying medium-carbon flake graphite to obtain high-purity graphite | |
| CN107303579A (en) | A kind of method of chloride residue dechlorination | |
| CN101875494A (en) | Preparation method of low-titanium and high-purity polycrystalline silicon | |
| CN106629809B (en) | Method for purifying coarse scandium oxide | |
| CN102367181A (en) | Process for preparing potassium manganate by liquid phase method | |
| JP5429081B2 (en) | Manganese ore processed material | |
| CN102557096A (en) | Circulating preparation method for producing simple substance boron by using potassium fluoborate as intermediate material and synchronously producing elpasolite | |
| CN106044805A (en) | Method for preparing beryllium chloride | |
| CN101544399B (en) | Method for directly producing potassium stannate by using tin raw material |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090304 Termination date: 20160319 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |