Tungsten Alloy Tennis Rackets CounterweightsⅠ

Tennis rackets counterweights refers to installing the counterweights in the edge of the tennis rackets so as to achieve the aim of altering the balance of tennis rackets to improve the hitting force of the players. The tennis rackets counterweights are mainly made of tungsten alloy materials, which are non-toxic and environmentally friendly. The counterweights that made of tungsten alloy (the following picture shows the different shapes of tungsten alloy counterweights) can be divided into ordinary tungsten alloy counterweights and special tungsten alloy counterweights in accordance with the uses of counterweights.
tungsten-alloy-counterweights
As the name suggests, ordinary tungsten alloy counterweights means that can be prepared by rough machining, it is no strict to the counterweights’ surface and accuracy requirements. The weight and volume of this kind tungsten alloy counterweights are relatively large, and mainly used as the counterweight blocks such as: marine ballast counterweights.
 
Comparing with the ordinary tungsten alloy counterweights, Special tungsten alloy counterweights relatively has the finer manufacturing process,the shapes of counterweights are more complex, and their weights and volumes are relatively small. Special tungsten alloy counterweights are mainly used to the things which need to weight, such as golf head counterweights, watches counterweights, the crankshaft counterweights of autos, the fly wheels counterweights of heavy machines and tennis rackets counterweights and so on. Why should we increase the counterweights to tennis rackets? What’s the theory of controlling the tennis rackets with counterweights? And which materials can be used to prepare tennis rackets counterweights? 

 

Temperature’s Effects on Ammonium Paratungstate Production

Ammonium paratungstate (APT) is an important intermediate product of the production of tungsten metal powder. To ensure the quality of tungsten powder, the average particle size, particle size distribution and crystal morphology should also meet certain requirements while the APT chemical purity does. With the rapid development of modern science and technology, there’re more and more demands for different grain size and shape of tungsten powder production, and thus the requirements of raw material APT are also getting higher and higher.
 
For APT crystallization conditions, the scholars have carried out extensive exploration and discussion, but the overall reports are rare, and the results are not entirely consistent. In order to investigate the basic conditions of APT production, for the preparation of APT crystallization problems, this article attempts to make some analysis and discussion on theory and the process practice based on a number of experimental studies made recently and some views are put forward by reference.
 
Test results are shown on Figure. With the increase of evaporation temperature, the crystal growth rate of APT is faster than the nucleation rate, which makes a particle size enlargement and increases the bulk specific gravity of APT (see figure). The reasons are increasing temperature , faster molecular motion, more opportunities of molecules colliding with each other, which are conducive to grain growth. 
 
Plane grain formation rate on the grain surface is affected a lot by temperature. When temperature increases to 10 ℃, speed needs to increase 2 to 4 times, so the increasing temperature is most significant for grain growth. It was also observed in the experiment that APT crystalline grains were much coarser than other parts on the crystallizer wall. This may be due to an indirect steam heating, the temperature on wall is higher than other parts , which is conducive to grain growth. It was also found in the experiment that the crystalline particles is more regular in a higher temperature than a lower one, and size distribution is more well-distributed.
 
Figure 4

 

Effect of Stirring Speed on Ammonium Paratungstate Production

Ammonium paratungstate (APT) is an important intermediate product of the production of tungsten metal powder. To ensure the quality of tungsten powder, the average particle size, particle size distribution and crystal morphology should also meet certain requirements while the APT chemical purity does. With the rapid development of modern science and technology, there’re more and more demands for different grain size and shape of tungsten powder production, and thus the requirements of raw material APT are also getting higher and higher.
 
For APT crystallization conditions, the scholars have carried out extensive exploration and discussion, but the overall reports are rare, and the results are not entirely consistent. In order to investigate the basic conditions of APT production, for the preparation of APT crystallization problems, this article attempts to make some analysis and discussion on theory and the process practice based on a number of experimental studies made recently and some views are put forward by reference.

The test results are shown in Figure 2. It’s complicated that stirring speed affects nucleation. On one hand, the stirring speed is accelerated, so that the newly formed crystals were minced and the form much crystal nucleus, particle size becomes fine, on the other hand, in a certain stirring speed range, increasing the stirring speed can increase the relative velocity between solid and liquid, thereby increasing the speed of nuclei grow. 
 
To prepare coarse APT, the best speed is when the resulting APT does not precipitate,  APT particle formed can make full contact with the solutes. It was also found  the effect is not the same with different paddles stirring or different stirring intensity. Stirring has a great impact on the preparation of the different particle size of APT, APT prepared by gas stirring is more regular . For different production conditions, it’s generally required to determine the proper form and speed of stirring through practice.
 
effects on APT bulk density

 

Tungsten Trioxide Introduction 3/3

Tungsten Trioxide - Preparation
Tungsten concentrate with sodium hydroxide or soda from the melt temperature, or high pressure sodium tungstate solution prepared boiled, and then purified by ion exchange or extraction, evaporation process to obtain ammonium paratungstate crystals, and then calcined at 700 ℃ to obtain tungsten trioxide. If you are scheelite concentrate as raw material, can also be decomposed into hydrochloric acid ,, then by ammonia dissolution, evaporation process to obtain ammonium paratungstate crystals were then calcined at 700 ℃ was prepared by the tungsten trioxide. It can also be directly obtained by calcining tungstate tungsten trioxide. The main reaction is as follows:

FeWO4 + 4NaOH → 2Na2WO4 + Fe (OH) 2

MnWO4 + 4NaOH → 2Na2WO4 + Mn (OH) 2

CaWO4 + 2HCI = H2WO4 + CaCI2  

H2WO4 + 2NH4 (OH) = (NH4) 2WO4 + 2H2O

12Na2WO4 + 14HCl → 5Na2O • 12WO3 + 14NaCl + 7H2O

5Na2O • 12WO3 + 10NH4Cl → 5 (NH4) 2O • 12WO3 + 10NaCl

5 (NH4) 2 • 12WO3 + 10HCl + 7H2O → 12H2WO4 + 10NH4Cl

H2WO4 → WO3 + H2O

5 (NH4) 2O-12WO3-6H2O → 12WO3 + 10NH3 ↑ + 11H2O

Tungsten Trioxide - Inspection
Weigh 0.5g sample, accurate to 0.000 2g, placed in 250mL beaker high type ammonia solution 40mL, cover the surface of the dish and heated in the furnace temperature, the solution was kept close to boiling point, stirring while heating the sample to complete dissolved, remove the hydrochloric acid was added 10mL After cooling to room temperature, carefully placed on a boiling water bath boiling concentrated by evaporation to a volume of about 10mL. The solution was diluted with 70 ℃ warm water to 70mL ~ 80mL, stirring constantly adding hydrochloric acid cinchonine solution 10mL, placed in a water bath (70 ℃ ± 5 ℃) on the insulation 1h, stirring once every 20min, the solution was filtered by pouring method (using Slow 11cm quantitative filter paper), glass and precipitated with beaker wall attached to a quantitative filter paper slowly wipe precipitate was washed with hydrochloric acid cinchonine lotion several times, volume control and the filtrate and washings about 180mL. The precipitate and filter paper moved to a constant weight of platinum crucible in an electric furnace carefully placed after ashing temperature furnace (750 ℃) in burning 10min, removed, cooled to room temperature was added 3mL ~ 5mL hydrofluoric acid and a few drops sulfuric acid, in a boiling water bath after nearly dry steam to move to the electric heating, the risk to make white smoke, then placed in a high temperature furnace (750 ℃) in burning 30min, removed, placed in a desiccator to cool to room temperature, weighed, repeated several times until a constant weight.

NOTE: The sample was dissolved with ammonia, the solution should be avoided so violent boiling, reduce volatilization of ammonia. If long after dissolving solution always appears cloudy or residue, quantitative filter paper, then with warm ammonia [1.5% (m / m)] repeatedly washed thoroughly beaker and filter paper, collect the filtrate and washings continue remaining experiment.

Expression of Results
Tungsten trioxide content expressed as a percentage by mass, according to equation (1):
    X(%)=(m1-m2)÷m0
Wherein: X- mass percentage of tungsten trioxide, %;
m0- crucible, g;
m1- crucible and precipitation, g;
m2 Quality sample, g;
The average of the two measurements, the results reservations two decimal places;
The precision r = 0.25%; R = 0.42%.

 

 

Tungsten Trioxide Introduction 2/3

Tungsten Trioxide - Precautions
Health hazards: low toxicity. The eyes, skin irritation. Tungsten steel smelting workers had systemic weakness, fever, measles-like rash, proteinuria, may be inhaled and smelting of tungsten trioxide related.

Explosion Hazard: This product is flammable, irritating.

Aid Measures
Skin contact: Remove contaminated clothing, rinse with plenty of water.
Eye contact: Did eyelid, mobile water or saline rinse.
Inhalation: rapidly from the scene to fresh air. Keep the airway open. If breathing is difficult, give oxygen. If breathing stops, artificial respiration immediately.
Ingestion: drink enough water, induce vomiting.

Fire-fighting Measures
Hazardous characteristics: with halogen compounds such as bromine pentafluoride, chlorine trifluoride react violently.
Hazardous combustion products: harmful toxic fumes.
Fire fighting methods: firefighters must wear fire protective body suits, the wind on fire. As far as possible to move containers from the scene empty Department for fire fighting. Then select the appropriate fire extinguishing agent fire reasons.

Accident
Emergency treatment: Isolation leak contaminated areas, restricting access. Recommended emergency personnel wearing dust masks, wearing overalls general operations. Do not direct contact with leakage.

A small leak: to avoid dust, carefully scan, collected in dry, clean, covered containers.

Large Leak: recycling or collection shipped to the waste disposal sites.

Handling and Storage
Handling Precautions: closed operation, local exhaust. Prevent dust released into the air workshop. The operator must go through specialized training, strict adherence to rules. Proposed operators wear self-absorption filter respirators, wearing chemical protective safety glasses, wear rubber acid suit, wearing rubber gloves acid. Avoid generating dust. Avoid bromine pentafluoride, chlorine trifluoride touch. Equipped with spill response equipment. Empty containers may be harmful residues.

Storage: Store in a cool, ventilated warehouse. Away from fire, heat source. Prevent direct sunlight. Packing seal. It should bromine pentafluoride, chlorine trifluoride stored separately and avoid mixing reservoir. Storage areas should be equipped with suitable material spill.

 

Tungsten Trioxide Introduction 1/3

Tungsten trioxide is yellow powder. It dissolves in water, soluble in alkali; slightly dissolves acid .It is used to make refractory alloys and tungsten carbide, tungsten and fire system materials. Tungsten ore and soda ash by eutectic after adding acid derived. It depends on the structure of the tungsten trioxide temperature: 三氧化钨740 ° C above it is tetragonal; 330-740 ° C is orthorhombic; 17-330 ° C is monoclinic; -50-17 ° C for the three triclinic. Tungsten trioxide is mainly used in the production of tungsten reduction calcined powder and tungsten carbide powder, and then used to produce carbide products, such as tool and die manufacturing. Tungsten concentrate with sodium hydroxide or soda from the melt temperature, or high pressure sodium tungstate solution prepared boiled, and then purified by ion exchange or extraction, evaporation process to obtain ammonium paratungstate crystals, and then calcined at 700 ℃ to obtain tungsten trioxide.
Chinese name: tungsten trioxide
Chinese alias: tungsten anhydride; tungsten oxide (VI)
English name: Tungsten trioxide
 

Tungsten Trioxide - Physical and Chemical Properties
Physical Properties

物理性质

Tungsten Trioxide Structure

Tungsten Trioxide Structural Formula
Melting point (℃): 1472
Relative density (water = 1): 7.16
Boiling point (℃): 1837
Formula: WO3
Molecular Weight: 231.85
Solubility: insoluble in water, soluble in alkali, slightly soluble in acid

Chemical Properties
Significant sublimation at 850 ℃; hardly inorganic acid except hydrofluoric acid and can slowly dissolve in ammonia or concentrated alkali solution. Heating the reaction of chlorine and chlorine oxides, but not reacted with bromine, iodine. Structure depends on the temperature of tungsten trioxide: it is more than 740 ° C for the tetragonal, 330-740 ° C orthorhombic, 17-330 ° C for the monoclinic system, -50-17 ° C for the three triclinic. The most common structures monoclinic, space group P21 / n.

Tungsten Trioxide - Specifications

 三氧化钨规格
Tungsten Trioxide Specifications

Tungsten Trioxide - the Role and Purpose
Tungsten trioxide is mainly used in the production of tungsten reduction calcined powder and tungsten carbide powder, and then used to produce carbide products, such as tool and die manufacturing. But also it can be used in the manufacture of pure tungsten products, tungsten, tungsten, tungsten electrode; and uses a counterweight and radiation shielding materials. Industrial production is also a small amount of yellow ceramics used as a coloring agent. Shipbuilding industry, tungsten oxide, tungsten is used as an important anti-corrosion paint and coatings materials.

 

Cupric Sulphate Precipitation Eliminating Molybdenum of Sodium Tungstate

In the process of decomposition of tungsten ore alkali, the impurity molybdenum will enter the sodium tungstate solution. Therefore, how to remove molybdenum from tungsten alkali leaching liquid and achieve the deep purification of the crude sodium tungstate solution are the major issues of improving the quality of tungsten products and expanding the comprehensive utilization of resources. The classic sulfide precipitation of purifying the sodium tungstate solution is still widely used in the tungsten metallurgy. The advantage of this method is simpleness and easily removing part of molybdenum in the solution. Its shortcomings are emitting toxic gases of hydrogen sulfide unavoidably in the process of molybdenum sulfide precipitation to pollute environment. The effect of eliminating molybdenum is not good enough and has great lost of tungsten. Typical extraction agent, which is used by Solvent extraction method for the purification of crude sodium tungstate solution, has a neutral phosphorous extraction agent, acid phosphorus extraction, nitrogen extraction agent, containing sulfur extraction agent, oxygen extraction agent, etc. Due to effect of selective, split phase, toxicity, economic problems, above-mentioned extraction agent has not been widely used. Eliminating molybdenum of sodium tungstate solution by using precipitating agent with copper sulfate is a kind of simple and practical method.
 
About operation process of this method is as follows: the first react with sodium sulfide sodium molybdate formed glucosinolates molybdate, tungsten compounds are still in the form of tungstate in solution. After vulcanization joined the crude sodium tungstate solution of copper sulfate, sulphur molybdenum acid radical generation and the generation of the combination of undissolved compound precipitate, realize the separation of tungsten and molybdenum. Then see the test method, first with dilute sulphuric acid and dilute sodium hydroxide solution of sodium tungstate solution to the required pH value, add a certain amount, sodium sulfide control proper curing temperature and time of vulcanization. Add a certain amount, after the completion of sulfide copper sulfate, control the appropriate temperature and time of reaction. 
 
After the completion of reaction heat filtration, the filtrate third tungsten and molybdenum oxide content can learn by experiment: 
1. Using sodium sulphide for vulcanizing agent, copper sulfate as precipitant, precipitated sulfur generation of molybdenum acid radical, can achieve effective separation of molybdenum and tungsten. During vulcanization, better conditions for the amount of sodium sulfide three times the amount on the theory of curing temperature 70 ℃, the curing time of 90 min, the sodium tungstate solution pH 7.
2, when precipitation temperature is 80 ℃, precipitation time is 120 minutes, precipitating agent dosage of copper sulfate for theory is five times of the amount of precipitation, it’s efficiency is highest. 
3. The sediment can be recycled molybdenum oxide treatment of residual copper compounds can be treated to return to the precipitation process. With copper sulfate precipitation despite the molybdenum of crude sodium tungstate solution, has the reagent was cheap, generating hydrogen sulfide gas, the operating conditions, grasp the advantages of easy to control. This method is not only simple, easily controlled but also has little pollution.
 

 

Anion Exchange Resin Eliminating Molybdenum of Sodium Tungstate

In order to separate tungsten and molybdenum, people studied the methods of ion exchange method and solvent extraction. These methods are mainly used for depth from tungstate solution to remove a small amount of impurity molybdenum or from acid salt solution depth to remove a small amount of impurities in tungsten. When high impurities content of molybdenum and tungsten in the solution, the above method is difficult to apply. But the method of using alkalescent anion exchange resin can effectively eliminating the molybdenum from sulfurized sodium tungstate solution.
 
It is well known that the affinity of molybdenum for sulfur is far greater than the affinity of tungsten for sulfur. Under the condition of weak alkaline, MoO2-4 can be vulcanized to sulfur acid radical ion preferentially. While tungsten still exists in the form of WO2-4. MoOxS2-4 - x has a strong affinity to the alkalescent anion exchange resin. The stronger the alkaline of resin is, the bigger of the affinity of MoOxS2-4 - x. But when MoOxS2-4 – x was adsorbed with strongly alkalescent anion exchange resin, MoOxS2-4 - x are difficult to desorption. The antioxidant of sodium hypochlorite or hydrogen peroxide must be added in desorption agent. MoOxS4 - x can be adsorbed after oxidation. This not only increases the difficulty of operation, but also causes the oxidation of resin. 
 
While the resin adsorption capacity of molybdenum is very small, MoOxS2-4 - x is easy to be adsorbed by NaOH solution so as to overcome the desorption difficulty. How to further improve the resin adsorption capacity of aluminum will has a good application prospect. According to the ion exchange equilibrium principle, the adsorption capacity of ion exchange resin will become bigger with the increase of the ion adsorption equilibrium concentration in the solution. So the adsorption and desorption behavior of alkalescent anion exchange resin in sodium tungstate solution can improve the adsorption capacity of resin and has the value of industrial application. 
 
According to this method we can draw the following conclusions:
1. The resin adsorption capacity of molybdenum significantly increases when molybdenum concentration is higher by using alkalescent anion exchange resin method to adsorb MoOxS2-4 – x. And in the dynamic adsorption, the adsorption capacity of molybdenum can also achieve high value and has practical value. At the same time, the resin can be desorbed by using the NaOH solution of 1.0mo/L concentration. The rate of desorption achieves 97.3%.
2. About the tungsten acid salt solution including molybdenum and sodium carbonate, the molybdenum adsorption rate and adsorption capacity can be significantly improved by using NaHS as vulcanizing agent. Thus it overcomes the adverse effect of molybdenum adsorption efficiency by reason of the competitive adsorption of carbonate ions. 
3. Because sulfur acid radical ion to WO2-4 displacement process exists within the ion exchange column, the adsorption capacity and the effect of eliminating molybdenum in the process of dynamic adsorption were better than the static adsorption process. As a result, the method of using alkalescent anion exchange resin can effectively eliminating the molybdenum from sulfurized sodium tungstate solution.
 

 

Recycling and Reusing Ammonium Paratungstate Crystal Liquor 3/3

M115-a is a new type of reagent people developed in recent  years,and it became highly respected once input application, because it played a significant role in solving the long-standing separation of tungsten and molybdenum tungsten industry.M115-a deals with sodium tungstate,ammonium tungstate solution,it can also deals with APT crystal liquored effectively the same time. The basic principle is using the difference in structure and ionic radius between ion of tungsten and ion molybdenum added,and the M115-a is preferentially precipitated with ion molybdenum and some other ion impurities to form insoluble substance,that way mutual separation achieved.
 
Design that Mo in the mother liquor concentration be 0.1~0.5 g/L, the concentration of WO3 is 15~18G/L,ion molybdenum precipitated down after adding M115-a,content of Mo in the mother liquor will drop to 0.005g/L,and useful components like WO3 and NH4Cl is retained in the mother liquor, reserving forthe follow-up process.
 
The huge advantage of M115-a lies in:the depth in removing impurity,good quality of mother liquor return to the main flow. Compared to the traditional technology of sheltie deposition,recovery rate of WO3 can be increased by about 10%, NH4Cl utilization rate raised from 0 up to 70%~80%, and wastewater eliminated.The mother liquor can be directly returned to the production for tungsten recovery.Effective use of NH4Cl at the same time,economic performance improved.And M115-a selective 
precipitation has the advantage of short process,sample equipment,low cost,easy to grasp,and suitable for both classical process and exchange process,it become a kind of method that with broad prospects.

For Recycling and Reusing Ammonium Paratungstate Crystal Liquor 1/3,please see in
http://news.chinatungsten.com/en/tungsten-information/81761-ti-10572

Recycling and Reusing Ammonium Paratungstate Crystal Liquor 2/3

Method two:Residual alkali decomposition 
Literature of<Research and practice of WO3 industrial method of ammonium paratungstate mother liquor recovery lime precipitation> pointed out that WO3 mainly appears in the form of tungstate or ammonium paratungstate,and accompany a few heteropoly acid salt and a large number of Mo and other impurities.The method of residual alkali decomposition  using coarse sodium tungstate in the residual alkali(alkali containing about 30~40g/L) reacte with tungsten and ammonium molybdate in mother liquor,reaction equation as follows:
2NaOH+(NH4)2WO4→Na2WO4+2NH4OH 
2NaOH+(NH4)2MoO4→Na2MoO4+2NH4OH
 
Adding 5 times of theoretical amount of Na2S into the solution we obtained after response,Mo precipitation sinking in the form of 
MoS3 in acidic(pH =2.5~3.0) environment,after filtration,solution return to main flow to combine with sodium tungstate for impurity 
removal, reserving for subsequent machining, mainly process shown in figure:
 
The mother liquor that dealing by alkali decomposition method combined with sodium tungstate will show an obvious effect. Also,it does no harm to the whole processing,and the APT it producing meets the requirement of high purity.

For Recycling and Reusing Ammonium Paratungstate Crystal Liquor 1/3,please see in 
http://news.chinatungsten.com/en/tungsten-information/81754-ti-10570

 

 

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