Coated Cemented Carbide Process III

Based on traditional chemical vapor deposition (CVD) and physical vapor deposition (PVD), some new coating technologies are emerging.

5. Plasma Chemical Vapor Deposition (PCVD)

Plasma Chemical Vapor Deposition (PCVD) uses the kinetic energy of charged particles of plasma to inspire the vapor chemical reaction. The basic principle is that deposited a film with high hardness and high wear resistance on the surface of metal matrix, such as titanium nitride (TiN), TiAlN, TiCN, TiSiN hard film and so on. Different from traditional chemical vapor deposition (CVD), PCVD has lower deposited temperature (about 500-600℃), which reduces the deposition directionality and makes the coating uniform. At present, the coating temperature of latest PACVD decreases to 180-200℃, the welding properties is much better and the welding place is no affected, which is suitable for welding-used tungsten carbide cutting tools and the surface hardening process of mold. The experimental data shows that compared with common high-speed steel drills, tungsten carbide drill by PCVD has higher efficiency, better comprehensive properties (wear resistance and corrosion resistance) and the service life extended about 10 times in the process of steel machining.

6. Vacuum Cathodic Arc Deposition (VCAD)

Vacuum Cathodic Arc Deposition (VCAD) is a kind of process that uses cathodic arc to evaporate and disassociate the target and deposited under negative bias voltages, which has many advantages, such as lower deposition temperature, higher deposition rate, larger covered acreage deposition, high ion energy, high ionization rate, good binding force between the film and the matrix, simple operation and simple equipments, etc. It can be widely used in TiN, TiC and some super-hard film deposited.

Some researcher study that based on the original process of vacuum cathodic arc deposition TiN film, uses titanium aluminum to take place of titanium target for deposited the (Ti, Al)N film with excellent properties, which is beneficial for pushing forward (Ti, Al)N film industrialized producing. Except applied in some metal film with high quality, VCAD is also suitable for Ta-C, optical film, transparent conductive oxide film, nitride multi-layers, nano composite film, MAX phase and some various film deposited.

coated cemented carbide

 

Wolframite Species

In the mineralization, most majority of tungsten forms into oxides (tungstate) , rarely sulfide, no natural tungsten. Currently it’s found only about 20 kinds of tungsten ores and minerals containing tungsten in the crust. Here are the introductions of wolframite species.

Huebnerite: 
Hübnerite or hubnerite is a mineral consisting of manganese tungsten oxide (chemical formula: MnWO4, it isn't a tungstate). It is the manganese endmember of the manganese - iron wolframite solid solution series. It forms reddish brown to black monoclinic prismatic submetallic crystals. The crystals are typically flattened and occur with fine striations. It has a high specific gravity of 7.15 and a Mohs hardness of 4.5. It is transparent to translucent with perfect cleavage. Refractive index values are nα=2.170 - 2.200, nβ=2.220, and nγ=2.300 - 2.320.
Typical occurrence is in association with high-temperature hydrothermal vein deposits and altered granites with greisen, granite pegmatites and in alluvial deposits. It occurs associated with cassiterite, arsenopyrite, molybdenite, tourmaline, topaz, rhodochrosite and fluorite.
It was first described in 1865 for an occurrence in the Erie and Enterprise veins, Mammoth district, Nye County, Nevada, and named after the German mining engineer and metallurgist, Adolf Hübner from Freiberg, Saxony.

Hubnerite
 
Ferberite: 
Ferberite is the iron endmember of the manganese - iron wolframite solid solution series. The manganese endmember is hübnerite. Ferberite is a black monoclinic mineral composed of iron(II) tungstate, FeWO4.
Ferberite and hübnerite often contain both divalent cations of iron and manganese, with wolframite as the intermediate species for which the solid solution series is named.
Ferberite occurs as granular masses and as slender prismatic crystals. It has a Mohs hardness of 4.5 and a specific gravity of 7.4 to 7.5. Ferberite typically occurs in pegmatites, granitic greisens, and high temperature hydrothermal deposits. It is a minor ore of tungsten.
Ferberite was discovered in 1863 in Sierra Almagrera, Spain, and named after the German mineralogist Moritz Rudolph Ferber (1805–1875).

Ferberite
 
Wolframite:
Wolframite, (Fe,Mn)WO4, is an iron manganese tungstate mineral that is the intermediate between ferberite (Fe2+ rich) and hübnerite (Mn2+ rich). Along with scheelite, the wolframite series are the most important tungsten ore minerals. Wolframite is found in quartz veins and pegmatites associated with granitic intrusives. Associated minerals include cassiterite, scheelite, bismuth, quartz, pyrite, galena, sphalerite, and arsenopyrite.
This mineral was historically found in Europe in Bohemia, Saxony, and Cornwall. China reportedly has the world's largest supply of tungsten ore with about 60%. Other producers are Canada, Portugal, Russia, Australia, Thailand, South Korea, Rwanda, Bolivia, the United States, and the Democratic Republic of the Congo.

 

Tungsten Mineral Species

In the mineralization, most majority of tungsten forms into oxides (tungstate) , rarely sulfide, no natural tungsten. Currently it’s found only about 20 species of tungsten ores and minerals containing tungsten in the crust.
 
Wolframite family: huebnerite, ferberite, wolframite;
Scheelite family: scheelite (calcium tungstate mineral), seyrigite, cuproscheelite;
Tungstite minerals: tungstite, meymacite, ferritungstite, yttrotungstite, cuprotungstite, anthoinite;
Unusual tungsten minerals: stolzite, raspite, sanmartinite, russellite, scheteligite, yttrocrasite (tungsten) and tungstenite.
 
Wolframite (wolframite) and scheelite (calcium tungstate mineral) have most industrial value.

Minerals

Huebnerite

Wolframite

Ferberite

Scheelite

Formula

MnWO4

(FeMn)WO4

FeWO4

CaWO4

WO3 %

76.5

76.6

76.3

80.6

Crystal System

monoclinic

monoclinic

monoclinic

square

Cleavage

Along the 

oblique plane

Along the 

oblique plane

Along the 

oblique plane

Parallel to 

the cone

Mohs Hardness

5-5.5

5-5.5

4-4.5

4.5-5

Density

7.2-7.5

7.1-7.5

6.8

5.9-6.2

Magnetism

weak

weak

weak

no

 
Wolframite formed iron tungstate and manganese tungsten transition minerals with same crystal structure, from which manganese and iron two elements can replace each other indefinitely. When content of manganese is relatively large (greater than 17.6%), huebnerite is formed; when content of manganese is fewer (less than 5.9%), ferberite is formed; when content of manganese is in between, wolframite is formed. The WO3 content of above three wolframites is more than 70%.
 
Color wolframite are dark gray, reddish brown, light brown black, taupe and iron brown and other colors, with a submetallic luster, metallic luster and resinous luster. It is monoclinic, brittle, with irregular-shaped fracture. Wolframite is usually leaf-shaped, curved flake, granular and compact shape, and some were thick plate, pointed columnar form distribution, often with white quartz vein together to form filled in and near the law granite rock crevices .

 

The Main Problems of China Tungsten Industry Development (2)

The main problems of China tungsten industry are excess production capacity, striking industrial structural contradictions, scarce R&D ability of high-grade products and input-output ratio of resource is not high. Besides, production cost increase, low international competitiveness, during industry development imbalance, discordant and unsustainable deep-rooted problems and constrictions are more prominence. What’s more, the consciousness of environment protection has enhanced, so China tungsten industry have to change traditional development patterns which depends on consume resources, increase production and sacrifice environment so that China tungsten industry can not only follow international tungsten industry development pace but also can develop better. As below I will more specifically introduce the main problems of China tungsten industry development.
1. Low-level redundant development, acute overloads production contradiction
According to statistic, in the end of 2014, China produced ammonium paratungstate 214,000.00 ton, tungsten powder 762,000.00 ton, tungsten cemented carbide 411,000.00 ton, tungsten wire 35 billion meter, and ferro tungsten 30,000.00 ton on the other hand, the rate of capacity utilization is 41.1%, 49.87%, 63.75%, 63.75%, 45.14% and 19.00% respectively.
2. Low industry contraction, development quality and benefit
China has lot of tungsten companies, but they are scattered, small and weak and this situation is not fundamental change. Besides, industry contraction is low and international competitiveness is not high. According to statistic, in 2013, 193 tungsten companies annual average production was less than 500 ton. Only 21 tungsten company annual production was higher than 1000 ton accounts for 50.28% of production. In 2014, only 3 tungsten companies produce more than 1,000.00 ton cemented carbide accounted for 45.7% of production. And the sales revenue of tungsten cemented carbide was 22 billion RMB and benefit was less than 1 billion RMB.

 

tungsten-alloy

 

 

The Main Problems of China Tungsten Industry Development (1)

China has abundant tungsten ore resources. After experienced early period unauthorized mining China government has employed a series of policy to promote tungsten industry development so that China tungsten industry has entered a phase of steady development. At the present, due to deteriorating global economic situation, China and international tungsten industry situation is not optimistic. To understanding the main problem which has occurred during China tungsten industry development process is very important for tungsten industry development.
1. Intensive mining, tungsten ore reserve-production ratio imbalance
Tungsten is an important strategic resource. However, China tungsten total reserve amount ratio accounts for less than 50% of global tungsten total reserve amount, but China has provided 80% global tungsten consumption. What’s more, China reserve-production ratio is less than one fourth with oversea reserve-production. According to the data China tungsten resource has small range increase, but the basic reserve has obviously declined. The tungsten resources superiority of China has been reduce and resource security situation is not optimistic.
2. Lacking independent innovation ability, low technology, content and low added value of products
Comparing with global tungsten industry, China tungsten industry is in the mid-range of global tungsten industry chain. There are great gap between China tungsten industry and advanced international tungsten industry. For example, digital, automation and intelligentize production process, enterprise management informatization, product specialization, scientific and technical innovation integration, market and talents globalization is low-level. Besides, taking company as main part, the scientific and technical innovation mechanism which combines with production, research, study and application is not quite complete. What’s more, research and development spending is less and also lack of high-end technical personnel so R&D ability is weak. What’s more, tungsten industry advanced technology of deep-processing and key areas have little major breakthroughs and originality alloying technique outcome also low. The products of tungsten are mainly mid-low-end which can’t meet China domestic high-end manufacturing’s requirements, so high quality, high precise and high-grade cemented carbide digital cuttings and other high technological content, high added valued tungsten products need to import from oversea.   

tungsten-ore

Tungsten Trioxide Hydrogen Reduction Factors

The gas-solid multiphase reaction of Hydrogen (H2) reduction of tungsten trioxide (WO3) is:

WO3+3H2 ===W+3H2O

Reduction Temperature
Volatile tungsten oxide increases with increasing temperature, the higher the reduction temperature, the more water vapor can promote the formation of tungsten oxide and volatile hydrate WOx • nH2O and restored good and cheap tungsten powder particles of tungsten oxide surface that is reduced, which leaving the primary particles grow thick. Since WO3 greater volatility than the WO2, therefore, the production of fine particles of tungsten powder requires the use of a lower reduction temperature. Generally speaking, we use two-stage reduction, the first reduction (WO3 - WO2) should be adopted a lower reduction temperature, while the second reduction (WO2 - W) used a high temperature reduction. Production of coarse particles of tungsten powder is used for some high-temperature reduction (direct reduction) method.

Hydrogen Humidity and Flow
Effect of humidity on hydrogen tungsten powder particle size is very significant. Hydrogen humidity, which is conducive to the formation of tungsten oxide and water vapor volatile hydrates and restored good tungsten powder and tungsten oxide surfaces, resulting in tungsten powder particles grow. In favor of increasing the hydrogen flow rate of water vapor reduction product discharged in time, it increases the reduction reaction speeds, it is easy to obtain fine particles of tungsten powder.

Boat Loading Capacity (Material Thickness)
More than the amount loaded boat or material layer is too thick, hydrogen is difficult to penetrate deep inside the material layer. The inner layer of tungsten oxide reduction is not complete, the steam generated is also difficult to discharge, causing the boat long thick inner layer of tungsten powder, and obtained tungsten powder particle size is uneven.

Push the Boat Speed
Push the boat speed, reducing short time. Tungsten trioxide will not enter the high-temperature region in stepwise reduction of chance to low temperature materials, which resulting in growth and high oxygen content of the tungsten powder. Pushing the boat speed is too slow, tungsten trioxide residence time in the high temperature zone too long; it is easy to grow thick and decreases productivity for tungsten powder.

Temperature Gradient
Large temperature gradient furnace is equivalent to push the boat too fast, which can lead to volatile metal tungsten oxide particles grow.

WO3 Original Size and Impurity
When the reduction process was controlled by hydrogen reduction of fine particulate WO3 generally get fine particles of tungsten powder; but since the surface of the fine particles of WO3 can be high, you may get coarser tungsten powder if reducing improper process control. WO3material containing metal sodium impurities, which will lead to more long thick tungsten powder; molybdenum or chromium and other impurities can inhibit the role of long thick tungsten powder.

 

Tungsten Trioxide Coulomb Titration Sulfur Effect

When tungsten trioxide in Coulomb titration burning sulfur, the organic sulfur can all break down at 800 ℃ ~ 900 ℃,while the sulphate sulfur requires to decompose at 1100 ℃ ~ 1200 ℃, so in order to ensure that coal various forms of sulfur can all decompose, there must be a higher oven temperature, on the other hand, SO2 + O2 = SO3-Q, between sulfur dioxide and sulfur trioxide in the presence of oxygen and heated environment, which is a reversible reaction, while trioxide sulfur does not participate in the reaction in the Coulomb titration process, which cause low determination conclusion .

We can see from the formula of sulfur dioxide and sulfur trioxide, this reaction is an exothermic reaction, the temperature rises will move toward the production of sulfur dioxide, so we should make the direction of the reaction to the reaction of sulfur dioxide and oxygen as far as possible In order to get accurate measurement results. The measurement results can be more accurate by the above two factors that are raising the temperature, but the temperature is too high will shorten the life of the combustion tube, thus, we have to reduce the combustion temperature, but must ensure that the sulfates completely decomposes at a lower temperature, so we cover a layer of catalyst on the coal.

tungsten trioxide effect graphTungsten Trioxide and Coal Principle During Combustion:
The catalyst is able to significantly change the reaction rate and the material, the chemical reaction itself, the chemical nature and quantity can be changed or not is according to the change of free energy, it  can not determine  the reaction occurs only according to the change of free energy, because chemical reaction also depends on the reaction energy barrier, that is, if the reaction energy barrier is high, we must provide the energy to fly over the energy barrier, the energy barrier known as the activation energy after completing the reaction, and the role of the catalyst is to reduce the activation of this reaction You can make it happen chemical reaction at relatively harsh environments.

The catalyst changes the reaction rate, which is due to changes in the reaction pathway, as the picture shows, by the reaction path requires a higher energy barrier is needed to change over the reaction pathway of low energy barrier, reducing the activation energy of the reaction. Tungsten trioxide plays a role of enabling sulphate complete decomposition in coal combustion process at a low temperature, which guarantees accurate measurement results.

 

Sodium Tungstate and SDBS Synergistic Inhibition Effect

Sodium dodecyl benzene sulfonate (“SDBS”for short) is white or light yellow powder or flake solid. It’s difficult to volatilize and soluble in water. It becomes translucent solution in water. Its chemical property is stable for the alkali, dilute acid and hard water. It’s mainly used as anionic surfactants. 
 
sodium dodecyl benzene sulfonate
Corrosion inhibitor is a kind of chemical substances which can prevent or slow down the corrosion or a mixture of several chemicals and when it exists in the environment in the appropriate concentration and forms. In general, corrosion inhibitors are those used in metal surface protection material. Adding trace or a small amount of such chemicals can make the corrosion speed of metal materials in the medium obviously decrease to zero. At the same time, it also can maintain the original metal materials of physical and mechanical properties unchanged. Fair use of corrosion inhibitors is the effective method to prevent metals and their alloys to occur corrosion in the environment medium. 
 
In recent years, with the enhancement of human environmental protection consciousness, the development and application of corrosion inhibitors are paying more and more attention to the requirements of environmental protection. And traditional inhibitor often has certain harm to the environment. Because tungstate has low toxicity and no harm to the environment, the human body and crops, nor causes microorganism growth, it is environmental friendly corrosion inhibitors and it has aroused widespread interest of people. Because single tungstate corrosion efficiency is not high and the dosage is bigger, the cost is higher. Thus the synergistic inhibition effect of the composite of sodium tungstate and other corrosion inhibitor has drawn attention of people. Corrosion of cast iron in 3.5% NaCl solution is serious. The composite inhibitor of sodium tungstate and SDBS has good synergistic inhibition effect by studied by immersion test, method of weight loss and polarization curves.
 
Through these methods we can draw the conclusions:
(1) In 3.5% NaCl solution, when adding sodium tungstate inhibitor alone and the mass fraction is 0.5%, the cast iron corrosion effect is best and the corrosion rate can reach 82.5%. When adding sodium dodecyl benzene sulfonic alone and the mass fraction is 0.9%, cast iron corrosion effect is best and the corrosion rate can reach 67.5%.
(2) The corrosion effect on cast iron of the composite corrosion inhibitor composed of 0.2%mass fraction sodium tungstate and 0.1% mass fraction sodium dodecyl benzene sulfonic is best. The corrosion rate can reach 91.3%. It has good synergistic inhibition effect. At the same time, it can reduce the dosage of sodium tungstate and SDBS.

 

Sodium Tungstate Catalyzes Cyclohexanone to Synthesize Adipic Acid

Cyclohexanone is the organic compound and the carbonyl carbon atoms included in saturated cyclic ketone in the six-member ring. It’s colorless transparent liquid with earthy. When it contains trace amount of phenol, it has the flavor of mint. Impurity content is light yellow and with storage time impurities generated. In water it becomes white to yellowish gray with strong pungent odor. Mixed with air blast extremely is the same as the open chain saturated ketones. Cyclohexanone is mainly used as organic synthetic raw material and solvent in industry, for example it can dissolve cellulose nitrate and paint. 
 

adipic acid

Adipic acid is also known as fatty acid and is a kind of important organic dibasic acid. It can occur as salt reaction, esterification and amidation reaction. And it can be condensed into a polymer with diamine or glycol. Adipic acid is binary carboxylic acid industry of important significance in industry and also plays an important role in such aspects as chemical industry, medicine production, organic synthesis and lubricant manufacturing. Its production is in the second place in all binary carboxylic acid.
 
The main production method of adipic acid is nitric acid oxidation method which takes a mixture of cyclohexanol and cyclohexanone as raw materials,or two steps of cyclohexane oxidation. Yield and selectivity are high, but the equipment corrosion is serious. Therefore, by improving production process to develop new catalytic system, improve the reaction selectivity and the development of atom economy reaction, using non-toxic harmless raw materials under the non-toxic harmless reaction conditions to produce adipic acid is the diligent direction of the related departments of scientific research workers. Compared with the traditional oxidant, hydrogen peroxide is a kind of green oxidants and clean oxidant.
 
Here is the experiment method of sodium tungstate catalyzing cyclohexanone to synthesize of adipic acid: 30% hydrogen peroxide (H2O2) as oxidant, sodium tungstate as catalyst, clean and catalyze oxidation
cyclohexanone to synthesize adipic acid in the presence of various ligands. Early experiments in situ synthesize tungstate--organic peroxide coordination complex catalyst. Without organic solvent, the product can be obtained by simple phase separation after reaction. at the same time, because of mild reaction condition, it’s easy to operate and does not produce toxic or harmful by-products.
 
Through this method we can draw the conclusions as follows: using sodium tungstate as catalyst, acid reagent as the ligand, the reaction of sodium tungstate catalyzing cyclohexanone to synthesize of adipic acid has obtained the good effect. Its oxidation condition is mild and the reaction is easy to control. All the reaction is clean and non-pollution which conforms to the requirements of the current green synthesis.
 

Sodium Tungstate Preparing Pyrochlore Type Tungsten Oxide

The chemical formula of pyrochlore type tungsten oxide is  H2W2O7. Pyrochlore type tungsten oxide has recently found its wide applications in many different areas such as photoelectron-chemistry, functional material and sensing. In addition, pyrochlore type tungsten oxide can be used as intermediate product for the industrial production of WO3. There are many kinds of synthesis methods of the pyrochlore type tungsten oxide. And there are two main types: Aurivillius type compound as precursor, pyrochlore type tungsten oxide is obtained by acid treatment. The second method is hydrothermal synthesis method, namely sodium tungstate solution acidification to a certain pH range and it can be obtained by hydrothermal reaction for a certain time. The hydrothermal method that has overwhelming superiorities than others also has its own sets of flaws such as high cost, long reaction time and low quality product. Therefore, how to intensify the preparation process of H2W2O7 to obtain high quality product with low cost has become an urgent problem.
 
In this article, XRD, TGA-DSC, and SEM were used to characterize the products. The sodium content in the H2W2Ois
determined by chemical analysis and most sodium could be removed by ion exchange method. 
The main research results are listed as follows.
 
(I)The seeded precipitation and salting-out precipitation methods are not appropriate to prepare H2W2O7 but salting-out precipitation method suggests a new way to prepare Na2WO4 and Na2W2O7.
(2)Under hydrothermal conditions, the addition of oxalic acid has its optimum value. When C (Na2WO4) =150g/L, T=126℃, t=11h, adding oxalic acid 65g/L, the reaction ratio reaches its peak value 91%. Additive C plays a part in reaction ratio and seeds of H2W2O7 could accelerate reaction rate. TheW7O246- ions may be the precursor in precipitating H2W2O7, but theFe2+ ions seem to change the precipitation mechanism.            
(3)The TGA-DSC curve shows a continuous water loss from ambient t0 450℃, and the H2W2O7 remains stable under 340℃. The SEM pictures of theH2W2O7 exhibit cubic morphology which can be changed by organic surfactant.
(4)Sodium is an inevitable impurity with its content varying from 3.3% to 4.9%, and ion exchange is a valid way to remove sodium content to about 0.3%.

 

 

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