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Visual Colorimetric Analysis for Niobium Content of the Potassium Fluotantalate

Rare Metals and Cemented Carbides | Vol., Issue 2, 2003 | pp. 31-32
Nb2O5 liquor is added into the Ta2O5 to form standard solution,then carry out chromatographic separating on paper after series of treatment with potassium fluotantalate sample parent solution.Finally directly take visual colorimetric analysis with sample by this method.The standard error and relative error and is 0.000 104% and 5.5%,respectively recovery is 97%~103%.It is applicable for the sample containing niobium 0.001~0.0x%.
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Development and Application of HIP Technology

Rare Metals and Cemented Carbides | Vol., Issue 2, 2003 | pp. 33-38
Based on the review of development history of HIP technology and equipment,overall description is made of the improvement of the cast product quality and development of applications into the new materials such as high-speed speel,double-refined steel and super-double refined steel,high-performance ceramics.It is expected that the annual increase of HIP application will be 15%~20%in the next few years and its annual application in Al processing will be 25%.
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Improvement of Na Reduction Process of Low-oxide Ta Powder in Large Reactor

Rare Metals and Cemented Carbides | Vol., Issue 2, 2003 | pp. 39-41
The paper describes the study and improvement of Na reduction process of low-oxide Ta powder in D700mm large reactor.The results showed that the improved process has basically solved the problem of the control of process parameters and operation problem.The oxygen content in the resultant Ta powder can be controlled at about 1%.
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Large-capacity H_2 Pressure Recovery Equipment from H_2-Reduction Furnance for W/Mo Production

Rare Metals and Cemented Carbides | Vol., Issue 2, 2003 | pp. 42-44
Brief description is made of the present status of equipment for excess H2 high-pressure and pressure recovery from reduction furnace.It focused on the operating process and characteristics of the first large capacity H2 pressure recovery equipment from reduction furnace.The said equipment is characterized by large capacity,advanced technology,PLC fully-automatic operation control.Through operating practice,the main technical specificatioms have met the design requirement.
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The Progress on Improving the Performance of Ceramic Liner of SHS Ceramic Composite Pipe

Rare Metals and Cemented Carbides | Vol., Issue 2, 2003 | pp. 45-48
A combination of the SHS method and centrifugal process is investigated to produce a composite pipe by coating a ceramic liner on inner surface of common carbon steel pipe.The ceramic-lining pipes are characterized by simple process and equipment,high productivity,energy-saving performance and low cost,providing a new approach for the ceramic composite pipe production.The performances of SHS composite pipes depend on ceramic-liner,The paper summarizes the ways for the improvement of the performances of SHS composite pipes with respect of increasing densification and corrosive resistance,improving toughness,and decreasing crack ratio.
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Recovery of Molybdenum from Copper and Molybdenum Middlings by High-pressure Oxygen Digestion-extraction

Rare Metals and Cemented Carbides | Vol., Issue 1, 2003 | pp. 1-3
Recovery of molybdenum from copper and molybdenum middlings has been studied.The main steps are as follows:NaOH hi-pressure oxygen digestion to enable Mo to enter the solution in the form of sodium molybdate with Cu remaining in the residues,which can be used as raw matcrial for Cu recovery.Mo is recovered by extraction from Mo-containrng solution.It is shown that,under given conditions,the recovery of molybdenum and copper is 95.6% and 99% respectively.
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Study on Recovery of Sulfuric Acid from TiO_2 Hydrolysis Waste Acid by Solvent Extraction

Rare Metals and Cemented Carbides | Vol., Issue 1, 2003 | pp. 4-7
Study is made of the process extraction of sulfuric acid from TiO2 hydrolysis waste acid with tri-isoctylamine as extractant and H2O as stripping reagent.Investgation is made on the impaction of extractant concentration,phase modifier concentration,phase ratio and temperature on the extraction and stripping.Simulation test is made.The results showed that under given condition,the H2SO4 recovery can reach 91.8% and acid concentration in the product is 119.73 g/L.
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