A kind of preparation method of rhenium hexafluoride
A technology of rhenium hexafluoride and nitrogen trifluoride, which is applied in the field of preparation of rhenium hexafluoride, can solve the problems of increased processing costs, difficult removal of impurities, and influence on the purification of rhenium hexafluoride, so as to achieve safe operation process Economical, high industrial application value, and high synthetic conversion rate
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Embodiment 1
[0024] (1) Spread 5g of rhenium powder in the reactor Ⅰ, and the air velocity is 20h -1 ~30h -1 Nitrogen trifluoride gas, the fluorination reaction is carried out at a reaction temperature of 400°C to 430°C and a reaction pressure of 0.15MPa to 0.2MPa, and the product is collected by condenser I, and the nitrogen and nitrogen trifluoride in the product are evacuated The valve is removed, and the rhenium hexafluoride and rhenium heptafluoride in the product are liquefied into mixed solids;
[0025] (2) First heat and sublimate the mixed solid collected in condenser I into a mixed gas, and then -1 ~10h -1 The space velocity is passed into the reactor II equipped with 10g rhenium powder, and the reduction reaction is carried out at a reaction temperature of 100 ° C ~ 120 ° C and a reaction pressure of 0.1 MPa ~ 0.3 MPa, and the product is collected by condenser II. The rhenium hexafluoride gas has a purity of 91.2 wt%.
Embodiment 2
[0027] (1) Spread 5g of rhenium powder in the reactor Ⅰ, and the air velocity is 30h -1 ~50h -1 Nitrogen trifluoride gas, the fluorination reaction is carried out at a reaction temperature of 470°C to 500°C and a reaction pressure of 0.1MPa to 0.12MPa, and the product is collected by condenser I, and the nitrogen and nitrogen trifluoride in the product are evacuated The valve is removed, and the rhenium hexafluoride and rhenium heptafluoride in the product are liquefied into mixed solids;
[0028] (2) First heat and sublimate the mixed solid collected in condenser I into a mixed gas, and then -1 ~10h -1 The space velocity is passed into the reactor II equipped with 10g rhenium powder, and the reduction reaction is carried out at a reaction temperature of 130 ° C ~ 150 ° C and a reaction pressure of 0.3 MPa ~ 0.5 MPa, and the product is collected by condenser II. The rhenium hexafluoride gas has a purity of 95.4 wt%.
Embodiment 3
[0030] (1) Spread 5g of rhenium powder in the reactor Ⅰ, and the air velocity is 30h -1 ~50h -1 Nitrogen trifluoride gas, the fluorination reaction is carried out at a reaction temperature of 440°C to 460°C and a reaction pressure of 0.13MPa to 0.15MPa, and the product is collected by condenser I, and the nitrogen and nitrogen trifluoride in the product are evacuated The valve is removed, and the rhenium hexafluoride and rhenium heptafluoride in the product are liquefied into mixed solids;
[0031] (2) First heat and sublimate the mixed solid collected in condenser I into a mixed gas, and then -1 ~10h -1 The space velocity is passed into the reactor II equipped with 10g rhenium powder, and the reduction reaction is carried out at a reaction temperature of 120°C to 140°C and a reaction pressure of 0.2MPa to 0.4MPa, and the product is collected by condenser II. The rhenium hexafluoride gas has a purity of 92.3 wt%.
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