Method for preparing silicon tetrafluoride from phosphorus ore accompanied with fluorine
A technology of silicon tetrafluoride and water-containing silicon tetrafluoride, applied in the field of phosphorus chemical industry, can solve problems such as by-product fluorosilicate, and achieve the effects of reducing output, reducing manufacturing cost and reducing consumption
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Embodiment 1
[0043] Mix 410kg 90wt% sodium fluorosilicate (water content 10%), 540kg water, 60kg quartz sand into a slurry, slowly add 1360kg washing sulfuric acid (95wt%), react for 90min, the system exothermic violently to obtain hydrous silicon tetrafluoride Crude gas; washed and dehydrated by 1360kg of hot concentrated sulfuric acid (98wt%, 160°C) to obtain anhydrous silicon tetrafluoride gas, cooled to -18°C, and then pressurized to 0.2MPa, into the refined Distillation tower 1 extracts uncondensed silicon tetrafluoride gas from the top of the tower, then further cools to -70°C, pressurizes to 0.5 MPa, enters rectification tower 2, and extracts silicon tetrafluoride gas from the bottom of the tower. The recovery rate of fluorine was 94.3%.
Embodiment 2
[0045] Mix 210kg 90wt% sodium fluosilicate (water content 10%), 1000kg 12wt% fluosilicic acid and 70kg phosphoric acid production tail wash silica gel into a slurry, slowly add 2213kg washing sulfuric acid (95wt%), react for 60min, the system is violent Release heat to obtain crude silicon tetrafluoride gas containing water; wash and dehydrate with 2210kg hot concentrated sulfuric acid (98wt%, 90°C) to obtain anhydrous silicon tetrafluoride gas, cool the anhydrous silicon tetrafluoride gas to -5°C, and then Pressurize to 0.3MPa, enter rectification tower 1, extract uncondensed silicon tetrafluoride gas from the top of the tower, then further cool to -80°C, pressurize to 0.45MPa, enter rectification tower 2, and extract from the bottom of the tower silicon tetrafluoride. The recovery rate of fluorine was 92.8%.
Embodiment 3
[0047] Mix 288 kg 90wt% potassium fluosilicate (water content 10%), 1160kg 8wt% fluosilicic acid and 80kg diatomaceous earth into a slurry, slowly add 2692kg washing sulfuric acid (95wt%), react for 30min, and the system decomposes violently heat to obtain crude silicon tetrafluoride gas containing water; wash and dehydrate with 2700kg hot concentrated sulfuric acid (98%, 120°C) to obtain anhydrous silicon tetrafluoride gas, cool the anhydrous silicon tetrafluoride gas to -20°C, and add Pressure to 0.1MPa, enter rectification tower 1, extract uncondensed silicon tetrafluoride gas from the top of the tower, then further cool to -40°C, pressurize to 0.6MPa, enter rectification tower 2, and extract from the bottom of the tower Silicon tetrafluoride. The recovery rate of fluorine was 91.4%.
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