Method and system for regeneration and recovery of glass thinning waste acid solution
A waste acid liquid thinning technology, applied in chemical instruments and methods, silicon oxide, fluosilicic acid, etc., can solve problems such as high processing costs, generation of potassium fluoride, insufficient recycling of waste discharge resources, etc., to achieve The effect of high recovery efficiency, realization of recycling and low treatment cost
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Embodiment 1
[0092] A method for regeneration and recovery of glass thinning waste acid solution, comprising:
[0093] Add 1000kg of waste acid liquid into the stirred reactor, and turn on the condenser (control the cooling temperature -5°C) (the condensation temperature can be selected from -15 to 19°C, and the better range is -10 to -5°C). Slowly and uniformly add 1850kg of 95% concentrated sulfuric acid into the stirred reactor, and stir while adding. It escapes in the form of gas; the output of hydrofluoric acid after passing through the condensation tower and refining tower is 113.8kg.
[0094] Uncondensed gas enters BF 3 Absorption Tower, BF 3 The gas is absorbed by ether into a liquid, and becomes a boron trifluoride-ether complex, which can be sold as a product. Moreover, the boron trifluoride-ether complex is analyzed and refined to obtain boron trifluoride gas; the auxiliary agent ether can be recycled. Boron trifluoride gas is absorbed by ice water into boron trifluoride dih...
Embodiment 2
[0100] A method for regeneration and recovery of glass thinning waste acid solution, comprising:
[0101] Add 1000kg of fluorine-containing waste acid to the stirred reactor, turn on the condenser (control the cooling temperature -5°C); slowly and uniformly add 1000kg of 95% concentrated sulfuric acid into the stirred reactor, stir while adding, the temperature of the reactor is displayed as 110 ℃, pressure 0.1-0.3MPa, reaction time 1 hour; hydrogen fluoride, silicon tetrafluoride, silicon tetrafluoride, and boron trifluoride escape in the form of gas; the output of hydrofluoric acid after passing through the condenser and refining tower is 108.2 kg.
[0102] Uncondensed gas enters BF 3 Absorption Tower, BF 3 The gas is absorbed by methanol into a liquid and becomes a boron trifluoride-methanol complex, which can be sold as a product. Among them, the boron trifluoride-methanol complex is analyzed and refined to obtain boron trifluoride gas; the auxiliary methanol can be rec...
Embodiment 3
[0108] A method for regeneration and recovery of glass thinning waste acid solution, comprising:
[0109] Add 1000kg of fluorine-containing waste acid to the stirred reactor, turn on the condenser (control the cooling temperature -5°C); slowly and uniformly add 4000kg of 95% concentrated sulfuric acid into the stirred reactor, stir while adding, the temperature of the reactor is displayed as 115 ℃, pressure 0.4-0.6MPa, reaction time 1 hour; hydrogen fluoride, silicon tetrafluoride, silicon tetrafluoride, and boron trifluoride escape in the form of gas; the output of hydrofluoric acid after passing through the condenser and refining tower is 82.3 kg.
[0110] Uncondensed gas enters BF 3 Absorption Tower, BF 3 The gas is absorbed by butyl acetate into a liquid and becomes boron trifluoride-butyl acetate complex, which can be sold as a product. Among them, the boron trifluoride-butyl acetate complex is analyzed and refined to obtain boron trifluoride gas; the additive butyl ac...
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Abstract
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