Method for producing nanosilicon dioxide and by-product hydrochloric acid through chlorosilane waste gas
A technology of nano-silica and by-product hydrochloric acid, which is applied in the direction of silica, silicon oxide, nanotechnology, etc., can solve the problems of secondary pollution, failure of resource utilization, and low value of resource utilization, etc., and achieve reduction The cost of waste gas treatment, reducing the pressure of sewage treatment, and realizing the effect of resource utilization
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Embodiment 1
[0032] A kind of chlorosilane exhaust gas described in this embodiment produces the method for nano silicon dioxide and by-product hydrochloric acid (such as figure 1 shown), including the following steps:
[0033] (1) Gas vapor contact hydrolysis reaction: put 1000m 3 / h of chlorosilane waste gas (15% SiCl 4 , 20% SiHCl 3 , 10% SiH 2 Cl 2 , 5% HCl, 5% H 2 , 45% N 2 ) and 145m 3 / h of water vapor (temperature: 120°C pressure: 2kgf / cm 2 ) into gas-steam hydrolysis reaction tower 1 at the same time, chlorosilane waste gas is hydrolyzed in gas-steam hydrolysis reaction tower 1 filled with water vapor, and the generated silica solid enters the gas-solid separation equipment together with the air flow, and the temperature of gas-steam hydrolysis reaction tower 1 Control at 130~140°C.
[0034] (2) Gas-solid separation: Chlorosilane waste gas and water vapor hydrolysis products enter the gas-solid separator 2, the temperature of the solid-liquid separator 2 is kept at 130~14...
Embodiment 2
[0039] A kind of chlorosilane exhaust gas described in this embodiment produces the method for nano silicon dioxide and by-product hydrochloric acid (such as figure 1 shown), including the following steps:
[0040] (1) Gas vapor contact hydrolysis reaction: put 1000m 3 / h of chlorosilane waste gas (10% SiCl 4 , 30% SiHCl 3 , 15% SiH 2 Cl 2 , 5% HCl, 5% H 2 , 35% N 2 ) and 186m 3 / h of water vapor (temperature: 140°C pressure: 4kgf / cm 2 ) into gas-steam hydrolysis reaction tower 1 at the same time, chlorosilane waste gas is hydrolyzed in gas-steam hydrolysis reaction tower 1 filled with water vapor, and the generated silica solid enters the gas-solid separation equipment together with the air flow, and the temperature of gas-steam hydrolysis reaction tower 1 Control at 150~160°C.
[0041] (2) Gas-solid separation: Chlorosilane waste gas and water vapor hydrolysis products enter the gas-solid separator 2, the temperature of the solid-liquid separator 2 is kept at 150~16...
Embodiment 3
[0046] A kind of chlorosilane exhaust gas described in this embodiment produces the method for nano silicon dioxide and by-product hydrochloric acid (such as figure 1 shown), including the following steps:
[0047] (1) Gas vapor contact hydrolysis reaction: put 1000m 3 / h of chlorosilane waste gas (5% SiCl 4 , 40% SiHCl 3 , 20% SiH 2 Cl 2 , 10% HCl, 5% H 2 , 20% N 2 ) and 229m 3 / h of water vapor (temperature: 160°C pressure: 6kgf / cm 2 ) into gas-steam hydrolysis reaction tower 1 at the same time, chlorosilane waste gas is hydrolyzed in gas-steam hydrolysis reaction tower 1 filled with water vapor, and the generated silica solid enters the gas-solid separation equipment together with the air flow, and the temperature of gas-steam hydrolysis reaction tower 1 Control at 180~190°C.
[0048] (2) Gas-solid separation: Chlorosilane waste gas and water vapor hydrolysis products enter the gas-solid separator 2. The temperature of the solid-liquid separator 2 is kept at 180~19...
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