Method for producing hydrochloric acid and silicon dioxide by using silicon tetrachloride as raw material
A technology of silicon dioxide and silicon tetrachloride, applied in the direction of silicon dioxide, silicon oxide, chlorine/hydrogen chloride, etc., can solve the problems of low utilization value, high production cost, complicated process, etc., and achieve good promotion and application prospects, The effect of low equipment requirements and simple reaction process
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[0020] Example 1
[0021] In this embodiment, the method for producing hydrochloric acid and co-producing silicon dioxide using ceramic balls as the reaction carrier includes the following steps:
[0022] (1) Such as figure 1 As shown, the ceramic balls 3 with a diameter of about 10mm are stacked in the reaction vessel 2, and the mass of the stack is 20kg. The bottom and top of the reaction vessel are respectively provided with inlet and outlet ports 4 and 1;
[0023] (2) Use water to wet the ceramic balls 3 accumulated in the reaction vessel, and the excess water will be discharged from the air inlet at the bottom. figure 2 As shown, there is adhesion water 5 in the contact part between the ceramic balls;
[0024] (3) Take 3kg of silicon tetrachloride, heat it to vaporize and pass it into the reaction vessel from the air inlet at the bottom, and react with the adhering water 5 in the contact part between the ceramic balls to generate silica, which is released at the same time. The ...
Example Embodiment
[0027] Example 2
[0028] The silica production method of this embodiment is the same as that of embodiment 1, the difference lies in image 3 As shown, a water vapor inlet 6 is provided at the bottom of the reaction vessel. While silicon tetrachloride is introduced, water vapor below the reaction amount is introduced to ensure that the silicon tetrachloride is excessive and the silicon tetrachloride enters the reaction vessel. When silicon tetrachloride reacts with water vapor, as silicon tetrachloride reacts with adhering water, all the generated silicon dioxide is finally attached to the reaction carrier, and then through subsequent processing to obtain silicon dioxide, it can improve the reaction of silicon tetrachloride Speed, improve the production efficiency of hydrochloric acid and silica.
[0029] The reaction time of this embodiment is 1 hour, and 0.3 kg of water vapor is injected in total, and finally 6.5 kg of hydrochloric acid (calculated as industrial concentrated hy...
Example Embodiment
[0030] Example 3
[0031] In this embodiment, the method for producing hydrochloric acid and co-producing silicon dioxide using perlite as the reaction carrier includes the following steps:
[0032] (1) Stack 10kg of perlite with an average particle size of 3-5mm in the reaction vessel;
[0033] (2) Wet the perlite accumulated in the reaction vessel with water, and the excess water is discharged from the air inlet at the bottom, and water is stored in the macroporous structure of the perlite after wetting;
[0034] (3) Take 70kg of silicon tetrachloride, heat it to vaporize and pass it into the reaction vessel from the air inlet at the bottom, and react with the water stored in the perlite to generate silica, and at the same time, the released hydrogen chloride is discharged from the reaction vessel The air outlet at the top was discharged and absorbed by a container with a spray device. After 6 hours of reaction, 140kg of hydrochloric acid was obtained (calculated as industrial conc...
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