Production method of electronic-grade sulphuric acid
A sulfuric acid production, electronic-grade technology, applied in chemical instruments and methods, sulfur compounds, inorganic chemistry, etc., can solve the problems that sulfuric acid is difficult to reach electronic-grade standards and high energy consumption
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Embodiment 1
[0038] See figure 1 The implementation steps of Example 1 are as follows:
[0039] 1): Provide industrial grade sulfur trioxide raw materials into the raw material storage tank;
[0040] 2): Transport the above-mentioned sulfur trioxide raw materials into the evaporation tank with a centrifugal pump;
[0041] 3): Use hot water to heat the evaporation tank, the heating temperature is controlled at 60°C, and the sulfur trioxide vapor generated by heating enters the absorption tower 2 after passing through the first filter 1;
[0042] 4): Use electronic grade ultrapure water to absorb sulfur trioxide vapor in the adsorption tower 2, and adjust the concentration of the absorption solution to 97% ± 0.5% by controlling the flow of sulfur trioxide vapor and the flow of ultrapure water. The temperature of 2 is controlled at 100°C, the absorbed solution is cooled by the first cooler 4 and then enters the degassing tower 7, and the outlet temperature of the first cooler 4 is controlled at 50°C...
Embodiment 2
[0048] See figure 1 , The implementation steps of Example 2 are as follows:
[0049] 1): Provide industrial grade sulfur trioxide raw materials into the raw material storage tank;
[0050] 2): Press the above-mentioned sulfur trioxide raw material into the evaporation tank with nitrogen;
[0051] 3): Use steam to heat the evaporation tank, the heating temperature is controlled at 70°C, and the sulfur trioxide steam produced by heating enters the absorption tower 2 after passing through the first filter 1;
[0052] 4): Use electronic grade ultrapure water to absorb sulfur trioxide vapor in the adsorption tower 2, and adjust the concentration of the absorption solution to 97% ± 0.5% by controlling the flow of sulfur trioxide vapor and the flow of ultrapure water. The temperature of 2 is controlled at 95°C, the absorbed solution is cooled by the first cooler 4 and then enters the degassing tower 7, and the outlet temperature of the first cooler 4 is controlled at 45°C;
[0053] 5): The d...
Embodiment 3
[0058] See figure 1 The implementation steps of Example 3 are as follows:
[0059] 1): Provide industrial grade sulfur trioxide raw materials into the raw material storage tank;
[0060] 2): Transport the above-mentioned sulfur trioxide raw materials into the evaporation tank with a centrifugal pump;
[0061] 3): Electric heating wire is used to heat the evaporation tank, and the heating temperature is controlled at 50°C. The sulfur trioxide vapor generated by heating enters the absorption tower 2 after passing through the first filter 1;
[0062] 4): Use electronic grade ultrapure water to absorb sulfur trioxide vapor in the adsorption tower 2, and adjust the concentration of the absorption solution to 97% ± 0.5% by controlling the flow of sulfur trioxide vapor and the flow of ultrapure water. The temperature of 2 is controlled at 85°C, the absorbed solution is cooled by the first cooler 4 and then enters the degassing tower 7, and the outlet temperature of the first cooler 4 is con...
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