Hydrogen peroxide extraction process with side column
A side column, hydrogen peroxide technology, applied in the field of extraction technology, can solve the problems of small mass transfer driving force, low tray efficiency, low two-phase mass transfer rate, etc., to improve the mass transfer driving force, simple process flow, and good extraction effect. Effect
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Embodiment 1
[0033] Hydrogen peroxide extraction process with side tower, for 100% operating load, oxidizing liquid flow rate is 40m 3 / h, the flow rate of pure water in the extraction tower is 0.8 m 3 / h, at this time, the side line is drawn out to enter the side line tower, and the amount of side line drawn is 4m 3 / h, after the second enhanced extraction, it will be recycled back to the original extraction tower, and the flow rate of pure water added to the top of the side line tower will be 0.15m 3 / h, after this process, the concentration of hydrogen peroxide at the bottom of the extraction tower is 30wt% to 33wt%, and the residual hydrogen peroxide content in the raffinate at the top of the extraction tower is 0.1g / L to 0.25g / L.
Embodiment 2
[0035] Hydrogen peroxide extraction process with side line tower, when operating at 80% load, the flow rate of oxidizing liquid is 32m 3 / h, the flow rate of pure water in the extraction tower is 0.64m 3 / h, at this time, the side line is drawn out to enter the side line tower, and the amount of side line drawn is 12m 3 / h, after the secondary enhanced extraction, it is recycled back to the original extraction tower, and hydrogen peroxide (concentration: 0.05wt%) is added to the top of the side line tower with a flow rate of 0.32m 3 / h, after this process, the concentration of hydrogen peroxide at the bottom of the extraction tower is 27.5wt% to 29wt%, and the residual hydrogen peroxide content in the raffinate at the top of the extraction tower is 0.2g / L to 0.25g / L; when the operating load increases to 135% When the flow rate of the oxidizing solution is 54m 3 / h, the flow rate of pure water in the extraction tower is 1.1m 3 / h, the amount of side line extraction is increas...
Embodiment 3
[0037] Hydrogen peroxide extraction process with side line tower, when operating at 80% load, the flow rate of oxidizing liquid is 32m 3 / h, the flow rate of pure water in the extraction tower is 0.64m 3 / h, at this time, the side line is drawn out to enter the side line tower, and the amount of side line drawn is 12m 3 / h, after the secondary enhanced extraction, it is recycled back to the original extraction tower, and hydrogen peroxide (concentration 12wt%) is added to the top of the side line tower with a flow rate of 0.28m 3 / h, after this process, the concentration of hydrogen peroxide at the bottom of the extraction tower is 27.5wt% to 28.5wt%, and the residual hydrogen peroxide content in the raffinate at the top of the extraction tower is 0.2g / L to 0.25g / L; when the operating load increases to 135 %, the flow rate of the oxidizing solution is 54m 3 / h, the flow rate of pure water in the extraction tower is 1.1m 3 / h, the amount of side line extraction is increased ...
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