Wheel disk type liquid-liquid extraction tower
An extraction tower and disc-type technology, applied in the field of liquid-liquid extraction tower, can solve the problems of easy clogging holes, industrial application restrictions, complex process flow, etc., achieve convenient operation and maintenance, fast mass transfer speed, and improve extraction efficiency Effect
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Embodiment 1
[0028] In this embodiment, the structure of the disc type liquid-liquid extraction tower is as follows figure 1 , figure 2 shown, including the first clarification stage L 2 , extraction section L 1 , the second clarification section L 3 , power unit 1 and main shaft 2, extraction section L 1 , the first clarification section L 2 and the second clarification section L 3 The shells are all cylindrical, the extraction section is located between the first clarification section and the second clarification section, the power unit 1 is a speed-regulating motor, the upper end of the main shaft is connected with the power output shaft of the speed-regulating motor, and the lower end Through the first clarification section L 2 into the extraction section L 1 Inner cavity, installed in the extraction section L 1 On the support seat 9 provided at the bottom; the first clarification section L 2 The side wall of the housing is provided with a feed liquid inlet 12 and an extract...
Embodiment 2
[0032] In this embodiment, the wheel-type liquid-liquid extraction tower with the structure described in Example 1 is used to extract wet-process phosphoric acid. 16. The combination of raffinate storage tank 17 and two pumps 18 is as follows Image 6 As shown, from the first clarification section L of the extraction tower 2 The feed liquid inlet 12 introduces the feed liquid, from the second clarification section L of the extraction tower 3 The extraction agent inlet 10 introduces the extraction agent, from the first clarification section L of the extraction tower 2 The extraction solution outlet 3 discharges the extraction solution, from the second clarification section L of the extraction tower 3 The raffinate outlet 11 discharges the raffinate.
[0033] In this embodiment, the mass concentration of phosphoric acid in the phosphoric acid feed liquid is 55%, and a mixture of tributyl phosphate and aviation kerosene is used as the extraction agent. The volume ratio of trib...
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