A kind of stripping equipment and method of supporting molybdenum tfa organic phase
An extraction equipment and organic phase technology, applied in the field of stripping, can solve the problems of emulsification interface, signal lag, easy damage of acid-base balance, etc., achieve the effect of stable reaction state, stable control interface, and saving transition acid consumption
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example 1
[0074] The side length of the mixing chamber is 400mm, the side ratio of the mixing chamber and the clarification chamber is 1:3, 4-stage (n1=4) back extraction, 2-stage (n2=2) countercurrent washing. Molybdenum-containing tri-fatty amine (7.5% TFA+15% TBP) kerosene solution, molybdenum concentration 10.0g / L, organic phase flow rate is 10L / min, is added from the mixing chamber in the first stage of stripping, lotion flow rate is 1L / min, from the washing The final mixing chamber joins. Add ammonia from the pre-mixing chamber, adjust the amount of ammonia added to control pH1=10; adjust the reflux adjustment device to control the contact ratio in the mixing chamber; adjust the interface control device to control the stability of the interface; adjust the speed of the stirring paddle to control the appropriate stirring intensity . The reaction temperature was 25°C. The stripping solution with a molybdenum concentration of 100g / L can be obtained; the molybdenum concentration of ...
example 2
[0076] The side length of the mixing chamber is 500mm, the side ratio of the mixing chamber and the clarification chamber is 1:2, 4-stage (n1=3) back extraction, 3-stage (n2=3) countercurrent washing. Molybdenum-containing tri-fatty amine (7.5% TFA+15% TBP) kerosene solution, molybdenum concentration 10.0g / L, organic phase flow rate is 20L / min, add from the mixing chamber in the first stage of stripping, lotion flow rate is 1L / min, from the washing The final mixing chamber joins. The concentrated ammonia water is added from the pre-mixing chamber, the flow rate of the concentrated ammonia water is approximately 1L / min, and the amount of concentrated ammonia water added is fine-tuned to control pH1=10.5; the reflux adjustment device is adjusted to control the contact ratio in the mixing chamber; the interface control device is adjusted to control the stability of the interface; Adjust the speed of the stirring paddle to control the proper stirring intensity. The reaction tempe...
example 3
[0078]The side length of the mixing chamber is 400mm, the side ratio of the mixing chamber and the clarification chamber is 1:3, 4-stage (n1=4) back extraction, 4-stage (n2=4) countercurrent washing. Molybdenum-containing tri-fatty amine (7.5% TFA+15% TBP) kerosene solution, molybdenum concentration 10.0g / L, organic phase flow rate is 13L / min, is added from the mixing chamber in the first stage of stripping, lotion flow rate is 1L / min, from the washing The final mixing chamber joins. Add ammonia gas from the pre-mixing chamber, adjust the amount of ammonia added to control pH1=10.8; adjust the reflux adjustment device, control the contact ratio in the mixing chamber; adjust the interface control device, control the stability of the interface; adjust the speed of the stirring paddle, and control the appropriate stirring intensity . The reaction temperature was 25°C. The stripping solution with a molybdenum concentration of 130g / L can be obtained; the molybdenum concentration ...
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