Air assisted solvent extraction method and equipment
An extraction equipment and gas-assisted technology, applied in the direction of liquid solution solvent extraction, etc., can solve the problems of difficult dispersion of extraction solvent, secondary pollution of raffinate phase, loss of extraction solvent, etc., achieve high practical value, strengthen extraction and separation, and promote full mixed effect
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Embodiment 1
[0020] Embodiment 1 is the making of the equipment used for a kind of gas-assisted solvent extraction method:
[0021] As shown in Figure 1, the present invention provides a kind of equipment used in gas-assisted solvent extraction method, mainly comprises gas-assisted mixed reduction extraction zone 4, gas-assisted enhanced extraction zone 5, three-phase flaring separation zone 9, gas distributor 2,3 , it is characterized in that, the gas distributor 2 and 3 and the heavy phase outlet 1 are arranged in the lower part of the gas-assisted mixed-reduction extraction zone 4, and the extraction agent inlet 21 is set in the upper part; the moving parts (sieve plate or turntable) are set in the gas-assisted enhanced extraction zone 5 6) and the drive shaft 7, which are driven by the driving device 13 on the top of the equipment, and the heavy phase inlet 8 is set on the top; the three-phase flare separation area 9 is provided with an inner bubble flare channel 10, which is placed in ...
Embodiment 2
[0025] Embodiment 2, butyl acetate aqueous solution-kerosene system
[0026] With the gas-assisted solvent extraction equipment made in Example 1, the butyl acetate aqueous solution of 0.53v% enters the gas-assisted enhanced extraction zone 5 from the heavy phase inlet 8 at a flow rate of 100ml / min, and the kerosene without butyl acetate enters the gas-assisted enhanced extraction zone 5 at a flow rate of 4ml / min. The flow rate enters the gas-assisted enhanced extraction zone 5 from the solvent phase inlet 21, and the ratio is 25:1, the two-phase countercurrent operation, the vibration frequency is 4.5 Hz, and the amplitude is 0.5 cm. The nitrogen in the compressed steel cylinder passes through the inlet pipe 2 and the gas distribution The device 3 enters the gas-assisted mixed reduction extraction zone 4. When there is no gas-assisted, that is, the gas flow rate is zero, the content of butyl acetate in the aqueous phase of the tower after 50 minutes of operation is 0.15v%, and...
Embodiment 3
[0027] Embodiment 3, the waste acid water-nonane system containing butyl acetate discharged in the production of penicillin
[0028] With the gas-assisted solvent extraction equipment made in Example 1, the flow of 75ml / min of waste acid water containing butyl acetate discharged in the production of 0.38v% penicillin enters the gas-assisted enhanced extraction zone 5 from the heavy phase inlet 8, and does not contain butyl acetate Ester nonane enters the gas-assisted enhanced extraction zone 5 from the solvent phase inlet 21 at a flow rate of 2.5ml / min, the ratio of the two is 30:1, two-phase countercurrent operation, vibration frequency 4.5 Hz, amplitude 0.5cm, compression cylinder Nitrogen enters the gas-assisted mixing reduction extraction zone 4 through the inlet pipe 2 and the gas distributor 3. When there is no gas-assisted, that is, the gas flow rate is zero, the butyl acetate content in the tower waste acid water after 40 minutes of operation is 0.13v%, and the extracti...
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