A device and method for enhancing liquid-liquid extraction
An enhanced liquid and extraction technology, applied in the field of liquid-liquid extraction, can solve the problems of low extraction efficiency, large amount of extraction phase, and large volume, and achieve the effect of high extraction efficiency, small amount of extraction agent, and small volume
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Embodiment 1
[0033] figure 1 It is the device for strengthening liquid-liquid extraction of the present invention, and the device for strengthening liquid-liquid extraction includes injection part 1 and the mixed extraction part 2 that is connected with described injection part 1, and described injection part 1 includes for extracting feedstock The feed tee 11, the feed tee 11 includes a first port 111, a second port 112 and a third port 113, wherein the first port 111 is used for the feed of the extracted phase, and the second port 112 is provided with a The injector 12 is used for compressing and shearing the extraction phase to generate turbulent kinetic energy, which is injected into the feed tee 11 through the injector 12, and is used for initially mixing the extracting phase and the extracted phase; the initially mixed extracting phase and The extracted phase enters the mixed extraction part 2 through the third port 113; the mixed extraction part 2 includes a mixer 21, and the mixer ...
Embodiment 2
[0048] A chemical plant uses extraction tower technology to sweeten liquefied hydrocarbons. The extraction tower is a sieve tray tower with a diameter of 1m and a height of 15m. Alkaline phenomenon. The device and method of Example 1 are used to replace liquefied hydrocarbon sweeteners, wherein the injection part adopts a single injector, the overall length of the mixer in the mixed extraction part is 2m, and the number of mixing stages is 2, using 5 as described in Example 1. Parallel processing of the device, the processing capacity can reach 25m 3 / h.
[0049] After transformation, the output of liquefied hydrocarbon sweetening has increased from 140,000 tons / year to 200,000 tons / year, and the imported mercaptan content is 2000-2500mg / m 3 liquefied hydrocarbons, the mercaptan content in the liquefied hydrocarbons after the original process is 200mg / m 3 , the content of mercaptans in liquefied hydrocarbons is 50 mg / m3 after modification 3 , to meet the treatment requirem...
Embodiment 3
[0051] In this example, the device and method described in Example 1 are used to extract ferric ions in the aqueous solution, wherein the extraction phase is an extractant prepared by mixing diphosphonate and sulfonated kerosene in a ratio of 3:7, and the extracted phase is Aqueous solution of ferric chloride, in which Fe 3+ The concentration was 100 mg / L, and the pH was adjusted to 1.86. The injection part adopts a single injector, the overall length of the mixer in the mixing extraction part is 60mm, the number of mixing stages is 3, and the processing capacity can reach 1m 3 / h.
[0052] Maintain the flow ratio of the extracted phase and the extracted phase at 10:1, investigate the extraction effect under different flow rates of the extracted phase, and measure the residual Fe in water 3+ Concentration evaluates the extraction effect, the results are shown in the table below, with the increase of the flow rate of the extracted phase, the extraction efficiency gradually in...
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