A device and method for efficiently recovering dmf from wastewater
A waste water and high-efficiency technology, applied in organic chemistry, carboxylic acid amide separation/purification, etc., can solve the problems of affecting the use of recycled DMF, low DMF recovery rate, and high formaldehyde content, achieving low cost, high extraction efficiency, and reduction of ammonia nitrogen and nitrogen. Effects of COD Concentration
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Embodiment 1
[0012] like figure 1 As shown, a device for efficiently recovering DMF from wastewater includes reboiler H101a, extraction tower T101, reboiler H101b, static mixer X101, static stratification tank V101, rectification tower T102 and vacuum rectification tower T103; the DMF wastewater containing salt and formaldehyde is used as the light phase F and preheated by the reboiler H101a from the bottom of the extraction tower T101; the extractant is injected as the heavy phase S from the top of the extraction tower T101 after being preheated by the reboiler H101b, The light and heavy phases are countercurrently contacted in the tower for multi-stage extraction; the transfer of DMF from the water phase to the organic phase is completed in the extraction tower T101, the raffinate phase R is extracted from the top of the extraction tower T101, and the extraction phase E containing DMF is extracted from the extraction tower T101 Extracted from the bottom; the extract phase and water enter...
Embodiment 2
[0014] The present invention also provides a kind of efficient recovery DMF method from waste water, comprises the following steps:
[0015] Step 1: DMF waste water containing salt and formaldehyde is taken as light phase F and preheated through reboiler H101a and enters from the bottom of extraction tower T101;
[0016] Step 2: The extractant is injected as the heavy phase S from the top of the extraction tower T101 after being preheated by the reboiler H101b, and the light and heavy phases are countercurrently contacted in the tower for multi-stage extraction;
[0017] Step 3: Complete the transfer of DMF from the aqueous phase to the organic phase in the extraction tower T101, the raffinate phase R is extracted from the top of the extraction tower T101, and the extraction phase E containing DMF is extracted from the bottom of the extraction tower T101;
[0018] Step 4: The extraction phase and washing water enter the static mixer X101 according to a certain volume ratio, an...
Embodiment 3
[0030] On the basis of above-mentioned embodiment, further specifying, the stage number of extraction tower T101 is 10, and rotating speed 45r / min, rectifying tower T102 plate number is 30, and T103 plate number is 20, and the content of DMF in the DMF waste water is 10 %, containing 2.4% formaldehyde, 5% salt, the temperature entering the extraction tower T101 is 40°C, the two-phase volume ratio of the extractant / raw wastewater is 2.0, the temperature of the extractant entering the tower is 30°C, and the extracted from the top of the extraction tower The raffinate phase was analyzed by high-efficiency gas chromatography. The content of water was 91.20%, the content of DMF was 0.12%, the content of dichloromethane was 1.15%, the content of formaldehyde was 2.12%, and the content of salt was 5.4%. The extraction efficiency of the extraction tower was 98.8%. The washing water enters the static mixer X101 according to 20% of the volume of the extraction phase and mixes it into the...
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