Method for recycling DMAC from membrane preparation industrial wastewater
A technology for industrial waste water and waste water, applied in the chemical industry, sustainable manufacturing/processing, climate sustainability, etc., can solve the problems of high energy consumption of DMAC, and achieve the effect of reducing energy consumption and high product quality
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Embodiment 1
[0046] In the following implementation example, the wastewater from the membrane industry determines the parameters as the feed situation, the feed flow rate is 2000kg / h, the DMAC content is 5%, the polymer is 1.2%, and the feed is at normal pressure and temperature; the total output at the top of the tower is 1800kg / h, the tower kettle is 200kg / h. The separation goal is: the yield of DMAC in the bottom of the column in the three-effect rectification is 100%.
[0047] The material DMAC waste water F1 enters from 20 plates of the first rectification tower T1 at normal temperature and pressure, and the operating reflux ratio at the top of the tower is 0.18. The tower top of T1 is refluxed, the production liquid is water, and the production volume at the top of the tower is 569kg / h. The bottom of the first rectification tower T1 is a mixture of DMAC and water, and the reflux liquid passes through the first heat exchanger H1 at 57-70 °C is refluxed in the bottom of the tower, th...
Embodiment 2
[0052] In the following implementation example, the wastewater from the membrane industry determines the parameters as the feed situation, the feed flow rate is 2000kg / h, the DMAC content is 15%, the polymer is 1.3%, and the feed is at normal pressure and temperature; the total output at the top of the tower is 1600kg / h, the tower kettle is 200kg / h. The separation goal is: the yield of DMAC in the bottom of the column in the three-effect rectification is 100%.
[0053] The material DMAC waste water F1 enters from the 18 plates of the first rectification tower T1 under normal temperature and pressure, and the operating reflux ratio at the top of the tower is 0.17. The top reflux of T1, the production fluid is water, the production volume at the top of the tower is 506kg / h, the bottom of the first rectification tower T1 is a mixture of DMAC and water, and the reflux liquid passes through the first heat exchanger H1 at 57.6-67.9 °C is refluxed in the bottom of the tower, and th...
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