A method for resource utilization of glue clear wastewater
A technology for cleaning waste water and reusing glue, applied in organic chemistry, ether separation/purification, ether preparation, etc., can solve the problems of difficult recovery of membrane fouling flux, unstable product quality, high cost of membrane replacement, etc., and meet the load of subsequent processes Small size, stable product quality, and excellent product quality
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Embodiment 1
[0027] Take fresh natural rubber latex from the rubber factory after centrifugation, and filter it through an alumina microfiltration membrane. The average pore size is 200nm, the transmembrane pressure difference is 0.1MPa, and the membrane surface flow rate is 1m / s. The wastewater is concentrated to obtain 1L of concentrated liquid and 9L of microfiltration permeate, and then the microfiltration permeate is sent to a zirconia ultrafiltration membrane for filtration. The average pore size of the ultrafiltration membrane is 20nm and the transmembrane pressure difference is 0.3MPa. The membrane surface flow rate is 2m / s, and ultrafiltration permeate is obtained.
[0028] The ultrafiltration permeate is then sent to a medium-polarity resin column (column volume 2L) with a flow rate of 1BV / h. After processing, it is eluted with 50% methanol (2L). The eluent is collected, filtered and distilled under reduced pressure to obtain 200g concentration. After standing at 0℃ for 24 hours, th...
Embodiment 2
[0032] Take fresh natural rubber latex from the rubber factory after centrifugation, and filter it through the alumina microfiltration membrane. The average pore size is 200nm, the transmembrane pressure difference is 0.5MPa, and the membrane surface flow rate is 1m / s. The wastewater is concentrated to obtain 1L of concentrated liquid and 9L of microfiltration permeate, and then the microfiltration permeate is sent to a zirconia ultrafiltration membrane for filtration. The average pore size of the ultrafiltration membrane is 20nm and the transmembrane pressure difference is 0.3MPa. The membrane surface flow rate is 2m / s, and ultrafiltration permeate is obtained.
[0033] The ultrafiltration permeate is then sent to a medium-polarity resin column (column volume 2L) with a flow rate of 1BV / h. After processing, it is eluted with 50% methanol (2L). The eluent is collected, filtered and then distilled under reduced pressure to obtain 200g concentration. After standing at 0℃ for 24h, t...
Embodiment 3
[0037] Take fresh natural rubber latex from the rubber factory after centrifugation, and filter it through an alumina microfiltration membrane. The average pore size is 50nm, the transmembrane pressure difference is 0.1MPa, and the membrane surface flow rate is 1m / s. Concentrate the wastewater to obtain 1L of concentrated liquid and 9L of microfiltration permeate. Adjust the pH of the microfiltration permeate to about 3.0~4.0, and then send it to the zirconia ultrafiltration membrane for filtration. The average pore size of the ultrafiltration membrane is 20nm , The transmembrane pressure difference is 0.3MPa, and the membrane surface flow rate is 2m / s to obtain ultrafiltration permeate.
[0038] The ultrafiltration permeate is then sent to a medium-polarity resin column (column volume 2L) with a flow rate of 1BV / h. After processing, it is eluted with 50% methanol (2L). The eluent is collected, filtered and then distilled under reduced pressure to obtain 200g concentration. The c...
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