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Method for preparing nanofiltration membrane with high desalination selectivity and high flux

A selective and high-throughput technology, which is applied in the field of preparation of high desalination selectivity and high-throughput nanofiltration membranes, can solve the problems of nanofiltration membrane performance attenuation, long-term stability of nanofiltration membranes cannot be guaranteed, and increase flux. To achieve the effects of broadening the types and application fields, improving anti-pollution performance, and widening the range of desalination options

Inactive Publication Date: 2016-05-25
BEIJING ORIGIN WATER FILM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this treatment method has a limited range to increase the flux. At the same time, due to the side reactions of other small molecules introduced in the reaction, a looser desalination layer is formed. The decrease in the density of the desalination layer makes the molecular interception of the membrane drop significantly, thus bringing The membrane performance improvement effect is not significant
[0005] Still aiming at the problem of low performance, some researchers improved its performance by "coating the hydrophilic polymer first, drying it in the shade, then adding the aqueous phase solution and continuing the interfacial polymerization reaction with the oil phase on the basis", but This method often causes the desalination layer to fall off after long-term operation due to poor adhesion between the base film and the first desalination layer; in addition, many researchers obtain a polyamide desalination layer through the "acyl chloride reaction, and then continue to coat the desalination layer on the basis of the desalination layer." However, this method often reduces the flux of the membrane significantly, so it is impossible to achieve both high flux and high desalination options.
Moreover, the properties of the nanofiltration membrane membranes prepared by these methods are seriously attenuated, which cannot meet the actual long-term production, that is, the long-term stability of the nanofiltration membranes cannot be guaranteed.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] First, soak the polysulfone ultrafiltration base membrane in 1wt% isopropanol solution for 4h to increase its degree of infiltration, then wash it with pure water, and configure it to contain piperazine with a mass fraction of 0.2wt% and a mass fraction of 0.3wt After the aqueous phase solution of the humectant triethylamine camphorsulfonate of 0.1% by weight is stirred evenly, the n-hexane solution of 0.1wt% polyfunctional acid chloride is prepared. Fix the polysulfone ultrafiltration membrane (molecular weight cut off about 68,000) on a glass plate, then pour a certain volume of aqueous phase solution into the surface of the ultrafiltration membrane, leave it for 10 seconds, then pour out the aqueous phase solution, and then pour the membrane After the surface water phase dries. Then pour a certain volume of oil phase solution into the surface of the membrane, and after standing for 10 seconds, pour out the oil phase. After the organic solvent on the surface of the me...

Embodiment 2

[0032] Configure the aqueous phase solution that contains the piperazine that mass fraction is 0.2%, the polyester polyol that mass fraction is 0.1% and the humectant triethylamine camphorsulfonate that mass fraction is 0.3%, other operation steps are with embodiment 1.

Embodiment 3

[0034] Configure the water phase solution that contains the piperazine that mass fraction is 0.2%, the polyvinyl alcohol ammonium sulfate that mass fraction is 0.1% and the humectant triethylamine camphorsulfonate that mass fraction is 0.3%, other operation steps are with embodiment 1.

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Abstract

The invention provides a method for preparing a nanofiltration membrane with high desalination selectivity and high flux. The method comprises the following steps: S10, preparation of an aqueous phase solution and an organic phase solution, wherein the aqueous phase solution containing multifunctional polyamines, reactive hydroxyl polymer and hydrophilic polymer salt, and the organic phase solution of polyfunctional acyl chloride with at least two reactive acyl halide groups are prepared; S20, interfacial polymerization reaction, wherein an ultrafiltration diaphragm is fixed on a glass plate, then the aqueous phase solution is poured onto the surface of the ultrafiltration diaphragm, and is poured away after placed for 10-30s, the organic phase solution is poured onto the surface of the ultrafiltration diaphragm after the aqueous phase solution on the surface of the diaphragm is dry, and poured away after placed for 10-30s, the ultrafiltration diaphragm is then placed in an oven at a temperature of 40-120 DEG C for thermal treatment, and a finished product is obtained. The method for preparing the nanofiltration membrane has the advantages that while the water flux of the nanofiltration membrane is improved, the desalination selectivity of the nanofiltration membrane is expanded to a relatively large extent.

Description

technical field [0001] The invention relates to membrane treatment technology, in particular to a preparation method of a nanofiltration membrane with high desalination selectivity and high flux. Background technique [0002] Nanofiltration is a new membrane separation technology between ultrafiltration and reverse osmosis, its operating pressure range is 0.2-1.0MPa, and the molecular weight cut-off is in the range of 200-2000. Compared with ultrafiltration membranes and reverse osmosis membranes, nanofiltration membranes have the advantages of high water flux and high rejection at lower operating pressures, especially for divalent ions and low molecular weight organic small molecules. It has a high rejection rate (greater than 98%), so it is widely used in water treatment, medicine, food and biological industries. The preparation process of nanofiltration membrane mainly includes phase inversion method, dilute solution coating method, interfacial polymerization method, hea...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D71/60B01D67/00B01D69/12B01D69/02
CPCB01D71/60B01D67/0006B01D69/02B01D69/12
Inventor 陈亦力杜文林夏建中丑树人于云
Owner BEIJING ORIGIN WATER FILM TECH
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