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Composite nanofiltration membrane and preparation method thereof

A composite nanofiltration membrane and base membrane technology, applied in chemical instruments and methods, membranes, membrane technology, etc., can solve the problems of low water flux of acid-resistant nanofiltration membranes, increase hydrophilicity and charge density, solve the Poor acid resistance

Inactive Publication Date: 2020-09-22
OCHEMATE MATERIAL TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] However, the water flux of current acid-resistant nanofiltration membranes is generally low. Patent CN105289305A discloses a preparation method for high-throughput acid-resistant nanofiltration membranes. The pure water flux of the prepared nanofiltration membranes at 0.5Mpa is 2.1 L / m 2 h

Method used

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  • Composite nanofiltration membrane and preparation method thereof
  • Composite nanofiltration membrane and preparation method thereof
  • Composite nanofiltration membrane and preparation method thereof

Examples

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preparation example Construction

[0046] (1) Preparation of polysulfone-based membrane

[0047] (1) Weighing 18wt% polysulfone, 72wt% N, N-dimethylacetamide, 10wt% polyethylene glycol with a molecular weight of 800;

[0048] (2) Add polysulfone to N,N-dimethylacetamide at 110°C, stir for 8 hours until the solution is clear; then add polyethylene glycol, stir at 50°C for 8 hours to form a casting solution;

[0049] (3) filter casting solution;

[0050] (4) Vacuum defoaming treatment of the filtered casting solution at 30° C. for 24 hours;

[0051] (5) On the film coating machine, the casting solution and polyester non-woven fabric are made into a membrane, and the membrane is placed in the air with a temperature of 25-30 ° C and a humidity of 70-80% for 2-3 minutes, and then Transfer to a deionized water coagulation bath for solidification, and soak in deionized water to obtain a polysulfone ultrafiltration membrane.

[0052] (2) Preparation of composite nanofiltration membrane

[0053] The prepared composi...

Embodiment 1

[0062] (1) 0.25g piperazine, 0.1g sodium dodecylsulfonate and 0.075g triethylamine are mixed with 100g deionized water to obtain an aqueous phase solution;

[0063] (2) Mix 0.15g 1,3,6-naphthalenetrisulfonyl chloride, 0.005g chlorinated anhydride and 100g Isopar G to obtain an oil phase solution;

[0064] (3) providing a polysulfone ultrafiltration base membrane with a molecular weight cut-off of 50,000 Da, immersing the base membrane in an aqueous phase solution to obtain a coated base membrane;

[0065] (4) The base film coated in step (3) was taken out after 5 minutes and dried at 30°C for 5 minutes, then immersed in the oil phase solution, taken out after 2 minutes and dried at 120°C for 5 minutes to obtain a composite nano filter membrane.

[0066] Test results: the obtained composite nanofiltration membrane was placed in 10wt% H 2 SO 4 Soaked in the aqueous solution for 10 hours, tested under the conditions of temperature 25°C and pressure 0.5Mpa, the pure water flux ...

Embodiment 2

[0068] (1) 1g piperazine is mixed with 100g deionized water to obtain an aqueous phase solution;

[0069] (2) Mix 0.25g of 1,3,6-naphthalenetrisulfonyl chloride, 0.015g of chlorinated anhydride and 100g of cyclohexane to obtain an oil phase solution;

[0070] (3) providing a polysulfone base membrane with a molecular weight cut-off of 50,000 Da, immersing the base membrane in an aqueous phase solution to obtain a coated base membrane;

[0071] (4) Take out the base film coated in step (3) after 5 minutes and dry it at 30°C for 5 minutes and then immerse it in the oil phase solution, take it out after 1 minute and dry it at 100°C for 10 minutes to obtain a composite nano filter membrane.

[0072] Test results: the obtained composite nanofiltration membrane was placed in 10wt% H 2 SO 4 Soaked in the aqueous solution for 10 hours, tested under the conditions of temperature 25°C and pressure 0.5Mpa, the pure water flux is 26L / m 2 h, the desalination rate is 80%.

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Abstract

The invention provides a high-flux composite nanofiltration membrane and a preparation method thereof. The acid resistance of the nanofiltration membrane is improved by obtaining a polysulfonamide desalination layer through interfacial polymerization reaction of polysulfonyl chloride, trimellitic anhydride chloride and polyamine. Chlorinated trimellitic anhydride, as an additive, is added into anoil phase solution to participate in an interface reaction, so that the porosity of a generated desalted layer can be increased, the finally prepared composite nanofiltration membrane has good acid resistance and high pure water flux at the same time, and the preparation process is simple, easy to implement, easy to realize industrialization and wide in application prospect.

Description

technical field [0001] The invention relates to a composite nanofiltration membrane and a preparation method thereof, in particular to an acid-resistant composite nanofiltration membrane and a preparation method thereof. Background technique [0002] As a new branch of membrane technology, nanofiltration separation technology is increasingly useful in modern chemical production. In the field of membrane separation technology, compared with ordinary nanofiltration membranes, composite nanofiltration membranes have the advantages of good permeability, strong pressure resistance and good selective separation performance due to their unique morphological structure, and are widely used. However, with the development of industry, the systems to be separated are gradually diversified and complicated. It is required that the separation membrane not only has good separation selectivity, but also has certain physical and chemical stability to maintain a long-term stable separation eff...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D69/12B01D69/02B01D71/68B01D71/34B01D67/00B01D61/02
CPCB01D61/027B01D67/0006B01D69/02B01D69/12B01D71/34B01D71/68B01D2325/26B01D2325/30B01D2325/36Y02A20/131
Inventor 王蒙王文宠沈艳君
Owner OCHEMATE MATERIAL TECH CO LTD