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A kind of high flux polyamide/zif-8 nanofiltration composite membrane and preparation method thereof

A technology of ZIF-8 and composite membrane, which is applied in chemical instruments and methods, membrane technology, semi-permeable membrane separation, etc., can solve the problems of MOFs agglomeration interface, defects, and affecting membrane separation performance, and achieve simple and feasible membrane production process. Effect of improving membrane performance and optimal selectivity

Inactive Publication Date: 2018-11-13
BEIJING FORESTRY UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The preparation of PA / MOFs nanofiltration membranes by this kind of filling and blending method requires the synthesis of MOFs materials before membrane formation, and the filling amount of MOFs is affected by its dispersion in the membrane-making liquid. separation performance

Method used

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  • A kind of high flux polyamide/zif-8 nanofiltration composite membrane and preparation method thereof
  • A kind of high flux polyamide/zif-8 nanofiltration composite membrane and preparation method thereof

Examples

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preparation example Construction

[0023] The invention provides a PA / ZIF-8 membrane used for nanofiltration and separation of aqueous solutions and a preparation method thereof. First, ZIF-8 particles are grown on the surface of the ultrafiltration bottom membrane by in-situ growth method, and then PA / ZIF-8 dense skin layer is prepared by the interfacial polymerization method, and the composite membrane is obtained by post-processing.

[0024] The prepared PA / ZIF-8 nanofiltration membrane uses a flat membrane performance evaluation device to evaluate the separation performance of the separation aqueous system, that is, the permeation flux and rejection rate of the membrane.

[0025] 1) Permeation flux (J), the permeability of the reaction membrane, its definition is:

[0026] J=M / (A·t) or J=V / (A·t)

[0027] In the formula, M and V are the mass (kg) and volume (m 3 ); A is the membrane area, m 2 ; T is the operating time, h.

[0028] 2) Rejection rate (R), the selectivity of the reaction membrane, its definition formula...

Embodiment 1~4

[0032] 5.0g Zn(NO 3 ) 2 ·6H 2 O is dissolved in a mixture of 100ml methanol and 50ml water to make Zn(NO 3 ) 2 ·6H 2 O solution, 15.0g 2-methylimidazole dissolved in 100mL methanol to prepare 2-methylimidazole solution; add Zn(NO 3 ) 2 ·6H 2 The O solution was quickly poured into the 2-methylimidazole solution and stirred for 10 minutes to obtain a white ZIF-8 dispersion. The polyethersulfone ultrafiltration bottom membrane (with a molecular weight cut-off of 30000 Dal) was immersed in the dispersion liquid and allowed to stand for 12 hours at room temperature to make the ZIF-8 particles grow on the surface of the bottom membrane. The bottom film was taken out and rinsed repeatedly with distilled water and methanol, and then dried at 60°C for 2 hours to obtain a single growth bottom film of ZIF-8. Repeat the above-mentioned ZIF-8 growth process to prepare a base film for multiple growth of ZIF-8.

[0033] The flat membrane performance evaluation device was used to evaluate the pu...

Embodiment 5-8

[0037] At room temperature, the TMC monomer is dissolved in n-hexane to prepare a 0.1% (w / v) organic phase solution, and the MPD monomer is dissolved in ultrapure water to prepare a 2% (w / v) aqueous phase solution. The ultrafiltration bottom membranes of Comparative Example 1 and Examples 1 to 4 were respectively selected and immersed in the MPD aqueous solution for 2 minutes, and the bottom membrane in the aqueous solution was taken out to remove the excess water phase on the membrane surface; then the bottom membrane was placed in the TMC The interfacial polymerization reaction occurred in the organic phase solution for 20 seconds, and it was taken out and dried in the air, and then heat-treated at 60°C for 2 min. Finally, it was repeatedly washed with deionized water to obtain a nanofiltration membrane.

[0038] The flat membrane performance evaluation device is used to determine the separation performance of the nanofiltration membrane separation aqueous solution system: the f...

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Abstract

The invention discloses a preparation method of a high-flux polyamide / ZIF-8 nanofiltration composite film. The preparation method comprises the following steps of (1) growing a ZIF-8 type metal-organic framework material on an ultrafiltration bottom film in situ; (2) preparing a polyamide skin layer on the bottom film with ZIF-8 particles through interfacial polymerization; and (3) post-treating a primary composite film to obtain the polyamide / ZIF-8 nanofiltration composite film. A dense skin layer of the nanofiltration film consists of ZIF-8 and polyamide; by virtue of single or multiple in-situ growth, the ZIF-8 particles grow on the surface of the bottom film, and the polyamide skin layer is formed through interfacial polymerization, and the ZIF-8 particles on the surface of the bottom film are embedded into the polyamide layer. By use of a ZIF-8 multi-hole structure and a nano-grade channel size, the nanofiltration separation performance of the polyamide film of the prepared polyamide / ZIF-8 nanofiltration composite film can be improved. On the basis of the in-situ growth method, the operation of firstly synthesizing ZIF-8 and then adding into film preparation liquid is eliminated, so that the film preparation technology is simple; the performance of the polyamide / ZIF-8 film prepared by in-situ growth for multiple times is high; when the nanofiltration composite film is used for separating an inorganic salt aqueous solution system, the permeation flux can be increased; when the nanofiltration composite film is used for separating a congo red aqueous solution, the permeation flux and the retention rate can be increased at the same time.

Description

Technical field: [0001] The invention relates to the preparation of a polyamide / ZIF-8 type metal-organic framework material nanofiltration composite membrane: ZIF-8 is grown in situ on the surface of the ultrafiltration bottom membrane in advance, and then polyamide / ZIF-8 nanofiltration is prepared by interfacial polymerization. Filter membrane. This method can introduce ZIF-8 material into the polyamide skin layer, increase the pores in the skin layer to improve the permeability of the membrane; pre-growth ZIF-8 can improve the dispersibility of ZIF-8 in the polyamide, thereby reducing interface defects and improving the membrane The selectivity. Background technique: [0002] The membrane separation process is a process in which the mixed components of the raw materials selectively permeate the separation membrane under the action of driving force to achieve separation. Nanofiltration is a membrane separation process driven by pressure difference. It has the characteristics o...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D71/56B01D69/12B01D67/00
Inventor 王璐莹雷建都何静刘静邓立红
Owner BEIJING FORESTRY UNIVERSITY