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ZIF-8-contained mixed matrix membrane as well as preparation and application thereof

A mixed matrix membrane, ZIF-8 technology, applied in membrane, membrane technology, semi-permeable membrane separation and other directions, can solve the problems of plasticization, gas separation performance reduction, etc. high volume effect

Inactive Publication Date: 2018-02-13
NANJING TECH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

On the other hand, polymer membranes generally have plasticization phenomenon, and the gas separation performance decreases with the increase of pressure.

Method used

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  • ZIF-8-contained mixed matrix membrane as well as preparation and application thereof
  • ZIF-8-contained mixed matrix membrane as well as preparation and application thereof
  • ZIF-8-contained mixed matrix membrane as well as preparation and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] Add 0.11 g of ZIF-8 nanoparticles into 5 mL of toluene solvent, stir to dissolve completely and evenly disperse. Take 1 gram of PEGDA-400 polymer, first add 0.1 gram of PEGDA-400 and 0.001 gram of benzoin dimethyl ether into the above solution, stir and disperse evenly. Add 0.9 g of PEGDA-400 into the solution and disperse evenly. Then, nitrogen was used to slowly purge excess toluene in the polymer solution (purge while stirring), and when nearly 1 gram of toluene remained, the purge was terminated. Then stand for degassing, pour the casting solution on the PAN ultrafiltration membrane, put it in the ultraviolet crosslinking apparatus to solidify for 2 minutes to form a solid film, and then soak it in toluene for 1 day. Then put it into a vacuum drying oven, vacuumize at 30°C for 12h, then raise the temperature to 70°C and dry for 12h, further remove the residual solvent, and finally obtain a mixed matrix film with a mass fraction of ZIF-8 of 10%, and a film thickness...

Embodiment 2

[0037] 0.11, 0.43, and 4.0 g of ZIF-8 were uniformly dispersed in three 10 mL portions of ethanol, respectively. Take three parts of 1 gram of PEGDA-600 polymer, first add 0.05 gram of PEGDA-600 and 0.005 gram of HCPK into the above solution, stir and disperse evenly. Add 0.95 g of PEGDA-600 into the solution and disperse evenly. Then, nitrogen was used to slowly purge excess ethanol in the polymer solution (purge while stirring), and when nearly 1 gram of ethanol remained, the purge was terminated. Then, the casting solution is obtained after static defoaming. Pour three parts of the casting solution on the PAN ultrafiltration membrane, irradiate with ultraviolet cross-linking method for 5 minutes to form a solid film, and then soak it in toluene for 1 day; then put it in a vacuum drying oven and vacuumize it at 45°C for 36 hours. Then the temperature was raised to 80° C. and dried for 36 hours to further remove the residual solvent, and finally obtained ZIF-8 / cross-linked ...

Embodiment 3

[0042] Add 3 parts of 0.43 g of ZIF-8 nanoparticles into 6 parts of 10 mL of chloroform solvent, stir to completely dissolve and evenly disperse. Take 1 gram of three organic polymers (PEGMEM, PEGMEA and PEGDMA), add 0.2 gram of organic polymer and 0.005 gram of HHMP into the above ZIF-8 solution, and disperse evenly. Then the remaining 0.8 g of organic polymer was added to the above solution and dispersed evenly. The solution was then slowly purged with nitrogen to remove excess chloroform (purging while stirring), until the chloroform volatilized to nearly 1 g, the purging was terminated. Then, static defoaming was carried out to obtain a uniform solution. The solution was coated on the PAN ultrafiltration membrane by knife coating. The method of ultraviolet crosslinking was irradiated for 30 minutes to make a solid film, and then soaked in chloroform for 1 day; then put it in a vacuum drying oven, evacuated at 60°C for 24h, and then dried at 100°C for 24h to further remov...

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Abstract

The invention discloses a ZIF-8-contained mixed matrix membrane as well as preparation and application thereof. The mixed matrix membrane is made of an organic polymer, and filler is made of nanoparticle ZIF-8, wherein the mass percent of the ZIF-8 in the mixed matrix membrane is 10 to 80 percent; the thickness of the mixed matrix membrane is 0.2 to 5 [mu]m. The ZIF-8 nanoparticles are uniformly dispersed in the organic polymer and a mixture coats a polyacrylonitrile ultrafiltration membrane supporting body by using a knife coating method, and finally a finished product is obtained. Stronger interaction is formed between the ZIF-8 and the interface of the organic polymer, so that mechanical properties of the membrane can be remarkably improved, and the mixed matrix membrane with high content of the ZIF-8 is prepared. The mixed matrix membrane has an obvious separating property for separating C3H6 / C3H8 mixed gas (JC3H6 is greater than 100 GPU, and alphaC3H6 / C3H8 is greater than 35), andreaches commercial application performance. The mixed matrix membrane prepared by the preparation method disclosed by the invention has higher gas permeability and separation selectivity of C3H6 andcan be applied to separation of propylene and propane in petroleum industry.

Description

technical field [0001] The invention belongs to the technical field of gas separation membranes, and in particular relates to a mixed matrix membrane containing ZIF-8 and its preparation and application. Background technique [0002] Olefin / alkane separation has long been an energy-intensive process in petrochemical production. For low-carbon olefins, the catalytic cracking method is mainly used to obtain them, but the cracked products are mixtures of olefins and alkanes, which must be separated. The conventional separation method currently used in industry is mainly low-temperature distillation. Since the boiling point of the mixture of alkanes and olefins with the same carbon is close, the separation process requires high energy consumption and large investment in production equipment. In order to reduce the cost and improve the separation effect, at present, membrane separation technology is mainly used to adapt to the development of new contemporary industries. Membrane...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D71/82B01D69/02B01D67/00B01D53/22
CPCB01D53/228B01D67/0002B01D69/02B01D71/82B01D2257/7022B01D2325/24B01D2325/04
Inventor 潘宜昌向龙王重庆
Owner NANJING TECH UNIV