阅读说明：本技术 基于双金属片状材料填充的混合基质膜的制备方法及应用 (Preparation method and application of mixed matrix membrane filled with bimetallic strip material ) 是由 李雪琴 黄路 吕侠 梁朝 于 2020-12-10 设计创作，主要内容包括：本发明公开了基于双金属片状材料填充的混合基质膜的制备方法,涉及气体分离膜技术领域。本发明包括镍钴双金属MOF片(Ni-Co-NS),用Ni-Co-NS作为填充剂制备混合基质膜,该杂化膜的厚度100-130μm,它由质量分数为1 wt%-7 wt%的Ni-Co-NS和93%-99%的Pebax～#1657组成。本发明方法制备的Pebax/Ni-Co-NS混合基质膜制备过程简单,反应可控,原料价廉易得,条件温和,可使MOF与高分子基质优势互补,利用双金属MOF片的片状形貌特征,在膜内构建曲折的传递路径；以及在MOF结构上引入双金属位点,利用不同金属位点对CO-2的不对称吸附和解吸行为,制备的混合基质膜同时具有CO-2亲和性和筛分作用,可强化CO-2在膜中的传递。(The invention discloses a preparation method of a mixed matrix membrane based on filling of a bimetallic strip material, and relates to the technical field of gas separation membranes. The invention comprises a nickel-cobalt bimetallic MOF sheet (Ni-Co-NS), a mixed matrix membrane is prepared by using the Ni-Co-NS as a filler, the thickness of the mixed matrix membrane is 100-130 mu m, and the mixed matrix membrane is prepared by 1-7 wt% of Ni-Co-NS and 93-99 wt% of Pebax ® 1657 and (b) mixing. The Pebax/Ni-Co-NS mixed matrix membrane prepared by the method has the advantages of simple preparation process, controllable reaction, cheap and easily obtained raw materials and mild conditions, can complement the advantages of the MOF and the polymer matrix, and utilizes the sheet shape characteristics of the bimetallic MOF sheet to construct a tortuous transfer path in the membrane; and inBimetallic sites are introduced into the MOF structure, and different metal sites are utilized to react with CO 2 The prepared mixed matrix membrane has CO simultaneously 2 Affinity and sieving effects, and can enhance CO 2 Transport in the membrane.)

1. The preparation method of the mixed matrix membrane based on the filling of the bimetallic strip material comprises a nickel-cobalt bimetallic MOF strip (Ni-Co-NS), and is characterized in that: the Ni-Co-NS is used as a filler to prepare a mixed matrix membrane, the thickness of the mixed matrix membrane is 100-130 mu m, and the mixed matrix membrane consists of 1-7 wt% of Ni-Co-NS and 93-99 wt% of Pebax^®1657 and (b) mixing.

2. The method for preparing a hybrid matrix membrane based on the filling of a bimetallic strip material according to claim 1, characterized in that: the preparation method comprises the steps of preparing Ni-Co-NS, preparing a Pebax solution and preparing a mixed matrix membrane by filling the Pebax with the Ni-Co-NS;

the preparation method of the Ni-Co-NS comprises the following steps:

step 1: weighing a certain amount of nickel nitrate hexahydrate (Ni (NO)₃)₂·6H₂O), cobalt nitrate hexahydrate (Co (NO)₃)₂·6H₂O) and terephthalic acid are dissolved in a certain volume of water, ethanol and N, N-Dimethylformamide (DMF) and stirred vigorously;

step 2: quickly adding a certain volume of triethylamine into the mixed solution in the stirring process, and continuously stirring for reacting for 5 min to obtain a mixed solution;

step 3: carrying out ultrasonic reaction on the mixed solution at room temperature for 4 hours, and then sequentially carrying out centrifugation and washing for three times to obtain Ni-Co-NS;

step 4: drying the Ni-Co-NS at 60 ℃ overnight to obtain a Ni-Co-NS nano filler;

the preparation method of the Pebax solution comprises the following steps:

step 5: weighing a certain amount of Pebax particles, dissolving the Pebax particles in a mixed solution of ethanol and water (the mass ratio is 70%/30%), heating in a water bath at 80 ℃ and stirring for 2 hours to completely dissolve the Pebax, thus obtaining a 6 wt% Pebax matrix solution;

the preparation method of the mixed matrix membrane comprises the following steps:

step 6: the Ni-Co-NS obtained by the method is mixed according to the mass ratio of (0.93-0.99): (0.01-0.07) physically blending with the prepared Pebax solution, and stirring for 4 hours at room temperature to obtain a casting solution;

step 7: pouring the obtained casting solution into a clean culture dish for casting film formation, and drying at room temperature (25 ℃) for 48 hours;

step 8: and (3) drying the dried casting solution in a vacuum drying oven at 40 ℃ for 24 h in vacuum, and removing residual solvent on the surface to obtain the required Pebax/Ni-Co-NS mixed matrix membrane with the membrane thickness of 100-.

3. The method for preparing the mixed matrix membrane based on the filling of the bimetallic strip-shaped material as claimed in claim 2, wherein the using mass of each solvent in the Step1 is nickel nitrate hexahydrate (Ni (NO)₃)₂·6H₂O) 5 mmol, cobalt nitrate hexahydrate (Co (NO)₃)₂·6H₂O) 2.5 mmol, terephthalic acid 7.5 mmol, water 2 mL, ethanol 2 mL and N, N-Dimethylformamide (DMF) 30 mL, and the amount of triethylamine added in Step2 is 0.8 mL.

4. The method for preparing the mixed matrix membrane based on the filling of the bimetallic strip-shaped material as claimed in claim 3, wherein the weighed amount of the Pebax particles in Step5 is 0.537 g.

5. The method for preparing the mixed matrix membrane based on the filling of the bimetal sheet material as claimed in claim 4, wherein the mass percentage of Ni-Co-NS in Step6 is 1 wt%, 3 wt%, 5 wt% and 7 wt%, and the Pebax solution in Step6 is 6 wt% Pebax solution.

6. The method for preparing a mixed matrix membrane based on the filling of a bimetallic strip material as claimed in claim 5, wherein the mass ratio of Pebax to Ni-Co-NS is 0.99:0.01, 0.97:0.03, 0.95: 0.5,0.93: 0.07.

7. the method for preparing the bimetal sheet material filling-based mixed matrix membrane according to claim 6, wherein the Pebax/Ni-Co-NS mixed matrix membrane is used for separating CO₂/CH₄Mixed gas of CO₂Flux was 394-483 Barrer (1 Barrer = 10)^-10 cm³ cm / cm² s cmHg），CO₂/CH₄The selectivity is 27-37.

Technical Field

The invention belongs to the technical field of gas separation membranes, and particularly relates to a preparation method and application of a mixed matrix membrane filled with a bimetallic strip material.

Background

The biological methane gas has the advantages of wide raw material source, short equipment construction period and the like, is used for relieving the energy crisis caused by fossil energy, and has the advantages that the main gas in the biological methane gas is methane gas (55-70 percent) and a small amount of CO exists₂(30% -45%) due to CO₂The existence of the carbon dioxide can affect the heat value and pipeline transportation of the biological methane gas, so that CO in the biological methane gas₂The removal is the key direction of current researchers' research and is in comparison with the traditional physical adsorption method and chemical absorption method to remove CO₂Compared with the membrane separation method, the membrane separation method has the advantages of high efficiency, environmental protection, low energy consumption, simple operation, small occupied area and the like, so that the membrane separation method is applied to CO₂The method has great potential in the aspect of removal, in order to improve the performance of the polymer film, graphene oxide, a covalent organic framework, a metal organic framework and the like are used as a filler to be combined with a polymer material to prepare a Mixed Matrix Membrane (MMMs), so that the MMMs have the advantages of the polymer material and the filler and can derive new advantages at the same time;

among all membrane materials, the traditional polymer membrane material is widely researched due to the advantages of easy processing, low price and the like, but the gas separation performance of the polymer membrane is limited by the trade-off effect and is difficult to break through the Robeson upper limit.

Disclosure of Invention

The invention aims to provide a preparation method of a mixed matrix membrane filled with a bimetallic strip material, which solves the problem that the gas separation performance of a polymer membrane is restricted by a trade-off effect and is difficult to break through the Robeson upper limit and the like.

In order to solve the technical problems, the invention is realized by the following technical scheme:

the invention relates to a preparation method of a mixed matrix membrane based on bimetallic strip material filling, which comprises a nickel-cobalt bimetallic MOF (Ni-Co-NS) sheet, wherein the Ni-Co-NS sheet is used as a filling agent to prepare the mixed matrix membrane, the thickness of the mixed membrane is 130 mu m, and the mixed matrix membrane is prepared from 1-7 wt% of Ni-Co-NS and 93-99% of Pebax by mass fraction^®1657 of a solvent;

preferably, the preparation method comprises the preparation of Ni-Co-NS, the preparation of Pebax solution and the preparation of Ni-Co-NS filled Pebax mixed matrix membrane;

the preparation method of the Ni-Co-NS comprises the following steps:

step 1: weighing a certain amount of nickel nitrate hexahydrate (Ni (NO)₃)₂·6H₂O), cobalt nitrate hexahydrate (Co (NO)₃)₂·6H₂O) and terephthalic acid are dissolved in a certain volume of water, ethanol and N, N-Dimethylformamide (DMF) and stirred vigorously;

step 2: quickly adding a certain volume of triethylamine into the mixed solution in the stirring process, and continuously stirring for reacting for 5 min to obtain a mixed solution;

step 3: carrying out ultrasonic reaction on the mixed solution at room temperature for 4 hours, and then sequentially carrying out centrifugation and washing for three times to obtain Ni-Co-NS;

step 4: drying the Ni-Co-NS at 60 ℃ overnight to obtain a Ni-Co-NS nano filler;

the preparation method of the Pebax solution comprises the following steps:

step 5: weighing a certain amount of Pebax particles, dissolving the Pebax particles in a mixed solution of ethanol and water (the mass ratio is 70%/30%), heating in a water bath at 80 ℃ and stirring for 2 hours to completely dissolve the Pebax, thus obtaining a 6 wt% Pebax matrix solution;

the preparation method of the mixed matrix membrane comprises the following steps:

step 6: the Ni-Co-NS obtained by the method is mixed according to the mass ratio of (0.93-0.99): (0.01-0.07) physically blending with the prepared Pebax solution, and stirring for 4 hours at room temperature to obtain a casting solution;

step 7: pouring the obtained casting solution into a clean culture dish for casting film formation, and drying at room temperature (25 ℃) for 48 hours;

step 8: and (3) drying the dried casting solution in a vacuum drying oven at 40 ℃ for 24 h in vacuum, and removing residual solvent on the surface to obtain the required Pebax/Ni-Co-NS mixed matrix membrane with the membrane thickness of 100-.

Preferably, the used mass of each solvent in Step1 is nickel nitrate hexahydrate (Ni (NO)₃)₂·6H₂O) 5 mmol, hexahydrateCobalt nitrate (Co (NO)₃)₂·6H₂O) 2.5 mmol, terephthalic acid 7.5 mmol, water 2 mL, ethanol 2 mL and N, N-Dimethylformamide (DMF) 30 mL, and the amount of triethylamine added in Step2 is 0.8 mL.

Preferably, the weighed amount of the Pebax particles in Step5 is 0.537 g.

Preferably, the mass percentage of the Ni-Co-NS in Step6 is 1 wt%, 3 wt%, 5 wt% and 7 wt%, and the Pebax solution in Step6 is a 6 wt% Pebax solution.

Preferably, the mass ratio of Pebax to Ni-Co-NS is 0.99:0.01, 0.97:0.03, 0.95: 0.5,0.93: 0.07.

preferably, the Pebax/Ni-Co-NS mixed matrix membrane is used for separating CO₂/CH₄Mixed gas of CO₂Flux was 394-483 Barrer (1 Barrer = 10)^-10 cm³ cm / cm² s cmHg），CO₂/CH₄The selectivity is 27-37.

The invention has the following beneficial effects:

the Pebax/Ni-Co-NS mixed matrix membrane prepared by the method has the advantages of simple preparation process, controllable reaction, cheap and easily obtained raw materials and mild conditions, can complement the advantages of the MOF and the polymer matrix, and utilizes the sheet shape characteristics of the bimetallic MOF sheet to construct a tortuous transfer path in the membrane; and introducing bimetallic sites on the MOF structure, utilizing different metal sites for CO₂The prepared mixed matrix membrane has CO simultaneously₂Affinity and sieving effects, and can enhance CO₂Transport in the membrane to CO₂/CH₄The mixture's permselectivity has exceeded the 2008 Robeson upper limit.

Of course, it is not necessary for any product in which the invention is practiced to achieve all of the above-described advantages at the same time.

Drawings

FIG. 1 is a sectional view of a scanning electron microscope of a Pebax/Ni-Co-NS-1 mixed matrix membrane prepared in example 1;

FIG. 2 is a cross-sectional view of a scanning electron microscope of the Pebax/Ni-Co-NS-3 mixed matrix membrane prepared in example 2;

FIG. 3 is a sectional view of a scanning electron microscope of the Pebax/Ni-Co-NS-5 mixed matrix membrane prepared in example 3;

FIG. 4 is a sectional view of a scanning electron microscope of the Pebax/Ni-Co-NS-7 mixed matrix membrane prepared in example 4;

FIG. 5 is a cross-sectional view of a Pebax film prepared in comparative example 1 under a scanning electron microscope;

FIG. 6 is a cross-sectional view of a scanning electron microscope of the Pebax/Ni-NS-5 film obtained in comparative example 2.

Detailed Description

The technical solutions in the embodiments of the present invention are clearly and completely described below, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.

The invention relates to a preparation method of a mixed matrix membrane based on bimetallic strip material filling, which comprises a nickel-cobalt bimetallic MOF (Ni-Co-NS) sheet, wherein the Ni-Co-NS sheet is used as a filling agent to prepare the mixed matrix membrane, the thickness of the mixed membrane is 130 mu m, and the mixed matrix membrane is prepared from 1-7 wt% of Ni-Co-NS and 93-99% of Pebax by mass fraction^®1657 and (b) mixing.

Further, the preparation method comprises the preparation of Ni-Co-NS, the preparation of Pebax solution and the preparation of mixed matrix membrane by filling the Pebax with the Ni-Co-NS;

the preparation method of the Ni-Co-NS comprises the following steps:

step 1: weighing a certain amount of nickel nitrate hexahydrate (Ni (NO)₃)₂·6H₂O), cobalt nitrate hexahydrate (Co (NO)₃)₂·6H₂O) and terephthalic acid are dissolved in a certain volume of water, ethanol and N, N-Dimethylformamide (DMF) and stirred vigorously;

step 2: quickly adding a certain volume of triethylamine into the mixed solution in the stirring process, and continuously stirring for reacting for 5 min to obtain a mixed solution;

step 3: carrying out ultrasonic reaction on the mixed solution at room temperature for 4 hours, and then sequentially carrying out centrifugation and washing for three times to obtain Ni-Co-NS;

step 4: drying the Ni-Co-NS at 60 ℃ overnight to obtain a Ni-Co-NS nano filler;

the preparation method of the Pebax solution comprises the following steps:

step 5: weighing a certain amount of Pebax particles, dissolving the Pebax particles in a mixed solution of ethanol and water (the mass ratio is 70%/30%), heating in a water bath at 80 ℃ and stirring for 2 hours to completely dissolve the Pebax, thus obtaining a 6 wt% Pebax matrix solution;

the preparation method of the mixed matrix membrane comprises the following steps:

step 6: the Ni-Co-NS obtained by the method is mixed according to the mass ratio of (0.93-0.99): (0.01-0.07) physically blending with the prepared Pebax solution, and stirring for 4 hours at room temperature to obtain a casting solution;

step 7: pouring the obtained casting solution into a clean culture dish for casting film formation, and drying at room temperature (25 ℃) for 48 hours;

step 8: and (3) drying the dried casting solution in a vacuum drying oven at 40 ℃ for 24 h in vacuum, and removing residual solvent on the surface to obtain the required Pebax/Ni-Co-NS mixed matrix membrane with the membrane thickness of 100-.

Further, the used mass of each solvent in Step1 was nickel nitrate hexahydrate (Ni (NO)₃)₂·6H₂O) 5 mmol, cobalt nitrate hexahydrate (Co (NO)₃)₂·6H₂O) 2.5 mmol, terephthalic acid 7.5 mmol, water 2 mL, ethanol 2 mL and N, N-Dimethylformamide (DMF) 30 mL, the amount of triethylamine added in Step2 was 0.8 mL.

Further, the amount of Pebax particles weighed in Step5 was 0.537 g.

Further, the mass percentages of Ni-Co-NS in Step6 are 1 wt%, 3 wt%, 5 wt% and 7 wt%, and the Pebax solution in Step6 is a 6 wt% Pebax solution.

Further, the mass ratio of Pebax to Ni-Co-NS is 0.99:0.01, 0.97:0.03, 0.95: 0.5,0.93: 0.07.

further, Pebax/Ni-Co-NS mixed matrix membranes are used for CO separation₂/CH₄Mixed gas of CO₂The flux is 394-483 Barrer (1 Barrer =)10^-10 cm³ cm / cm² s cmHg），CO₂/CH₄The selectivity is 27-37.

Example 1:

preparing a Pebax/Ni-Co-NS-1 mixed matrix membrane, wherein the thickness of the mixed matrix membrane is 107 microns, the Pebax is used as a membrane matrix of the mixed matrix membrane, and Ni-Co-NS is added into the membrane matrix, wherein the mass ratio of the Pebax to the Ni-Co-NS is 0.99:0.01, the preparation method of the mixed matrix membrane comprises the following steps:

step1, preparation of Ni-Co-NS:

at room temperature 5 mmol of Co (NO)₃)₂·6H₂O，2.5 mmol Ni(NO₃)₂·6H₂O and 7.5 mmol of terephthalic acid were dissolved in a mixed solution of 2 mL of water, 2 mL of ethanol and 30 mL of DMF. Then, 0.8 mL of triethylamine was added to the reaction system with vigorous stirring, and then it was sonicated for 4 h. The precipitate was collected by centrifugation and washed three times with ethanol to give Ni-Co-NS. Finally, the Ni-Co-NS was dried overnight at 60 ℃ and Ni-Co-NS nanofillers were obtained.

Step2, weighing 0.537 g of Pebax, dissolving the Pebax into 10 ml of mixed solution of ethanol and water (the mass fraction ratio is 7: 3), and stirring the mixture for 2 hours at 80 ℃ to completely dissolve Pebax particles so as to prepare a Pebax matrix solution with the mass fraction of 6 wt%.

Step3, physically blending the Ni-Co-NS (0.0054 g) prepared in the step1 and the 6 wt% Pebax matrix solution prepared in the step2, stirring for 4 hours at room temperature to obtain a casting solution, and pouring the casting solution on a clean culture dish for casting; drying at room temperature (25 ℃) for 48 h, and then drying in a vacuum drying oven at 40 ℃ in vacuum to remove residual solvent on the surface of the mixed matrix membrane to obtain a Pebax/Ni-Co-NS-1 mixed matrix membrane, wherein the thickness of the mixed matrix membrane is 117 mu m.

FIG. 1 is a sectional view of a scanning electron microscope of the Pebax/Ni-Co-NS-1 mixed matrix membrane prepared in example 1.

The Pebax/Ni-Co-NS-1 mixed matrix membrane is used for CO at 25 ℃ and 2 bar₂20% by volume of CO₂/CH₄Mixed gas separation test of CO₂Flux 394 Barrer, CO₂/CH₄The selectivity was 27.

Example 2:

a Pebax/Ni-Co-NS-3 mixed matrix membrane was prepared, which differs from the Pebax/Ni-Co-NS-3 mixed matrix membrane in example 1 in that: the thickness of the film was 117 μm, wherein the mass ratio of Pebax to Ni-Co-NS was 0.97:0.03, the preparation of this mixed matrix membrane differs from the preparation method of example 1 only in that: in step3, 0.0054 g of Ni-Co-NS is changed into 0.0166 g of Ni-Co-NS; finally, a mixed matrix film having a thickness of 117 μm was obtained.

FIG. 2 is a cross-sectional view of a scanning electron microscope of the Pebax/Ni-Co-NS-3 mixed matrix membrane prepared in example 2.

The Pebax/Ni-Co-NS-3 mixed matrix membrane obtained in example 2 was used for CO at 25 ℃ under 2 bar₂20% by volume of CO₂/CH₄Separation test of mixture gas, CO thereof₂Flux of 420 Barrer, CO₂/CH₄The selectivity was 32.

Example 3:

a Pebax/Ni-Co-NS-5 mixed matrix membrane was prepared, which differs from the Pebax/Ni-Co-NS-1 mixed matrix membrane of example 1 in that: the thickness of the film was 123 μm, wherein the mass ratio of Pebax to Ni-Co-NS was 0.95: 0.05, the preparation of the mixed matrix membrane differs from the preparation method of example 1 only in that: in step3, 0.0054 g of Ni-Co-NS is changed into 0.0283 g of Ni-Co-NS; finally, a mixed matrix film having a thickness of 123 μm was obtained.

FIG. 3 is a cross-sectional view of a scanning electron microscope of the Pebax/Ni-Co-NS-5 mixed matrix membrane prepared in example 3.

The Pebax/Ni-Co-NS-5 mixed matrix membrane obtained in example 3 was used for CO at 25 ℃ under 2 bar₂20% by volume of CO₂/CH₄Separation test of mixture gas, CO thereof₂A flux of 483 Barrer, CO₂/CH₄The selectivity was 36.

Example 4:

a Pebax/Ni-Co-NS-7 mixed matrix membrane was prepared, which differs from the Pebax/Ni-Co-NS-1 mixed matrix membrane in example 1 in that: the thickness of the film is 125 μm, wherein the mass ratio of Pebax to Ni-Co-NS is 0.93: 0.07, the preparation of this mixed matrix membrane differs from the preparation method of example 1 only in that: in step3, weighing 0.0054 g of Ni-Co-NS into 0.0404 g of Ni-Co-NS; finally, a mixed matrix film having a thickness of 125 μm was obtained.

FIG. 4 is a cross-sectional view of a scanning electron microscope of the Pebax/Ni-Co-NS-7 mixed matrix membrane prepared in example 4.

The Pebax/Ni-Co-NS-7 mixed matrix membrane obtained in example 4 was used for CO at 25 ℃ under 2 bar₂20% by volume of CO₂/CH₄Separation test of mixture gas, CO thereof₂Flux 443 Barrer, CO₂/CH₄The selectivity was 29.

Comparative example 1:

preparing a Pebax film with the film thickness of 106 mu m; the preparation method comprises the following steps: 0.537 g of Pebax particles are weighed and dissolved in a mixed solution of ethanol with the mass fraction of 70% and water with the mass fraction of 30%, stirred for 2 h at 80 ℃, the obtained casting solution is poured on a clean super-flat dish for casting, dried for 48 h at room temperature, and then put into a vacuum oven with the temperature of 40 ℃ for 24 h to remove residual solvent, so as to obtain a Pebax film with the thickness of 106 μm.

FIG. 5 is a cross-sectional view of a pure Pebax film prepared in the comparative example under a scanning electron microscope.

The Pebax membrane prepared in the comparative example was used for CO at 25 ℃ and 2 bar₂20% by volume of CO₂/CH₄Separation test of mixture gas, CO thereof₂Flux of 280 Barrer, CO₂/CH₄The selectivity was 25.

Comparative example 2:

Pebax/Ni-NS-5 films were prepared, in contrast to Pebax/Ni-Co-NS-5 in example 3: the film thickness was 121 μm. The preparation of this mixed matrix membrane differs from the preparation of example 3 only in that: in step3, 0.0283 g of Ni-Co-NS is changed into 0.0283 g of Ni-NS; finally, a mixed matrix film having a thickness of 121 μm was obtained.

FIG. 6 is a sectional view of a Pebax/Ni-NS-5 mixed matrix film obtained in comparative example 2 under a scanning electron microscope.

Peb from comparative example 2 at 25 ℃ under 2 barAax/Ni-NS-5 mixed matrix membranes for CO₂20% by volume of CO₂/CH₄Separation test of mixture gas, CO thereof₂Flux of 425 Barrer, CO₂/CH₄The selectivity was 31.

Compared with 3-dimensional isotropic filler, the 2-dimensional filler with the characteristic of high length-width ratio greatly increases the contact area with the mixed matrix membrane, so that a tortuous transfer path is constructed in the mixed matrix membrane for wide application, and transition metal ions can effectively increase CO in the mixed matrix through pi-complexation₂And different metal ions due to their respective inherent properties, for CO₂Has different affinities and asymmetric adsorption and desorption behaviors, and can improve the mixed matrix membrane to CO₂/CH₄The perm-selectivity of the mixed gas.

The invention uses the ultrasonic reaction to synthesize the nickel-cobalt bimetallic MOF sheet (Ni-Co-NS) as the filler, according to different metal pairs CO₂With high aspect ratio, the construction of tortuous CO in mixed matrix membranes based on polyoxyethylene-polyamide block copolymers (Pebax)₂A transfer path to promote the perm-selective properties of the mixed matrix membrane and to overcome the trade-off effect.

In the description herein, references to the description of "one embodiment," "an example," "a specific example" or the like are intended to mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.

The preferred embodiments of the invention disclosed above are intended to be illustrative only. The preferred embodiments are not intended to be exhaustive or to limit the invention to the precise embodiments disclosed. Obviously, many modifications and variations are possible in light of the above teaching. The embodiments were chosen and described in order to best explain the principles of the invention and the practical application, to thereby enable others skilled in the art to best utilize the invention. The invention is limited only by the claims and their full scope and equivalents.