Preparation and application of polymer-aminated transition metal carbide blended membrane
A transition metal and carbide technology, which is used in the preparation and application of polymer-aminated transition metal carbide blend membranes, can solve problems such as high gas permeability and selectivity, and limited applications
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Embodiment 1
[0039] Weigh 1.4g of polyethylene glycol methyl ether acrylate, 0.6g of polyethylene glycol diacrylate, 0.0202g of f-MXene powder, and 0.002g of 1-hydroxycyclohexyl benzophenone in a glass bottle, stir well at room temperature, Mix f-MXene with the polymer evenly, and ultrasonically defoam in an ice-water bath to obtain a prepolymer solution. Pour the prepolymer solution onto a clean quartz plate, control the film thickness with a copper wire, cover another quartz plate, transfer it to an ultraviolet lamp, irradiate for 5 minutes and solidify to form a film, and peel off the film from the quartz plate to obtain Polymer-aminated transition metal carbide blend membranes.
[0040] The test conditions and methods were the same as in Comparative Example 1, CO 2 Gas permeability is 438.9 barrer, N 2 Gas permeability is 8.3barrer, CO 2 / N 2 The selectivity was 52.9.
Embodiment 2
[0042] The preparation method is consistent with that of Example 1, except that the mass of f-MXene powder is 0.0408g.
[0043] The test conditions and methods were the same as in Comparative Example 1, CO 2 Gas permeability is 380.3barrer, N 2 Gas permeability is 7.3barrer, CO 2 / N 2 The selectivity is 52.1.
Embodiment 3
[0045] The preparation method is the same as in Example 1, except that the mass of f-MXene powder is 0.0619g.
[0046] SEM characterization of the polymer-aminated transition metal carbide blend film prepared in Example 3, the structure is as follows figure 2 shown by figure 2 It can be seen that the f-MXene in the polymer-aminated transition metal carbide blend film prepared in this example has a two-dimensional sheet structure, which is evenly distributed in the film without obvious aggregation.
[0047] The test conditions and methods were the same as in Comparative Example 1, CO 2 Gas permeability is 915.3barrer, N 2 Gas permeability is 22.0barrer, CO 2 / N 2 The selectivity was 41.6.
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