A kind of modification method of proton exchange membrane for all-vanadium redox flow battery
An all-vanadium redox flow battery and proton exchange membrane technology, applied in fuel cells, regenerative fuel cells, circuits, etc., can solve the problems affecting the electrochemical performance of all-vanadium redox flow batteries, poor vanadium resistance performance, etc., and achieve vanadium ion permeation. The effect of reduced rate, good bonding, uniform cross-section
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Embodiment 1
[0041] Such as figure 1 As shown, embodiment 1 provides a kind of modification method for the proton exchange membrane of all-vanadium redox flow battery, and it comprises the following steps:
[0042] S1. Preparation of submicron ZSM-5 zeolite: first weigh 2.185g of deionized water, add it to 5.463g (the mass ratio of deionized water to tetrapropylammonium hydroxide is 1:2.5) and the concentration is 1.0 mol / L tetrapropylammonium hydroxide (TPAOH) aqueous solution, stirring to form a uniform solution; then weigh 1.093g of silicic acid (that is, the mass ratio of silicic acid to TPAOH is 1:5), and add silicic acid to the above uniform solution; then add 0.044g of sodium metaaluminate (that is, the mass ratio of sodium metaaluminate to silicic acid is 1:25) powder into the above solution, and stir evenly to obtain a milky white solution; then the obtained milky white The solution was stirred for 24 hours to obtain a homogeneous solution, which was transferred to a 100mL Teflon...
Embodiment 2
[0051] The difference between the modification method of a proton exchange membrane used in an all-vanadium redox flow battery provided in Example 2 and the modification method described in Example 1 is that the quality of TPAOH in Step S1 of Example 1 is 5.463 g is replaced by: the mass of TPAOH is 6.555g, that is to say, the mass ratio of deionized water to TPAOH is 1:3, and at the same time, according to the mass ratio of silicic acid to TPAOH is 1:5, sodium metaaluminate and silicic acid The mass ratio is 1:25, add 1.311g silicic acid and 0.052g sodium metaaluminate, other content is all the same as embodiment 1, repeats no more here. The composite proton exchange membrane prepared in Example 2 is numbered A2.
Embodiment 3
[0053] The difference between the modification method of a proton exchange membrane used in an all-vanadium redox flow battery provided in Example 3 and the modification method described in Example 1 is that the quality of TPAOH in step S1 of Example 1 is 5.463 g is replaced by: the mass of TPAOH is 7.648g, that is to say, the mass ratio of deionized water to TPAOH is 1:3.5, and at the same time, according to the mass ratio of silicic acid to TPAOH is 1:5, sodium metaaluminate and silicic acid The mass ratio is 1:25, add 1.530g silicic acid and 0.061g sodium metaaluminate, other content is all the same as embodiment 1, repeats no more here. The composite proton exchange membrane prepared in Example 3 is numbered A3.
[0054] Comparing the properties of the composite proton exchange membranes prepared in Examples 1-3, it was found that the performance of the composite proton exchange membrane prepared in Example 2 was the best. In other words, the performance of the composite ...
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