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Methanol permeation through proton exchange membranes of direct methanol fuel cells.

机译:甲醇透过直接甲醇燃料电池的质子交换膜渗透。

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Methanol permeation through proton exchange membranes is one of the major constraints inhibiting large scale commercialization of direct methanol fuel cell (DMFC). Potentiometric technique was used to determine methanol crossover flux and permeability of prepared SPEEK/TPA/MCM-41 and SPEEK/TPA/Y-zeolite composite membranes.; SPEEK/TPA/MCM-41 composite membranes with inorganic loadings (TPA/MCM-41) of 10wt %-30wt % have permeability values of 0.57 x 10-8 cm 2 s-1--3.51 x 10-8 cm 2 s-1. While SPEEK/TPA/Y-zeolite composite membranes with inorganic loadings (TPA/Y-zeolite) of 10wt % -30 wt % have permeability values of 1.71 x 10-8 cm2 s-1--4.29 x 10-8 cm 2 s-1. These values are low compared to that of pure SPEEK 1.6 membranes; 4.41 x 10-8 cm2s -1. But when 40wt % of TPA/Y-zeolite loading was used higher permeability value of 7.04 x 10-8 cm2s -1 was obtained. Better reduction in methanol permeation was observed with lower loadings of the inorganic material (TPA/MCM-41 or Y-zeolite) than with higher loadings. These composite membranes have good potential for use in the direct methanol fuel cell (DMFC) due to their low methanol permeability.
机译:通过质子交换膜的甲醇渗透是阻碍直接甲醇燃料电池(DMFC)大规模商业化的主要限制之一。用电位法测定所制备的SPEEK / TPA / MCM-41和SPEEK / TPA / Y-沸石复合膜的甲醇穿越通量和渗透率。无机载量(TPA / MCM-41)为10wt%-30wt%的SPEEK / TPA / MCM-41复合膜的渗透率值为0.57 x 10-8 cm 2 s-1--3.51 x 10-8 cm 2 s- 1。无机负载量(TPA / Y沸石)为10wt%-30 wt%的SPEEK / TPA / Y沸石复合膜的渗透率值为1.71 x 10-8 cm2 s-1--4.29 x 10-8 cm 2 s -1。与纯SPEEK 1.6膜相比,这些值较低; 4.41 x 10-8 cm2s -1。但是,当使用40wt%的TPA / Y沸石负载量时,可以获得更高的渗透率值7.04 x 10-8 cm2s -1。较低的无机材料负载量(TPA / MCM-41或Y沸石)比较高的负载量观察到更好的甲醇渗透降低。这些复合膜由于其低甲醇渗透性而具有直接甲醇燃料电池(DMFC)的良好潜力。

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