催化剂层 meaning in Chinese
catalyst lining
Examples
- Improvement of power output has also been achieved by increasing the porosity of the anode catalyst layer , so that the co2 produced there can be easily released
本研究还以促进co2气体排放为目标，采用添加造孔剂的方法提高了液体进料dmfc阳极催化剂层的孔隙率，显著地改善了电池性能。 - The decrease of active surface area in the anode caused by co2 accumulation is reduced through treating the diffusion layer and catalyst layer with ptfe , resulting in increased dmfc performance
通过对阳极扩散层和催化剂层的疏水处理，降低了阳极产生的co2导致的催化活性比表面积损失，有效地提高了电池性能。 - The performance of liquid dmfc is evaluated as a function of the composition and structure of meas , hot - pressing condition and activation process by means of v - i polarization and ac impedance spectrometry
本研究采用电流电压极化曲线和交流阻抗谱方法，对膜电极的热压条件、扩散层和催化剂层的组成与结构、电极活化过程等因素对液体进料dmfc性能的影响进行了全面的研究。 - The investigation reveals that the performance of a mea is mainly controlled by the conductivity of membrane , load of catalyst and co2 holding in the anode , ion conductivity and specific of active area in both anode and cathode
研究表明，膜电极性能主要受质子交换膜的电导率、阳极催化剂用量、阳极co2气体和阴极水的传递、催化剂层的活性比表面积和质子电导率等因素控制。 - The experimental results demonstrate that the suitable mea hot - pressing temperature and pressure are 120 and 15 . 5mpa , respectively . the optimum catalyst loading in anode is 4 mg pt / cm2 , and the best contents of nafion ionomer in anode and cathode layer are 45wt % and 35 . 3wt % , respectively
实验结果显示，制备膜电极时最佳的热压温度和压力分别为120和15 . 5mpa ；阳极催化剂的适宜载量为4mgpt / cm2 ；阳极和阴极催化剂层的nafion最优含量分别为45 . 0wt %和35 . 3wt % 。