英语翻译1.Modified polyol synthesis of PtRu/C for high met

英语翻译
1.Modified polyol synthesis of PtRu/C for high metal loading and effect of post-treatment
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2.MEA fabrication and single-cell performance measurements
The catalysts tested in the present study were applied as anode
catalysts and a commercial Pt black catalyst (Johnson Matthey)
was applied as the cathode catalyst.The catalyst-coatedmembrane
(CCM) was constructed by spraying the catalyst ink directly on to
the polymer electrolyte membrane.Nafion 115 was used as the
membrane,and the catalyst loadingwas 1.5mg cm−2 on both sides
of the membrane.Anode and cathode gas-diffusion layers were
then placed on both sides of the CCM [13].Polarization curves for
each MEA were measured in individual 5 cm2 cells.The MEA was
placed between two gas-diffusion layers (GDLs),inserted into two
graphite plates that contained a serpentine flow-field,and then
assembled at a uniform torque.The single cell was then connected
to a fuel cell test station (FCTS,WonATech Co.,Ltd.) that consisted
of a methanol pump,a mass flow controller,and electrical heaters
to control the temperature.A 1M methanol solution and air were
fed respectively into the anode and cathode sides of the single cell
to measure the performance of the MEA.The feed rate of the 1M
methanol solution and air were 1 and 90mlmin−1 for the anode
and cathode,respectively.The temperature of the single cell was
maintained at 60 ◦C [14].

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1.论文题目 Modified polyol synthesis of PtRu/C for high metal loading and effect of post-treatment
用于高金属沉积和后处理效应的PtRu/C的改进多元醇合成
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2.MEA fabrication and single-cell performance measurements
MEA（薄膜电极接合体?）的制造和单（电）池性能的测量
The catalysts tested in the present study were applied as anode
catalysts and a commercial Pt black catalyst (Johnson Matthey)
was applied as the cathode catalyst.本研究中试验的催化剂被用作阳极催化剂,而一种商品级的铂黑催化剂（Johnson Matthey公司出品）被用作阴极催化剂.PtThe catalyst-coated membrane(CCM) was constructed by spraying the catalyst ink directly on to
the polymer electrolyte membrane.由催化剂涂覆的隔膜（CCM）通过将催化剂油墨直接喷涂到聚合物电解质隔膜上而构成.Nafion 115 was used as the
membrane,and the catalyst loadingwas 1.5mg cm−2 on both sides
of the membrane.Nafion115被用作隔膜,催化剂的沉积为隔膜两面各1.5mg cm−2.
Anode and cathode gas-diffusion layers were
then placed on both sides of the CCM [13].然后阳极和阴极气体扩散层被置于CCM的两面.Polarization curves for each MEA were measured in individual 5 cm2 cells.在单独的5cm2电池上测量每个MEA的极化曲线.The MEA was
placed between two gas-diffusion layers (GDLs),inserted into two
graphite plates that contained a serpentine flow-field,and then
assembled at a uniform torque.MEA被放置在插入两块石墨板两个气体扩散层（GDLs）之间,石墨板包含迂回曲折的流动场,然后以均匀的转矩组装.The single cell was then connected to a fuel cell test station (FCTS,WonATech Co.,Ltd.) that consisted
of a methanol pump,a mass flow controller,and electrical heaters
to control the temperature.然后将单池连接到燃料电池试验站（FCTS,WonATech Co.,Ltd.公司出品）,试验站有一台甲醇泵、一台热质流量控制器和若干控制温度的电加热器.A 1M methanol solution and air were fed respectively into the anode and cathode sides of the single cell to measure the performance of the MEA.将1M的甲醇溶液和空气分别送入单池的阳极侧和阴极侧,以测量MEA的性能The feed rate of the 1M
methanol solution and air were 1 and 90mlmin−1 for the anode
and cathode,respectively.The temperature of the single cell was
maintained at 60 ◦C [14].1M的甲醇溶液和空气的馈送速度对阳极和阴极分别为1 和 90mlmin−1.单池的温度保持在60 ◦C