1) hydrogen refueling station
加氢站
1.
Therefore it is urgent to build a mini-network of hydrogen refueling stations to serve those vehicles.
在2008年之前,上海的燃料电池汽车数量将达到百辆级规模,为了示范运行这些车辆,迫切需要建立一个有若干个加氢站组成的小型网络来提供加氢服务,为此需要确定投资运营成本。
2.
The results can provide reference for equipment design on occasions which has requirement for initial temperature such as in design of hydrogen refueling stations.
研究结果可以为加氢站等对于初始温度有要求场合的设计提供参考。
3.
With the world wide development of large-scale FCV demonstration projects, the global number of hydrogen refueling stations has increased rapidly in recent years.
伴随着世界各国氢燃料电池车示范项目的实施,与之配套的氢能基础设施——加氢站也在全球范围内迅速发展。
2) Hydrogen fueling station
氢加注站
3) mobile hydrogen refueling station
移动加氢站
1.
A brief introduction of current situation of mobile hydrogen refueling station; analyzed essential parts off illings ystema nd principles;p roposedt hreed ifferent filling patternsa ccordingt or equiredf illingp ressure; under hydrogen real gas state equation, calculated consecutivef illingc apabilitya ndu ltimatef illingc apability of mobile hydrogen refueling station of example.
介绍了国内外移动加氢站的发展现状,分析了加注系统的主要组成部分及工作原理,针对不同的加注压力,提出了三种不同的加注模式,运用氢气真实气体状态方程计算了移动加氢站的连续加注能力和极限加注能力。
4) hydrogenation
[,haidrədʒə'neiʃən]
加氢
1.
Advance and trend in glucose hydrogenation catalysts for sorbitol;
葡萄糖加氢催化剂研究现状及发展趋势
2.
Supported nickel catalyst for hydrogenation of p-nitrophenol to p-aminophenol;
负载型Ni催化剂上对硝基酚加氢合成对氨基酚的研究
3.
Modification of the Cu-Zn catalysts supporred on γ-Al_2O_3 for hydrogenation of furfural to furfuryl alcohol;
糠醛加氢制糠醇中γ-Al_2O_3负载Cu-Zn催化剂的改性研究
5) Hydrofining
['haidrə,fainiŋ]
加氢
1.
Analysis Quality and Profit of Wax Hydrofining Production;
白土预精制在蜡加氢生产中效益分析
2.
Trial manufacture and application of LH-3 diesel oil hydrofining catalyst;
LH-03柴油加氢改性催化剂的试生产和应用
3.
Reformation of Feeding Pump for 4×10 5 t/a Hydrofining Unit;
40万吨/年加氢精制装置进料泵改造
6) hydrotreating
加氢
1.
Comparison of residue oil ebullated-bed hydrotreating processes in China and abroad
国内外渣油沸腾床加氢技术的比较
2.
The effect of the pH of impregnating solution and the use of additives on the chemical and physical properties of Co-Mo/Al 2O 3 hydrotreating catalyst were discussed.
讨论了浸渍溶液pH以及在浸渍溶液中添加助剂等对Co -Mo加氢催化剂物化性质的影响 ,调整浸渍溶液 pH可以改变催化剂孔结构 ,在浸渍溶液中添加助剂可以改善活性金属在加氢催化剂表面的分布。
3.
Effects of Na +,heavy metal nickel and vanadium,sulfur and viscosity of residue on activity of catalyst for S-RHT were investigated on a residue hydrotreating pilot unit.
在中型渣油加氢试验装置上考察了钠离子、镍、钒、硫和渣油粘度对S-RHT催化剂活性的影响。
补充资料:宾加水电站
宾加水电站 |
Binga Hydropower Station |
概 述 |
宾加水电站位于菲律宾吕宋岛的阿格诺(Angno)河上。工程主要用于发电。塑性斜心墙堆石坝,最大坝高107.4m,水库总库容0.482亿m3,水电站装机容量10万kW。工程于1957年开工,1959年完工。 |