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Vast sea in a beautiful ball to over the ascension of hydrogen, vapor ...... for the dull sky adds a touch of brilliant color, eye along the slide at the end of the ball of hydrogen, you will find that the ball was a hand-held hydrogen slim girls.

茫茫人海中,一只漂亮的氢气球向上空升腾、升腾……为乏味的天空添加了一抹绚丽的色彩,眼光顺着氢气球滑到尽头,你便会发现手持氢气球的是一位亭亭玉立的少女。

Phosphor change 1.2 helminthic agents steel of aluminous tablet; is bottled carbon dioxide gas. 1.3 circumfluent equipment and tray of testing instrument stainless steel a certain number of;CHXY100/65-Ⅲ movable type are circumfluent detector of chroma of gas of phosphine of;HL-210 of equipment of fuming or steaming-treating diseases with fumes as in moxibustion or with steam generated by boiling medicine herbs. 2 experiments method 2.1 install bug basket and dot of phosphine gas sampling to offer bug trying a storehouse to be mixed in experiment storehouse respectively contrast collect inside the storehouse, choose, every storehouse cent installs 3 bug basket, place respectively in: Pay Yan Xing bing4 ru4 gao1huang1 ③ of number of place of the 4m below cover of food of northeast part of caboodle of grain of; of ② of number of the 2m below cover of food of part of southeast of caboodle of grain of; of ① of number of this Chang?

两仓熏蒸试验时的条件见表1.1.2杀虫药剂56%磷化铝片剂;钢瓶装二氧化碳气体。1.3环流设备和检测仪器不锈钢托盘若干;CHXY100/65-Ⅲ移动式环流熏蒸设备;HL-210磷化氢气体浓度检测仪。2试验方法2.1设置虫笼和磷化氢气体取样点供试仓虫分别在试验仓和对照仓内采集、筛选,每仓分装3个虫笼,分别放置在:粮堆中心粮面下50cm编号①;粮堆东南角粮面下2m编号②;粮堆东北角粮面下4m处编号③。

Installing a desiccator in hydrogen system of turbo generator has become a necessary method to reduce hydrogen humidity in generator sets.

在氢气系统中加装干燥设备已成为降低汽轮发电机组内氢气湿度的一种必要手段。

Hydrogen gas, as a refrigerant of the dynamotor, can increase the efficiency of generating electricity.

氢气作为发电机的冷却剂可以有效地提高其发电效率,而氢气参数处于正常范围内更是保证发电机高效、安全正常工作的必要条件,所以对发电机系统氢气参数的实时监测可以实现对发电机运行的必要而且有效的实时状态评估。

Design of a solar based hydrogen generation system with a fuel cell/electrolyzer to generate hydrogen during the day and use it in the evening, or for transportation.

设计一个以太阳能为基础之包含有燃料电池/电解池的氢气产生系统,这个系统白天产生氢气用在傍晚或用来输送。

We get the optimum process scheme which is suitable for the unit, through analysising and comparising different absorption schemes in the incipience of running of PSA. As to different operation conditions during pressure swing absorption actual operating, we propose to refer absorption cycle time, hydrogen yield and recovery rate as target of process characteristic, study and find out the interrelation between process parameters which influences each other and controls guideline; Through optimizing process conditions, we find out the best operation clicking in actual production, then confirm the best range of absorption cycle time, which make hydrogen yield of plant, hydrogen products purity and hydrogen recovery rate come up to the production requirement at the same time.

通过装置运行初期对不同吸附方案的分析、比较,选出适合本套装置的最优方案,针对变压吸附实际运行过程中的不同生产条件,提出了吸附时间、氢气产量和氢气回收率作为工艺条件研究的主要对象,找出相互影响的工艺参数和控制指标的相互关系;通过对工艺条件的优化,找出实际生产中最佳操作点,确定吸附时间的最佳范围,使装置氢气产量、氢产品纯度和氢气回收率同时满足生产要求,并对影响氢气回收率的其他因素进行了阐述,对优化操作提出建议。

The structure and morphology of CNTs which have been purified and not yet, were characterized by TEM, SEM, XRD, Raman, TG-DTA, BET, IR. The results indicated that when the stokehole reaction temperature was 1170℃,the decompose temperature of Ferrocene was 150℃,he volatilize temperature of Benzene was 50 ℃, hydric flow rate was 270ml/min, the concentration of thiophene was l% and the reaction time was 20 minutes, the CNTs with single-walled and multi-walled were prepared.

结果表明:炉膛反应温度1170℃、二茂铁的分解温度150℃、苯的挥发温度50℃、氢气的流量270ml/min、噻吩体积分数1.00/100ml苯、反应时间20min时,可以得到碳纳米管,既有单壁管又有多壁管,单壁管的内径分布在0.88~1.15nm之间,多壁管的直径分布在40~120nm之间;纯化后的碳纳米管比表面积增加,管壁光滑,而且产生了大量的含氧官能团,有利于在水溶液中的分散。

The structure and morphology of CNTs which have been purified and not yet, were characterized by TEM, SEM, XRD, Raman, TG-DTA, BET, IR. The results indicated that when the stokehole reaction temperature was 1170℃,the decompose temperature of Ferrocene was 150℃,he volatilize temperature of Benzene was 50 ℃, hydric flow rate was 270ml/min, the concentration of thiophene was 1% and the reaction time was 20 minutes, the CNTs with single-walled and multi-walled were prepared. The diameters of the single-walled CNTs are in the range of 0.08~1.15nm, and that of the multi-walled CNTs are in the range of 40~120nm.

结果表明:炉膛反应温度1170℃、二茂铁的分解温度150℃、苯的挥发温度50℃、氢气的流量270ml/min、吩体积分数1.00/100ml苯、反应时间20min时,可以得到碳纳米管,既有单壁管又有多壁管,单壁管的内径分布在0.881.15nm之间,多壁管的直径分布在40120nm之间;纯化后的碳纳米管比表面积增加,管壁光滑,而且产生了大量的含氧官能团,有利于在水溶液中的分散。

This paper first presents a review of the existing hydrogen delivery methods. Then a study is made of the delivery cost, energy consumption and the safety of hydrogen transportation by tube trailer, tank and pipe.

首先结合文献定性介绍了现有氢气运输方式,然后对氢气通过长管拖车、槽车及管道运输的运输成本、能源消耗及安全性进行深入研究。

With fuels of hydrogen and hydrogen-ethylene mixture in the wind tunnel heater, experiments to study hydrogen combustion in scramjets were carried out.

本文选择氢气及氢气-乙烯混合气体两种燃料在风洞加热器中加热空气来开展氢气燃烧的研究实验。

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