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The way of the formation of methane through CO2/H2 reduced, the main origin of hydrogen elements are from production of anaerobic degradation of organic matter in the role of the hydrogenase with biohydrogen-bacterium.

对于CO2(H2)还原途径形成的甲烷,元素主要来源于产菌在化酶的作用对有机质的厌氧降解。

The results also indicate that the Ph stability and the concentration of N exert a great influence on the growth of C reinhardtii- se and the acetic acid is the key substance for hydrogenase induction.

综合考虑两步法产对细胞生长周期和细胞密度的要求以及最终厌氧诱导获得的酶活性,最终选择seTA培养基作为莱茵衣藻- se 产用培养基。

Types of hydrogenase are reviewed,i ts applications have found its appli cations,such as biohydrogen production,wastewater treatment,prevention of microbial-induced corrosion,generation and regeneration of NADP cofactors.

介绍了化酶的类型,讨论了化酶在生物制、废水处理、预防微生物腐蚀、NADP辅因子的产生及其再生等生物技术领域中的应用。

This paper reviews recent developments in the design and assembly of hydrogenase-modified electrodes, wherein the enzyme was immobilized by physical adsorption, self-assembly, sol-gel and Langmuir-Blodgett methods. Electrochemical properties of hydrogenase in the molecular assemblies and biohydrogen production are discussed.

本文综述了酶及其分子聚集体薄膜在电极表面的组装技术,如吸附法、自组装法、Langmuir-Blodgett法和溶胶-凝胶法等,并讨论了分子聚集体薄膜中酶的结构、生物活性、电化学性质及其在催化产方面的应用。

Using the length of cells' growth cycle,the density of cells and the activity of induced hydrogenase as criteria,the optimal formulation of culture medium was obtained as seTA(se -Tris Acet) which contains acetic acid as C source,higher concentration of N and stronger pH buffer system based on the se formulation.

结果发现,培养基的pH和氮素的含量是影响莱茵衣藻生长的重要因素;而培养基中醋酸根的含量则有助于提高厌氧产过程中衣藻的酶活性,从而提高其产量。

The catalyst was applied to hydrogenateα-octene in normal temperature and pressure, the conversion ofα-octene was 98.6%, and the yield of octane was 63.1% by the bimetallic catalyst.

CTS-ACRPd用于常温常压下α-辛烯的催化化,并在催化化过程中添加Ni~(2+),Ni~(2+)-pd双金属催化剂催化α-辛烯的加反应150 min时α-辛烯的转化率为98.6%,正辛烷产率63.1%。

The additional activity of the mechanical mixture can be ascribed to the acid sites on dealuminated Y zeolite, where the activated hydrogen spilt over from the neighboring Pt sites could hydrogenate the adsorbed benzene with the formation of cyclohexane and methylcycloheptane.

发现虽然Y沸石本身没有加活性,但它的加入可以显著提高Pt/Al2O3的活性,因为在Pt中心上得到活化的可以快速溢流到邻近的沸石颗粒表面的酸中心上,并和吸附在其上的苯发生加反应生成环己烷和甲基环戊烷。

Hydrogenation of N=O group is easier than hydrogenolysis of the C-Cl bond on the hydrogenation of chloronitrobenzene .

氯代硝基苯中N=O极性键的加较C-Cl键的解容易进行,肉桂醛中C=O极性键较C=C键的加难。

Hydrogenolysis results show that the activity and selectivity of methanol produced from synthesis gas are smaller than those from pure H2.With increasing reaction temperature,the activity of methanol synthesis increases gradually,with simultaneously speeding up of side reactions.

结果表明,合成气解反应活性和甲醇选择性明显低于纯解反应活性和甲醇选择性,反应温度高对提高催化剂活性有利,但同时也加速了副反应的进行。

Above all, schematic ground introduced the development existing state of affairs of economy of foreign hydrogen the sources of energy, right the United States, Canada, Europe, Japan, Korea, Brazil, Icelandic the existing state of affairs of hydrogenous economy progress that waits for different type country and area with Norway undertook an analysis, the characteristic; that pointed out they are respective next, review and analysed economy of our country hydrogen to develop course and current situation, the place; that summed up inadequacy is final, on the foundation of afore-mentioned analysises, put forward to suggested at 5 o'clock to the development of economy of our country hydrogen.

首先,概要地介绍了国外能源经济的发展目前状况,对美国、加拿大、欧洲、日本、韩国、巴西、冰岛和挪威等不同类型国家和地区的经济发展目前状况进行了分析,指出了他们各自的特色;其次,回顾并分析了我国经济发展历程和目前状况,总结了不足之处;最后,在上述分析的基础上,对我国经济的发展提出了5点建议。

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