The invention relates to a regenerating method of an acidic gas catalyst filtering material and a device thereof.
本发明是有关一种酸性气体触媒滤材的再生方法及其装置。
It is a new and efficient gas catalyst can maintain high activity and capacity at normal temperature and pressure.
它是一种新型高效的气体催化剂，能在常温、常压下保持较高的活性与容量。
Hydrogen was a gas catalyst in the reactions, and it was useful for hydrogen to synthesis of C2 hydrocarbons by dehydrogenation coupling reactions of methane.
在该偶联反应中，氢气是一种气体催化剂，它的加入有助于甲烷的脱氢偶联转化制备C2烃。
Combined with another catalyst, such as platinum, that can produce hydrogen gas from water, the system can duplicate the water splitting reaction that occurs during photosynthesis.
结合上其他从水中产生氢气的催化剂如铂，这个系统就能复制在光合作用中所发生的水分解反应。
This allows the catalyst to break down the remaining methane into solid carbon and hydrogen gas.
这使得催化剂能将余下的甲烷分解成固体碳和氢气。
The key component in the process is a catalyst -- cobalt metal, phosphate and an electrode, placed in water -- that produces oxygen gas from water, while another catalyst produces hydrogen gas.
研究人员解释说，这个流程的关键组成成分是一个催化剂-放置在水中的钴金属、磷和电极-这个催化剂从水中产生氧气，另一个催化剂产生氢气。
It does this by combining CO2 with natural gas in the presence of a proprietary metallic catalyst it has developed and licensed.
方法是利用一种金属催化剂，将二氧化碳与天然气混合。这种催化剂是他们公司发明并注册的。
Invented by Italian engineer Andrea Rossi, the E-Cat is designed to create heat from a simple combination of hydrogen gas, powdered nickel, and an undisclosed catalyst.
由意大利工程师安德里亚∙罗西发明，E -Cat能够利用氢气、镍粉及一种未公开催化剂的简单组合生成热量。
No need Baking Soda as a catalyst that will increase in gas output in the same time increasing temperature to dangerous condition.
无需烘烤条件纯碱作为催化剂，同时将增加天然气产量的温度升高到危险的时候。
It is prepared by reacting anhydrous ammonia and carbon dioxide gas under very high pressure in the presence of a suitable catalyst.
它是在某种催化剂参与下，由无水氨和二氧化碳气体在高压条件下反应生成的。
By employing the catalyst and nanoparticle layers as bottom and top electrodes respectively, the researchers successfully designed and tested a gas sensor.
通过分别以催化剂层和纳米颗粒层分别作为底部电极和顶部电极，研究人员成功地设计了一个气体传感器并测试了其传感性能。
Take gas diffusion electrode of zinc-air battery for example and add catalyst by layers, we studied the effect of changing catalyst layer location on the performance of gas diffusion electrode.
以锌空气电池气体扩散电极为研究对象，采用分层添加催化剂的方式研究了改变催化层位置对气体扩散电极放电性能的影响。
The difference of gas diffusion regularity between moving bed and fixed bed enlarged with the increase of catalyst recycle intensity.
随着催化剂循环强度的增加，移动床与固定床在气体扩散规律上的偏离程度增大。
The gas solid contact efficiency was improved by adjusting the flow tracks of catalyst.
通过改变催化剂的流动轨迹达到改善气固接触效率的目的。
This paper describes the experiment of producing ethylene oxide (EO) by using ethylene recovered from catalytic cracking dry gas in the presence of ys silver catalyst.
叙述了在YS型银催化剂作用下，利用催化裂化于气回收的乙烯制备环氧乙烷的实验研究。
The result indicates that the ferric citrate catalyst is effective to deal with H_2S highly concentrated refinery gas.
实验结果表明，应用柠檬酸铁催化剂处理含高浓度H_2S炼厂气，该方法是行之有效的。
Combining the chemical cleaning and air blasting method, this paper introduces a new method of removing the deposit resulting from the shift gas and catalyst powder, etc.
采用化学清洗和空气爆破相结合的方法，清除换热器中由变换气及催化剂粉末等形成的垢物，降低换热器的阻力，提高热效。
Nibased industrial catalyst has been introduced into hot gas cleanup study for removal of ammonia, coal tar and organic sulfur compounds in high temperature gas.
选用了一种工业镍基催化剂，它具有同时脱除热煤气中氨、有机硫和煤焦油蒸气的多种净化功能，而且能达到较高的净化效率。
The biomass was also liquefied in the others solvent at high temperature and high pressure in the presence of other catalyst with other reducing gas.
初步进行了其他不同溶剂、不同催化剂以及还原气体的木质生物质直接液化研究。
The results showed that both carbon conversion and gas composition were strongly influenced by the catalyst content and reaction temperature.
实验结果表明，催化剂添加量和气化温度对碳转化率和煤气组成的影响最为显著。
Development and commercial application of domestic gas phase polyethylene BCS02 slurry catalyst were described and comparison of it with other polyethylene catalysts was discussed.
介绍了国产BCS02型浆液聚乙烯催化剂的开发和工业应用情况，并与其它同类型催化剂进行对比。
Based on the special requirements towards catalyst for converting natural gas to city gas intermittently, the development of corresponding catalyst is conducted.
基于天然气间歇转化制城市燃气对催化剂的特殊要求，开展了相应催化剂的研究制备工作。
The key of the CO shift process is applying sulfidation resistance shift catalyst, so that the feed gas with sulfide can be shifted directly without removing sulfide.
工艺关键是使用耐硫变换催化剂，使气化后的含硫工艺气不经脱硫而直接进行变换。
The application, reaction mechanism and selection of liquid or gas atmospheric temperature arsenic removal catalyst in olefin unit are introduced in the article.
介绍液态或气态常温脱胂催化剂在烯烃工业中的应用、反应机理及其选用。
The activation ambience, reaction temperature, catalyst's send live time, gas flow rate were used to study the best catalyst.
对最优催化剂进行了活化气氛、反应温度、催化剂致活时间、反应气流速等方面的考察。
Regeneration of the deactivated catalyst was conducted by passing carrier gas at given temperature through the catalyst, resulting in the recovery of its initial activity.
同时进行了催化剂的再生研究，在载气下于一定温度将催化剂热再生，基本上可恢复催化剂的活性。
The formation of camphor from the catalytic dehydrogenate of isoborneol in gas phase was investigated and catalyst CDH has been selected.
本文研究了异龙脑气相催化脱氢生成樟脑过程，筛选出催化剂金属氧化物CDH。
The height computation model of fluidize-bed showed that the bed height is mainly influenced by catalyst filling amount, linear speed of reaction gas and particle size of catalyst.
流化床高度计算模型表明，床层高度主要受催化剂装填量、反应气体线速和催化剂粒度的影响。
The height computation model of fluidize-bed showed that the bed height is mainly influenced by catalyst filling amount, linear speed of reaction gas and particle size of catalyst.
流化床高度计算模型表明，床层高度主要受催化剂装填量、反应气体线速和催化剂粒度的影响。
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