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catalyst相关的网络例句

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Among them, the glue solvent addition-nitric acid had a greater impact, and its amount was controled at 8%~10% for the best; 2though the result of the ball catalyst prepared by oil ammonia column was better, the process was more complex; 3performance of the catalyst prepared by impregnation ball support was poor.

其中,胶溶剂硝酸的加入量有较大影响,其用量控制在8%~10%为最佳;2油氨柱滴球成型法制得的球形催化剂虽然齐聚反应效果较好,但工序较复杂;3浸渍球形载(来源:A61BcacaC论文网www.abclunwen.com)体法制得的催化剂催化性能较差。

Underoptimal conditions, in toluene / dimethyl phthalate / TBP, after EAHQ was oxidizedwith 〓, then the catalyst and styrene were added, the conversion of styrene basedon EAHQ is 68%, the selectivity for styrene oxide based on styrene is 92% and theTON of the catalyst is 500; in toluene / phenyl ether / TBP, epoxidation of styrenewas performed with 〓 generated in situ, the conversion is 46%, the selectivity is94% and the product can be separated by distillation under reduced pressure.

优化条件下,甲苯/邻苯二甲酸二甲酯/TBP(2/2/1,体积比)中,EAHQ先用〓氧化完全后,再加入催化剂A和苯乙烯进行环氧化反应苯乙烯相对于EAHQ的转化率为68%,生成环氧苯乙烷的选择性为92%,催化剂A的TON达到500;甲苯/二苯醚/TBP(1/3/1,体积比)中,原位生成〓条件下苯乙烯相对于EAHQ的转化率为46%,生成环氧苯乙烷的选择性为94%,产物可通过减压蒸馏分离。

Effects of mass ratio of reactants,catalyst dosage,reaction time,reaction temperature and catalyst reuse were discussed.

考察了反应物质量比、催化剂用量、反应时间、反应温度和催化剂重复使用等因素对反应的影响。

In esterification of 2,6-NDA obtained from Henkel reaction of 1,8-naphthalenedicarboanhydride catalyzed non-cadmium catalyst zinc carbonate, the effect of process parameters like esterification catalyst and its amount used, reaction temperature and time, and methanol/anhydride molar ration, etc, was investigated.

在碳酸锌催化和二氧化碳气氛中1,8-萘二甲酸酐于300~340℃反应3~4小时,可以较高收率地获得2,6-萘二甲酸粗品,收率达到62%,该产物可以直接用于合成双酯的酯化反应中。

In the preparation method, primary soybean oil and deep hydrogenation soybean oil, or primary rapeseed oil and deep hydrogenation rapeseed oil are adopted as raw materials; sodium methoxide is selected as a catalyst; the consumption of the catalyst is 0.1 percent to 0.5 percent; the reaction temperature is 70 DEG C to 110 DEG C; therefore, the primary soybean oil and the deep hydrogenation soybean oil, or the primary rapeseed oil and the deep hydrogenation rapeseed oil have randomized lactide reaction for 10 min to 90 min, so as to change the composition of mixed oil triglyceride and obtain the low/zero trans fatty acid base oil with different melting points and the characteristics of solid fat.

本发明以一级大豆油和极度氢化大豆油,或一级菜籽油和极度氢化菜籽油为原料,选择甲醇钠为催化剂,催化剂用量0.1%~0.5%,反应温度70~110℃,使一级大豆油和极度氢化大豆油,或一级菜籽油和极度氢化菜籽油之间进行随机交酯化反应,反应时间10~90min,从而改变混合油甘三酯组成,得到具有不同熔点和固体脂肪特征的低/零反式脂肪酸基料油。

Kinetic investigation about Pt/TiO〓 catalyst and adding transition metal, rare-earth metal to Pt/TiO〓 catalyst on the hydrogenation of CNB.

初步探讨了Pt/TiO〓催化剂以及添加过渡金属和稀土金属催化剂上氯代硝基苯催化加氢的反应动力学。

The invention relates to a rare-earth metal oxide supported transition metal or transition metal alloy catalyst and the method of on the catalyst, using alcohol or alcohol water solution catalytic chemical deposition to prepare nano carbon fiber and 3D order nano carbon stacking structure.

本发明涉及一种稀土金属氧化物担载过渡金属或过渡金属合金催化剂及利用在该催化剂上,乙醇或乙醇水溶液催化化学沉积制备纳米碳纤维和三维有序纳米碳纤维堆积结构的方法。

It is demonstrated that, in one aspect, in-situ zeolite has more effective catalytic capability based on unit active site, in another aspect, it has excellent ring-open activity as so called in-situ type hydrocracking catalyst can produce tail oil with generally 2-3 unit lower than traditional hydrocracking catalyst on BMCI index.

实验结果表明,原位分子筛材料不仅表现了具有更高本征催化效率的特点,而且突出表现了优异的开环裂解性能,所涉及的所谓原位型加氢裂化催化剂能获得比常规催化剂低2~3个单位的低BMCI值尾油。

Due to the suppression of reverse water gas shift reaction by adding steam in feed gas, more CO〓 participated in and promoted CO〓 reforming of CH〓 reaction, higher catalytic activity and less carbon deposition were obtained. On the surface of used catalyst there were two kinds of carbon species deposited on catalyst, one was decomposed CH〓 fragment, and the another was graphiticlike carbon.

在反应后催化剂表面有两类碳物种,一类在250~350℃出现的少量α-碳,应主要是活性高的CH〓解离碎片,一类是在700℃附近出现的β-碳,应是导致催化剂失活的类石墨化碳。

A Ni/Ce-Zr-Al-Ox catalyst was prepared by hydrothermal synthesis-impregnation method. The CO2 reforming of CH4 reaction was performed. By XPS and TPH methods the carbon species deposited on the surface of catalyst during the reaction were characterized; The effect on the carbon deposit by adding a small amount of steam in feed gas and the interaction between steam and carbon species were studied.

采用水热合成-负载法制备了Ni/Ce-Zr-Al-Ox催化剂,进行了CO2重整CH4的反应,并采用X射线光电子能谱、程序升温加氢等方法表征了在反应过程中催化剂表面的积碳物种,考察了添加少量水蒸汽对积碳的影响以及水蒸汽和表面积碳物种的作用。

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The above mentioned teaching model of spiral rising can be used to avoid rigidness in teaching.

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