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Under the optimal conditions, the conversion of reactant and the yield of H_12MDA are both as high as 100% with content of trans-trans isomer being lower than 10%.

在优化的反应条件下,可以实现MDA的转化率和全加氢产物收率均是100%,反-反异构体含量低于15%,最低可以达到5%。

The effects of the preparation and reaction conditions on the conversion and isomerization selectivity of n-heptane were studied carefully.

详细讨论了催化剂的制备条件和反应条件的改变对正庚烷的转化率和异构化选择性的影响。

The selected prepared catalyst for isomerization of light oilis used under the reaction conditions of 260°C, 2.0MPa, WHSV=1.0h-1 , H2/Hydrocarbon molarration 4.0, n-pentane conversion rate is 62.17%,isopentane yield is 57.01%(isomerization rate is58.00%), isopentane selectivity is 91.60%, liquid product yield is 94.84%.

在 T=260°C,P= 2.0MPa ,WHSV= 1.0h-1 ,H/C5= 4.0 时,正戊烷转化率为 62.17%,异戊烷收率为 57.01%(产率为58.00%),选择性为 91.60%,液体产物收率为 94.84%。

Ethanol production by fed-batch fermentation was investigated and the maximum ethanol concentration of 94.81 g/L, equivalent to 81.54% of its theoretical value, was reached with final Jerusalem artichoke flour of 300 g/L in a 5 L jar fermenter.

在此基础上,对菊芋粉补料发酵进行了试验,补料至菊芋粉终浓度为300 g/L,发酵终点乙醇浓度为94.81 g/L,理论转化率为81.54%。

It was tested that the lymphocyte transformation rate of experimental group and of control group at 48,72 and 96 hours ,after bleeding and separating leukocyte,chicken infectious laryngotracheitis standard virus as stimulus.

在48、72和96小时采血分离白细胞,以鸡传染性喉气管炎标准毒做刺激剂,检查试验组和对照组淋巴细胞转化率

The efficiency of surfactant was evaluatedby measurement of the polymerization kinetics, the conversion of MMA, the amount of thecoagulation, the surface tensteon of the miniemulsion before and after polymerization, andthe particle size and particle size distribution of obtained lattice.

通过对聚合反应的动力学,单体MMA的转化率,凝结物的生成量,细乳液聚合前后的表面张力,及所得乳胶粒子的粒径和粒径分布的表征,评价了大分子乳化剂在RAFT细乳液聚合中的效率。

It was found that the catalysts with 1.5% Pd content showed a higher activity. At 60—65℃ and 0.6MPa with a total catalyst amount of 0.5%,the conversion of dehydrolinalool was higher than 99% and the selectivity for linalool was higher than 96%. The change in catalyst composition upon reused for 7 times was evaluated by using ICP,and the effect of Pb and Bi to the catalytic behavior was discussed.

结果表明,钯质量分数为1.5%的催化剂活性较高,在反应温度为60~65 ℃,系统压力为0.6 MPa,催化剂用量为原料质量的0.5%,去氢芳樟醇转化率大于99%时,芳樟醇选择性大于96%,催化剂套用7次后,利用ICP对使用前后催化剂的组成进行分析后,根据反应结果分析了Pb和Bi对加氢反应的作用。

The results show that smaller height of reaction channel can shorten the time which reactants diffuse from channel to reaction surface, longer length of micro-channel can extend residence time of reactants on the catalyst surface, and consequently increase the methane conversion and hydrogen production. The pressure drop between inlet and outlet increases lineally with the increasing of length, while the height influences the pressure drop significantly when the height is less than 0.4 mm. Based on the overall consideration for the methane conversion and resistance characteristic generally, the suitable height of channel should be between 0.4 mm and 0.6 mm.

结果表明:较小的通道高度能够减小反应物在通道中的扩散时间,较长的反应通道长度能够增加反应物与催化剂的接触时间,甲烷转化率和产氢率提高;通道长度线性地影响微通道进出口压降的大小,而在通道高度小于0.4mm时,通道高度显著地影响进出口压降的大小;综合考虑微通道的重整性能和进出口压降等因素,通道高度在0.4~0.6mm之间较为合适。

The effects of the reaction temperature,lipase dosage and molar ratio of water/linseed on the reaction rate and conversions were examined.

考察了反应温度、脂肪酶用量、水/亚麻油摩尔比等因素对反应速率及转化率的影响。

The effect of temperature, reaction time ,catalyst on high temperature rapid liquefaction of two kinds of coal .

实验结果表明,在高温短时间内出现较高的煤转化率

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