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1.Intrinsic kinetics of CO shift reaction over BX HTS catalyst
BX型中温变换催化剂上CO变换反应本征动力学研究收藏指正
2.Study on pressured CO shift reaction kinetics on cobalt-molybdenum series catalysts
钴钼系催化剂一氧化碳加压变换反应动力学研究收藏指正
3.CO Oxidation and Low Temperature Water-gas Shift Reaction Over Supported Gold-base Catalysts
负载型金基催化剂上CO氧化和水煤气变换反应性能研究收藏指正
4.The dehydrogenation of ethane was enhanced by CO2 because of the existence of the reverse water gas shift reaction and the Boudouard reaction.
由于存在逆水煤气反应和Boudouard反应,CO2能显著促进乙烷的脱氢反应.收藏指正
5.As CO_2,to a certain extent,inhibits the shift reaction rate,some way must be found to reduce the adverse effect of CO_2in order to increase the shift reaction rate.
CO2对变换反应速率还是存在一定的抑制,因此为提高变换反应速率,应当设法减小CO2的不利影响;收藏指正
6.THE TPD STUDY OF CO FROM THE Cu/ZnO/AI_2O_3 CATALYST FOR LOW TEMPERATURE SHIFT REACTION
CO在Cu/ZnO/Al_2O_3型低变催化剂上的TPD研究收藏指正
7.Study on Intrinsic-Kinetics Equations of CO Shift Reaction on Basf’s K_(8-11) Catalyst
BASF　K_（8－11）催化剂一氧化碳变换反应动力学研究收藏指正
8.A side-stream experiment of SX-1type Cu-based catalyst for high temperature shift reaction of CO with low steam to carbon ratio
SX-1型低汽气比铜系CO高温变换催化剂侧流试验收藏指正
9.XPS data indicated that a better dispersion of Mo and less Mo~(6+)formed during water gas shift reaction on the La-promoted catalyst.
XPS测定结果发现La助化的催化剂在反应时,其Mo可以保持较好的分散和较少形成Mo~(6+),而Mo~(6+)对反应是无活性的。收藏指正
10.Using an inner recycle non=gradient reactor at 205～290℃,0. 15～1. 2 MPa,the CO shift reaction kinetics data on cobalt-molybdenum sulfur-tolerant catalySt B301 were measured, and the power function equation of kinetics was determined. With the experimental data the influence of reaction temperature and CO conversion rate on efficiency factor has been reckoned up.
本文利用内循环无梯度反应器在温度、压力分别为205～290℃及0．15～1．2MPa范围内，测定了一氧化碳变换反应在B301型钴钼耐硫变换催化剂上的反应动力学数据，确定了幂函数型动力学方程．并由实验数据计算了反应温度及CO变换率对效率因子的影响。收藏指正
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