shift reaction

The kinetics of desorption of H_2O ( g) from Cu-ZnO-Al_2O_3 catalyst of lowtemperature shift reaction was studied by means of temperature programmed desorption ( TPD) technique.

以程序升温脱附（TPD）技术对H2O（g）在Cu-ZnO-Al2O3型低温变换催化剂上的脱附行为进行研究。

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The adsorption and water gas shift reaction mechanism on reduced cerium dioxide

二氧化铈还原表面上水煤气变换反应机理

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The polarization action of glue and thiourea make peak current density of copper deposition reaction decrease and make peak potential shift to more negative direction.

Glue和（NH2）2CS的极化作用使铜沉积反应的峰电流密度降低，峰电势负移；

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The recent literature concerning oxidation of CO, hydrochlorination of ethyne, selective hydrogenation of crotonaldehyde, water-gas shift reaction and reduction of nitrogen oxides on supported gold catalysts is briefly reviewed in this article.

概括地介绍了近期发表的关于金负载催化剂成功地用于催化CO氧化，乙炔氢氯化，丁烯醛选择加氢，水煤气转换和氮氧化物还原等反应的例子。

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The "negative shift" peak for total gas is the normal reaction of the gas with low thermal conductive factor.

全量曲线负漂峰是惠斯顿电桥鉴定器测量低导热系数气体的正常反应，它对判断CO2气体和N2气体的存在有较好的应用价值。

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The Adsorption-Desorption Study for the Low Temperature Water Gas Shift Reaction System by TPD

程序升温脱附法对低变反应体系的吸-脱附研究

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The chemical shift has a close relation with the reaction activeness: the smaller the δ_H value of the alpha position hydrogen in the compound, the higher the electricity substitution activeness.

分子的化学位移与反应活性有密切联系：化合物α位氢原子的δH值愈小，该化合物亲电取代反应活性愈高；

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Effect of Some Rare Earths and Molybdenum on CO Shift Reaction and Surface Behaviour of Ferric Catalyst

稀土和钼对铁系中温变换催化剂反应性能及表面性质的影响

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Intrinsic kinetics of the co high temperature shift reaction over BX catalysts

在BX型中温变换催化剂上CO变换反应本征动力学的研究

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Effects of Charging Method in the Precipitation Process on Iron-based Catalysts for High Temperature Shift Reaction

中和沉淀过程中加料方法对新型铁基CO高变催化剂性能影响的研究

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With the catalyst, the diesel fuel exhaust gas reforming reaction is endothermic, steam reforming reaction and water gas shift reaction are main reaction; partial oxidation reaction is secondary.

没有催化剂时，柴油废气重整反应是吸热反应，水蒸汽重整反应和水煤气反应是主要反应，氧化反应是次要反应。

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Study on Reaction Kinetics of FBD Water-gas Shift Reaction Catalyst

FBD型一氧化碳高温变换催化剂动力学研究

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The experimental results showed that the water gas shift reaction could not reach thermodynamic equilibrium.

在内循环无梯度反应器内研究了C6H12－H2O转化反应的宏观动力学，实验结果表明，实验条件下，水－煤气变换反应并未达到平衡。

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The activated surface oxygen and oxygen vacancy from CeO2-CNT composites play an important role in two-step ODH reaction by promoting reverse water-gas shift reaction.

对于碳纳米管内负载CeO2催化剂，活化的表面氧和氧空穴在这个两步脱氢中通过促进逆水汽反应承担重要的作用。

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Both the water gas shift reaction and the methanation reaction do not reach the thermodynamic equilibrium.

水煤气变换反应和甲烷化反应均未达到平衡；

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