水煤气

含La耐硫水煤气变换催化剂的研究

Study on La-PROMOTED sulfur resistant water gas shift catalyst

采用SEM，XRD，XPS，ESR考察了Co-Mo-K/Al2O3水煤气变换催化剂的结构。

The structure of Co-Mo-K / Al2O3 water gas shift ( WGS ) catalyst ( B302Q ) produced by our Institute has been investigated by SEM , XRD , XPS and ESR .

负载型金基催化剂上CO氧化和水煤气变换反应性能研究

CO Oxidation and Low Temperature Water-gas Shift Reaction Over Supported Gold-base Catalysts

流化床与固定床水煤气CO含量的比较

CO Content of Water Gas from Fluidized-bed or Fixed-bed

生物质气化气要实现高氢浓度的转化，需要通过水煤气变换反应将CO转化为H2。

High concentration hydrogen of the producer gas could be realized through water-gas shift reaction .

当金负载量为3%，水煤气变换反应温度为200℃时，CO的转化率可达995%。

CO conversion reaches 99 5 % at gold loading of 3 % and 200 ℃ .

焙烧温度对Au/Fe2O3Zr-O2水煤气变换催化剂的影响

Influence of calcination temperature on Au / Fe_2O_3-ZrO_2 water-gas shift catalyst

ZnO负载纳米金催化剂上的低温水煤气变换反应

Low-Temperature Water-Gas Shift Reaction over ZnO-Supported Gold Nanoparticle Catalyst

Co－Mo／MgO－Al2O3水煤气耐硫变换催化剂失活的研究

Deactivation of Co-Mo / MgO-Al2O3 Type Water-Gas Shift Catalyst

Co-Mo-K/Al2O3水煤气变换催化剂的失硫与活性

Sulfur Loss and Activity of Co-Mo-K / Al_2O_3 Water Gas Shift Catalyst

Co-Mo-K/Al2O3水煤气变换催化剂结构的研究

Study on the structure of co-mo-k / al_2o_3 water gas shift catalyst

水煤气变换催化剂Co-Mo-K/Al2O3的酸性对活性的影响

Acidity of water gas shift catalyst : co-mo-k / al_2o_3

CO2+O2气化制气配水煤气生产甲醇的构想与可行性分析

Concept and Feasibility Analysis of Methanol Production by Gasification with CO_2 + O_2 and Blending with Water Gas

水煤气发生炉微机监控系统，采用PLC对生产过程进行控制和监测。

In the computer control system of water gas , the process is controlled and monitored by PLC .

Cu/ZnO催化剂上逆向水煤气变换反应反应机理的MonteCarlo模拟

Monte Carlo simulation for mechanism of reverse watergas shift reaction over cu / zno catalyst

制备参数对Au/Fe2O3催化剂水煤气变换性能的影响

Effect of Preparation Parameters on Activity of Au / Fe_2O_3 Catalyst for Water-Gas Shift Reaction

半水煤气脱硫塔出口气H2S含量超标原因分析及处理措施探讨

Analysis of Causes and Dealing Measures Discussion of High H_2S Content Purified Gas of Desulphurizing Tower

水煤气变换催化剂Fe3O4的亚稳结构

Metastable Structure of Fe_3O_4 for Water - Gas Shift Catalyst

基于PLC与PC打印口通信的水煤气发生炉微机监控系统

The Computer Control System of the Water Gas Generating Boiler based on the Communication between PLC and the Printer Port of PC

不同金属催化水煤气变换反应活性的DFT研究

DFT studies of activity of water gas shift reaction by several metals catalyzed

助剂对低温水煤气变换反应Au/α-Fe2O3催化剂性能的影响

Effect of promoter on the performance of low-temperature water-gas shift reaction in H_2-rich steam over supported gold catalyst

试验征明，反应的初次产物是CO，而CO2是由水煤气转换反应生成的。

It has been confirmed that the primary product is carbon monoxide , and the carbon dioxide formed is produced by shift - reaction .

微乳法制备Au/Fe2O3水煤气变换反应催化剂Ⅰ.制备参数对催化剂活性的影响

Au / Fe_2O_3 Water-Gas Shift Catalyst Prepared by Microemulsion Method ⅰ . Effect of Synthesis Parameters on Catalyst Activity

本研究主要考察了不同组成的汽车尾气净化催化剂在无氧条件下对CO水煤气反应和HC蒸汽转换反应的催化性能。

The performance of different catalysts in the water-gas shift and steam reforming reactions under rich condition was studied experimentally .

对于以水煤气为原料提取CO的工艺，如果氢气未能充分利用，则提高了CO生产成本。

In the industrial process manufacturing carbon monoxide from water gas , if hydrogen can 't be fully utilized , the production cost will be increased .

结合两个实例介绍了DCS在水煤气两段炉的应用。第一个实例是运用DCS系统提供的开关仪表和顺控表解决行程开关输入响应异常的问题；

This text introduces briefly some experience of the DCS system application in water gas two-stage furnace by the practice examples .

CeO2@Au核壳纳米粒子是一种有发展前途的重要的水煤气转换反应和直接甲醇燃料电池催化剂。

CeO_2 @ Au core-shell nanoparticles is an important catalyst and widely used in water-gas shift reaction and direct methanol fuel cells .

半水煤气净化能耗浅析CO2电极响应过程受半透膜中CO2扩散步骤控制，可用稳态模型描述之。

Analysis on Energy Consumption of Semi-water Gas Purification Process A dynamic differential equation of membrane diffusion , based on the steady state model , was proposed .

如：空气煤气CO2为标志气体，水煤气以H2、CO为标志气体，为调控提供可靠依据。

For instance , the mark gas of air gas is CO2 while the water gas considers H2 and CO as its mark gas .

结果表明，Fe－Cu－K催化剂上费托反应与水煤气变换反应同时进行，产物分布（油、蜡、烯／烷比、正构烷烃、1－烯烃等）随操作条件发生有规律的变化。

The results show that FT and water gas shift ( WGS ) reactions take place simultaneously on the catalyst surface , and product distributions vary with operation conditions .