The performance of the catalyst for carbon dioxide reforming of methane was investigated.
采用大气压高频冷等离子体炬,对用于甲烷和CO2重整反应的Ni/γ-Al2O3催化剂进行还原。
Effects of pressure on catalytic performance of Ni/CeO_2-Al_2O_3 catalyst prepared by impregnation for CH_4 reforming with CO_2 were investigated systematically.
以 Ni/CeO_2-Al_2O_3为催化剂,考察了压力对 CH_4/CO_2重整反应的影响。
The effects of preparation methods on structure and TPR profiles of Ni based catalysts for CH 4 reforming with CO 2 were investigated by means of BET, XRD, XPS, IR and TPR techniques.
同时 ,该方法适宜于制备负载多组分金属催化剂 ,有利于发挥助剂的改善调节作用 ,满足CH4 CO2 重整反应对催化剂的要求 。
The impact of a catalytic reforming reaction on the ignition temperature was investigated during the firing of diesel oil mixed with water.
研究了催化重整反应对柴油掺水燃烧中着火温度的影响 ,以及有无催化重整时 ,着火温度的变化 ,从实验结果中可看出催化重整反应对乳化柴油着火有显著的影响 ,能够显著降低着火温度。
The result shows under a certain flow of methane and vapour and when there is catalyzer in the surface of bluff body, catalytic reforming reaction will take place in the surface and produce some hydrogem (H)so that the flame can be blown out with a much faster air speed and the stability of the flame has been effectively increased.
结果指出,在甲烷流量和水蒸汽流量一定的条件下,当钝体表面喷涂有催化剂时,将在表面处发生催化重整反应,产生部分氢气,从而使得火焰需要在更大的空气流速下才会被吹熄,有效地提高了火焰的稳定性。
The overall performance of solid oxide fuel cell (SOFC) is controlled by CH4 steam reforming reactions and CO, H2 electrochemical reactions, which take place in the porous anode simultaneously and are influenced by various operation and design parameters when pre-reformed methane/steam mixture is used.
以经过预重整反应的混合气为原料的固体氧化物燃料电池(SOFC)内部,甲烷蒸气重整反应与电化学反应同时发生在阳极多孔介质中,二者受到不同的操作与设计参数的影响,对电池总体性能起着决定性作用。
Simulation of Catalytic Reformiong Process and Steady State Simulation of the Catalytic Reforming Reactors;
催化重整全流程仿真及重整反应器的稳态模拟
Application of Rare-earth Additives La_2O_3 in CH_4-CO_2 Reforming Reaction
稀土助剂La_2O_3在CH_4-CO_2重整反应中的应用
Mass-Loss Characteristic of Carbonaceous Catalyst in CH_4-CO_2 Reformation
CH_4-CO_2重整反应过程中炭催化剂失重特性
Dynamic Simulation of Catalytic Reforming and the Discusstion of the Catalytic Reforming Reactor Simulation;
催化重整全流程动态模拟及重整反应器模拟方法探讨
The Intrinsic Kinetics of Methane Steam Reforming and Reaction Performance Study in Micro-channel Reactor
甲烷蒸汽重整反应本征动力学及微通道反应器性能研究
NUMERICAL SIMULATION ON CH_4/H_2O CATALYTIC REFORMING REACTION ON Ni/α-Al_2O_3 WITH CO_2/CH_4 REACTION IN A MICRO-CHAMBER
CH_4/CO_2反应对微细腔内CH_4/H_2O镍基催化重整反应的影响
THE STUDY OF CATALYTIC REFORMING REACTION KINETICS MODEL(Ⅲ)THE CATALYTIC REFORMING REACTION KINETICS OF C_8 HYDROCARBONS
催化重整集总反应动力学模型研究——(Ⅲ)八碳重整反应网络动力学模型研究
The Kinetic Study in the CH_4/CO_2 Reforming Reactions over Ni-based Catalysts;
镍基催化剂上CH_4/CO_2重整反应的动力学研究
Study on Modification of Ni/BaTiO_3 Catalyst in CO_2 Reforming of CH_4;
Ni/BaTiO_3催化剂在CH_4/CO_2重整反应中的改性研究
fixed bed swing reactor catalytic reforming
固定床切换反应器催化重整
A Theoretical Study of the CO_2 Reforming of CH_4;
CO_2重整CH_4反应的理论研究
American Reaction to Germany s Rearmament in 1935;
美国对德国1935年重整军备的反应
Research on the Catalytic Process of Hydrogen Production from Dimethyl Ether Reforming
二甲醚重整制氢催化反应过程的研究
Progress in the investigation on mechanism of methanol steam reforming for hydrogen production
甲醇蒸气重整制氢反应机理研究进展
LUMPED KINETIC MODEL OF AROMATIC TYPE CATALYTIC NAPHTHA REFORMING
芳烃型催化重整集总反应动力学模型
STUDIES ON CATALYTIC REFORMING REACTION KINETIC MODELS (Ⅰ)Catalytic reforming reaction kinetics of C_6 hydrocarbons
催化重整集总反应动力学模型研究——(Ⅰ)六碳反应网络的动力学模型
STUDIES ON CATALYTIC REFORMING REACTION KINETIC MODELS (Ⅱ)The catalytic reforming reaction kinetics of C_7 Hydrocarbons
催化重整集总反应动力学模型研究——(Ⅱ)七碳反应网络的动力学模型
Hydrogen production from reform of bio-oil aqueous phase over Z204 catalyst using two-stage fixed bed reactor
两段式固定床反应器上生物油水相部分的重整制氢反应
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