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51.
S. Freni N. Mondello S. Cavallaro G. Cacciola V.N. Parmon V.A. Sobyanin 《Reaction Kinetics and Catalysis Letters》2000,71(1):143-152
A two-layer fixed-bed catalytic reactor for hydrogen production by steam reforming of ethanol is proposed. In this reactor ethanol is first converted to acetaldehyde over a Cu-based catalyst and then acetaldehyde is converted to a hydrogen-rich mixture over a Ni-based catalyst. It is shown that the use of such type of reactor prevents coke formation and provides hydrogen yields closed to equilibrium. 相似文献
52.
53.
助剂对负载型镍催化剂重整活性和抗积炭性能的影响 总被引:3,自引:0,他引:3
应用XRD和催化活性评价手段,考察了助剂对C2重整制合成气的负勒型Ni催化剂的重整活性和其抗积炭性能的影响。实验结果表明,NiO在γ-Al2O3表面上最大分散量随MgO、La2O3助剂的添加没程度地增大,助剂能影响负载型Ni催化剂 论性能,MgO、La2O3的添加对改善Ni催化剂的重整活性和抗积炭性能有明显效果,并与助剂的种类添加次序有关。 相似文献
54.
Hongqing Chen Hao Yu Yong Tang Minqiang Pan Guangxing Yang Feng Peng Hongjuan Wang Jian Yang 《天然气化学杂志》2009,18(2)
Hydrogen was produced over noble metal (Ir, Ru, Rh, Pd) catalysts supported on various oxides, including γ-Al2O3, CeO2, ZrO2 and La2O3, via the autothermai reforming reaction of ethanol (ATRE) and oxidative reforming reaction of ethanol (OSRE). The conversion of ethanol and selectivites for hydrogen and byproducts such as methane, ethylene and acetaldehyde were studied. It was found that lanthana alone possessed considerable activity for the ATRE reaction, which could be used as a functional support for ATRE catalysts. It was demonstrated that Ir/La2O3 prevented the formation of methane, and Rh/La2O3 encumbered the production of ethylene and acetaldehyde. ATRE reaction was carried out over La2O3-supported catalysts (Ir/La2O3) with good stability on stream, high conversion, and excellent hydrogen selectivity approaching thermodynamic limit under autothermal condition. Typically, 3.4 H2 molecules can be extracted from a pair of ethanol and water molecules over Ir(5wt%)/La2O3. The results presented in this paper indicate that Ir/La2O3 can be used as a promising catalyst for hydrogen production via ATRE reaction from renewable ethanol. 相似文献
55.
《Comptes Rendus Chimie》2014,17(5):454-458
The steam reforming of methane over Cu/Co6Al2 mixed oxides with different copper contents was studied. The Co6Al2 support was prepared via the hydrotalcite route. It was thermally stabilized at 500 °C, impregnated with 5 wt.%, 15 wt.% or 25 wt.% copper using copper (II) nitrate Cu(NO3)2·3H2O precursor and then calcined again at 500 °C under an air flow. The impregnation of copper enhanced significantly the reactivity of the solids in the considered reaction. The 5Cu/Co6Al2 solid was the most reactive one, with a methane conversion of 96% at 650 °C. The selectivities of H2 and CO2 were also better for the catalyst containing 5 wt.% copper compared to higher copper loadings. The decrease in the catalytic reactivity with increasing the copper content was attributed to the formation of agglomerated and less reactive CuO species, which were detected by XRD and TPR analyses. 相似文献
56.
《Journal of Energy Chemistry》2014,23(5):633-638
MgO-modified Ni/Al2O3 catalysts with different Ni loadings were prepared and employed in dry reforming of methane (DRM). The effect of Ni loadings on the activity and coke formation of Ni/MgO-Al2O3 catalysts were investigated. The synthesized catalysts were characterized by XRD, N2 adsorption-desorption, SEM, TPO and TPR techniques. The obtained results showed that increasing nickel loading decreased the BET surface area and increased the catalytic activity and amount of deposited carbon. In addition, the effect of gas hourly space velocity (GHSV) and feed ratio were studied. 相似文献
57.
以稀土金属Nd,Ce或La的氧化物为助剂,采用β-环糊精浸渍法对Ni/SBA-15催化剂进行了改性,并运用X射线衍射、N2吸附-脱附、程序升温还原和热重等手段考察了改性的催化剂在CO2重整CH4制合成气反应中的催化性能. 结果表明,Nd等稀土金属氧化物的添加对催化剂孔结构和晶相结构等性质影响不大,但可影响NiO的还原; Nd的添加使NiO与载体之间以Ni-Nd-O形式相互作用,促进了活性组分NiO的还原. 其中,Nd的添加量为5-10 wt%时所制备的催化剂在重整反应中的催化活性最高,且具有很强的抗积碳性能. La和Ce氧化物促进的Ni催化剂也表现出类似的性质和催化性能. 相似文献
58.
《催化学报》2014,(12):1781-1792
Chin. J. Catal., 2014, 35: 1911–1916 doi: 10.1016/S1872‐2067(14)60208‐4 Dehydrogenation of primary aliphatic alcohols to aldehydes over Cu‐Ni bimetallic catalysts Tianliang Lu, Zhongtian Du, Junxia Liu, Chen Chen, Jie Xu * Dalian Institute of Chemical Physics, Chinese Academy of Sciences; University of Chinese Academy of Sciences 相似文献
59.
A novel technological concept of sorption-enhanced steam reforming of hydrocarbons is suggested. The peculiarity of the concept
is the autothermal regeneration of the carbon dioxide scavenger in the moving super-adiabatic heat wave of an exothermic catalytic
combustion reaction performed directly inside the adsorption-catalytic bed. The capability and high efficiency of the proposed
technological approach are confirmed by process simulation. The approach proposed is shown to open a way for the creation
of an inexpensive, reliable and energy-saving adiabatic packed bed methane processors of unlimited processing capacity. 相似文献
60.