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过刊目录

    2008, Vol. 17, No. 4 Online: 2008-12-30
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    Articles
    Influence of alkali metal doping on surface properties and catalytic activity/selectivity of CaO catalysts in oxidative coupling of methane
    V. H. Rane*;S. T. Chaudhari;V. R. Choudhary
    2008, 17(4): 313-320.  DOI:
    摘要 ( 8321 )   PDF  
    Surface properties (viz. surface area, basicity/base strength distribution, and crystal phases) of alkali metal doped CaO (alkali metal/Ca = 0.1 and 0.4) catalysts and their catalytic activity/selectivity in oxidative coupling of methane (OCM) to higher hydrocarbons at different reaction conditions (viz. temperature, 700 and 750 oC; CH4/O2 ratio, 4.0 and 8.0 and space velocity, 5140–20550 cm3/(g·h) have been investigated. The influence of catalyst calcination temperature on the activity/selectivity has also been investigated. The surface properties (viz. surface area, basicity/base strength distribution) and catalytic activity/selectivity of the alkali metal doped CaO catalysts are strongly influenced by the alkali metal promoter and its concentration in the alkali metal doped CaO catalysts. An addition of alkali metal promoter to CaO results in a large decrease in the surface area but a large increase in the surface basicity (strong basic sites) and the C2+ selectivity and yield of the catalysts in the OCM process. The activity and selectivity are strongly influenced by the catalyst calcination temperature. No direct relationship between surface basicity and catalytic activity/selectivity has been observed. Among the alkali metal doped CaO catalysts, Na-CaO (Na/Ca = 0.1, before calcination) catalyst (calcined at 750 oC), showed best performance (C2+ selectivity of 68.8% with 24.7% methane conversion), whereas the poorest performance was shown by the Rb-CaO catalyst in the OCM process.
    Preparation and thermal treatment of Pd/Ag composite membrane on a porous alumina tube by sequential electroless plating technique for H2 separation
    E. Navaei Alvar;M. Reza Golmohammadi;M. Rezaei*;H. Navaei Alvar;A. Mardanloo;S. Habibzad Nouhian;M. Didari
    2008, 17(4): 321-326.  DOI:
    摘要 ( 7826 )   PDF  
    Pd/Ag/α-Al2O3 composite membranes were prepared by sequential electroless plating technique. The prepared membranes were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), energy dispersive spectroscopy, and inductively coupled plasma atomic emission spectroscopy techniques (ICP-AES). Effects of annealing time, Ag content, and air treatment on the hydrogen permeation flux and morphology of the alloys were investigated. The results of the investigation showed that the prepared type of tube had a good potential as substrate for membrane preparation. In addition, a uniform defect-free alloy was prepared by annealing at 550 ?C in H2 atmosphere. The permeation results showed an increase in H2 permeation flux by increasing the Ag content and the annealing time. In addition, the air treatment of the prepared membranes at 400 ?C for 1 h changed the morphology of the alloy and substantially enhanced the hydrogen flux.
    Preparation and characterization of ultrafine Fe-Cu-based catalysts for CO hydrogenation
    Yunlai Su;*;YingliWang;Zhongmin Liu
    2008, 17(4): 327-331.  DOI:
    摘要 ( 7553 )   PDF  
    The ultrafine particles of a new style Fe-Cu-based catalysts for CO hydrogenation were prepared by impregnating the organic sol of Fe(OH)3 and Cu(OH)2 onto the activated Al2O3, in which the organic sol of Fe(OH)3 and Cu(OH)2 were prepared in the microemulsion of dodecylbenzenesulfonic acid sodium(S)/n-butanol(A)/toluene(O)/water with V (A)/V (O) = 0.25 and W(A)/W(S) = 1.50. This catalyst was characterized by particle size analysis, XRD and TG. The results of particle size analysis showed that Fe(OH)3 particles with a mean size of 17.1 nm and Cu(OH)2 particles with an average size of 6.65 um were obtained. TG analysis and XRD patterns suggested that 673 K is the optimal calcination temperature. CO hydrogenation produced C+2 OH with a high selectivity above 58 wt% by using the ultrafine particles as catalyst, and the total alcohol yield of 0.250 g·ml-1·h-1 was obtained when the contents of Al2O3 and K were 88.61 wt% and 1.60 wt%, respectively.
    Effect of dispersion and distribution of tungsten on W/HZSM-5 for selective catalytic reduction of NO by acetylene
    Ran Bi;Xinping Wang*;Zhiguang Liu;Jing Chen
    2008, 17(4): 332-336.  DOI:
    摘要 ( 8132 )   PDF  
    Catalytic performance of W/HZSM-5 in selective catalytic reduction of NO by acetylene was investigated in a reaction system with 1600 ppm of NO, 800 ppm of C2H2, and 9.95% of O2 in He. It was found that promotional effect of tungsten on the reaction is strongly affected by catalyst preparation conditions and Si/Al ratio of the parent zeolite. A better dispersion of tungsten on HZSM-5 and relatively more monomeric tungsten species were found on 8%W/HZSM-5 prepared by impregnation of the zeolite with lower SiO2/Al2O3 ratio (25) in ammonic ammonium tungstate solution and calcination of the resulting material at higher temperature (550 ?C). The highest NO conversion to N2 of 86.3% in the reaction system was obtained at 350 ?C over the catalyst thus prepared. The mechanism of monomeric tungsten species improving the C2H2-SCR can be attributed to accelerating the formation of active nitrate species.
    Effect of Pd or Ir on the catalytic performance of Mo/H-ZSM-5 during the non-oxidative conversion of natural gas to petrochemicals
    Ahmed K. Aboul-Gheit*;Ahmed E. Awadallah;Salah M. El-Kossy;Abdel-Lateef H. Mahmoud
    2008, 17(4): 337-343.  DOI:
    摘要 ( 8747 )   PDF  
    Natural gas conversion to petrochemicals, principally, benzene, naphthalene, toluene, as well as ethylene under non-oxidative conditions was examined in a fixed bed flow reactor at 700oC and gaseous hourly space velocity (GHSV) of 1500 ml·g-1·h-1 at time-on-stream ranging from 5min to 4h using catalysts containing 6.0% Mo/H-ZSM-5 promoted with Pd or Ir metal. The catalysts were characterized by XRD, TPD, and TGA. The addition of Pd or Ir to 6%Mo/H-ZSM-5 catalyst promoted ethylene production but inhibited the cyclization reaction to aromatics owing to the strong interaction between these noble metals and the framework Al species, which were attached to the acid sites during the impregnation process. Coke deposition on the catalysts was found to decrease upon addition of 0.5wt% of Pd or Ir to 6%Mo/H-ZSM-5 catalyst owing to the hydrogenating activity of these metals.
    Yttria promoted metallic nickel catalysts for the partial oxidation of methane to synthesis gas
    Yaquan Wang*;Xuebin Hong;Bingbing Li;Wenju Wang;Dalin Wang
    2008, 17(4): 344-350.  DOI:
    摘要 ( 7674 )   PDF  
    A metallic Ni catalyst was prepared with nickel sponge, followed by acid treatment. It was further promoted with yttria by an impregnation method. The catalysts were characterized by SEM, BET, XRD, TPR, XPS, etc., and studied in the partial oxidation of methane to syngas. The characterization results showed that the yttria promoted metallic Ni catalysts had high specific surface area and more NiO. The reaction results showed that the yttria promoter increased the CH4 conversion and the selectivity for H2 and CO.
    Hydroformylation of methyl-3-pentenoate over a phosphite ligand modified Rh/SiO2 catalyst
    Xianming Li;Yunjie Ding;*;Guiping Jiao;Jingwei Li;Li Yan;Hejun Zhu
    2008, 17(4): 351-354.  DOI:
    摘要 ( 8285 )   PDF  
    A phosphite ligand modified Rh/SiO2 catalyst has been developed for hydroformylation of internal olefins to linear aldehydes, which showed high activity and regioselectivity and could be separated easily by filtration after reaction in an autoclave. Effects of reaction temperature and syngas pressure on the performances of the catalyst in the reaction were also investigated.
    Study on Ni/C catalysts for vapor phase carbonylation of ethanol
    Qing Zhang;Huifang Wang;Guosong Sun;Kelin Huang;Weiping Fang;Yiquan Yang*
    2008, 17(4): 355-358.  DOI:
    摘要 ( 8315 )   PDF  
    Activated carbon-supported Ni catalysts for vapor phase carbonylation of ethanol to propionic acid in the presence of ethyl iodide as promoter were investigated. Under optimum reaction conditions, the conversions of carbon monoxide and ethanol were measured to be 81.37% and 98.41%, respectively, while the selectivity for propionic acid was found to be 98.65%. The catalyst was stable within 48 h on stream. XRD and XPS methods were used to characterize the structures and surface properties of the fresh and tested catalysts. The characterization results indicated that aggregation of nickel particles and formation of nickel iodide on the catalyst surface should be responsible for the deactivation of the catalysts.
    CO removal by two-stage methanation for polymer electrolyte fuel cell
    Zhiyuan Li;Wanliang Mi;Juan Gong;Zhenlong Lu;Lihao Xu;Qingquan Su*
    2008, 17(4): 359-364.  DOI:
    摘要 ( 8934 )   PDF  
    In order to remove CO to achieve lower CO content of below 10 ppm in the CO removal step of reformer for polymer electrolyte fuel cell (PEFC) co-generation systems, CO preferential methanation under various conditions were studied in this paper. Results showed that, with a single kind of catalyst, it was difficult to reach both CO removal depth and CO2 conversion ratio of below 5%. Thus, a two-stage methanation process applying two kinds of catalysts is proposed in this study, that is, one kind of catalyst with relatively low activity and high selectivity for the first stage at higher temperature, and another kind of catalyst with relatively high activity and high selectivity for the second stage at lower temperature. Experimental results showed that at the first stage CO content was decreased from 1% to below 0.1% at 250–300 ?C, and at the second stage to below 10 ppm at 150–185 ?C. CO2 conversion was kept less than 5%. At the same time, influence of inlet CO content and GHSV on CO removal depth was also discussed in this paper.
    H2-induced CO adsorption and dissociation over Co/Al2O3 catalyst
    Xiaoping Dai;Changchun Yu*
    2008, 17(4): 365-368.  DOI:
    摘要 ( 8605 )   PDF  
    The activation of adsorbed CO is an important step in CO hydrogenation. The results from TPSR of pre-adsorbed CO with H2 and syngas suggested that the presence of H2 increased the amount of CO adsorption and accelerated CO dissociation. The H2 was adsorbed first, and activated to form H* over metal sites, then reacted with carbonaceous species. The oxygen species for CO2 formation in the presence of hydrogen was mostly OH*, which reacted with adsorbed CO subsequently via CO* + OH*---CO2* +H*; however, the direct CO dissociation was not excluded in CO hydrogenation. The dissociation of C–O bond in the presence of H2 proceeded by a concerted mechanism, which assisted the Boudourd reaction of adsorbed CO on the surface via CO* + 2H*---CH* + OH*. The formation of the surface species (CH) from adsorbed CO proceeded as indicated with the participation of surface hydrogen, was favored in the initial step of the Fischer-Tropsch synthesis.
    Effects of impregnation sequence on the microstructure and performances of Cu-Co based catalysts for the synthesis of higher alcohols
    Siyu Deng;Wei Chu*;Huiyuan Xu;Limin Shi;Lihong Huang
    2008, 17(4): 369-373.  DOI:
    摘要 ( 8648 )   PDF  
    Silica-supported CuCo catalysts were prepared by impregnation method with different impregnation sequence for higher alcohols synthesis. These catalysts were characterized by H2-TPR, XRD, N2 adsorption, XPS techniques and CO selective hydrogenation reaction measurement. The effects of impregnation sequence on the structure and performance of catalysts were investigated, and there were important influences on the selectivity to higher alcohols. There was a strong synergistic effect between copper and cobalt for the co-impregnated sample. The CuCo/SiO2 catalyst prepared by co-impregnation showed a better yield of total alcohols, and a higher selectivity to total alcohols which reached 51.53%.
    Effect of surface structure on the catalytic behavior of Ni:Cu/Al and Ni:Cu:K/Al catalysts for methane decomposition
    S. Tajammul Hussain*;Sheraz Gul;Muhammed Mazhar;Dalaver H. Anjum;Faical Larachi
    2008, 17(4): 374-382.  DOI:
    摘要 ( 8466 )   PDF  
    Methane decomposition using nickel, copper, and aluminum (Ni:Cu/Al) and nickel, copper, potassium, and aluminum (Ni:Cu:K/Al) modified nano catalysts has been investigated for carbon fibers, hydrogen and hydrocarbon production. X-ray photoelectron spectroscopy (XPS), static secondary ion mass spectrometry (SSIMS), thermal gravimetric analysis (TGA), Fourier transform infrared (FT-IR), secondary electron microscopy/X-ray energy dispersive (SEM-EDX), and temperature programmed desorption (TPD) were used to depict the chemistry of the catalytic results. These techniques revealed the changes in surface morphology and structure of Ni, Cu, Al, and K, and formation of bimetallic and trimetallic surface cationic sites with different cationic species, which resulted in the production of graphitic form of pure carbon on Ni:Cu/Al catalyst. The addition of K has a marked effect on the product selectivity and reactivity of the catalyst system. K addition restricts the formation of carbon on the surface and increases the production of hydrogen and C2, C3 hydrocarbons during the catalytic reaction whereas no hydrocarbons are produced on the sample without K. This study completely maps the modified surface structure and its relationship with the catalytic behavior of both systems. The process provides a flexible route for the production of carbon fibers and hydrogen on Ni:Cu/Al catalyst and hydrogen along with hydrocarbons on Ni:Cu:K/Al catalyst. The produced carbon fibers are imaged using a transmission electron microscope (TEM) for diameter size and wall structure determination. Hydrogen produced is COx free, which can be used directly in the fuel cell system. The effect of the addition of Cu and its transformation and interaction with Ni and K is responsible for the production of CO/CO2 free hydrogen, thus producing an environmental friendly clean energy.
    Environment-friendly synthesis of N-phenylpiperidine from aniline and 1,5-pentanediol over γ-Al2O3 catalyst
    Wei Tan;Chunmei Li;Jiacong Zheng;Lei Shi*;Qi Sun;Yuhong He
    2008, 17(4): 383-386.  DOI:
    摘要 ( 7578 )   PDF  
    An efficient environment-friendly synthesis ofN-phenylpiperidine was developed from aniline and 1, 5-pentanediol over γ-Al2O3 catalyst under atmospheric pressure. The conversion of 1,5-pentanediol reached 97% and the selectivity for N-phenylpiperidine attained 94%. The structure of the catalyst was characterized by NH3-TPD and BET. The influences of calcination temperature of the catalyst and reaction temperature on activity and selectivity of the catalyst were investigated.
    A sulfur-tolerant Pd/CeO2 catalyst for methanol synthesis from syngas
    Yuchun Ma;Qingjie Ge*;Wenzhao Li;Hengyong Xu*
    2008, 17(4): 387-390.  DOI:
    摘要 ( 8382 )   PDF  
    The catalytic activity of ceria-supported Pd for selective hydrogenation of CO is well preserved in the presence of 30 ppm H2S due to the parallel oxidation of sulfur by CeO2 under standard methanol synthesis conditions. The bifunctional nature of this catalyst opens a route for the conversion of sulfur-contaminated gas streams such as the integrated gasification combined cycle syngas or biogas into liquid fuels if desulfurization by conventional means is not practical.
    Adsorption separation of carbon dioxide, methane, and nitrogen on HB and Na-exchanged B-zeolite
    Xiaoliang Xu;Xingxiang Zhao;Linbing Sun;Xiaoqin Liu*
    2008, 17(4): 391-396.  DOI:
    摘要 ( 9336 )   PDF  
    Adsorption isotherms of carbon dioxide (CO2), methane (CH4), and nitrogen (N2) on HB and sodium exchanged B-zeolite (NaB) were volumetrically measured at 273 and 303 K. The results show that all isotherms were of Brunauer type I and well correlated with Langmuir-Freundlich model. After sodium ions exchange, the adsorption amounts of three adsorbates increased, while the increase magnitude of CO2 adsorption capacity was much higher than that of CH4 and N2. The selectivities of CO2 over CH4 and CO2 over N2 enhanced after sodium exchange. Also, the initial heat of adsorption data implied a stronger interaction of CO2 molecules with Na+ ions in NaB. These results can be attributed to the larger electrostatic interaction of CO2 with extraframework cations in zeolites. However, NaB showed a decrease in the selectivity of CH4 over N2, which can be ascribed to the moderate affinity of N2 with NaB. The variation of isosteric heats of adsorption as a function of loading indicates that the adsorption of CO2 in NaB presents an energetically heterogeneous profile. On the contrary, the adsorption of CH4 was found to be essentially homogeneous, which suggests the dispersion interaction between CH4 and lattice oxygen atoms, and such interaction does not depend on the exchangeable cations of zeolite.
    Catalytic properties of Cu/Co/Zn/Zr oxides prepared by various methods
    Limin Shi;Wei Chu*;Siyu Deng;Huiyuan Xu
    2008, 17(4): 397-402.  DOI:
    摘要 ( 7855 )   PDF  
    The new Cu-Co based (Cu/Co/Zn/Zr) catalysts for higher-alcohol synthesis were prepared using coprecipitation method, plasma enhanced method and reverse coprecipitation method under ultrasound irradiation. The catalysts were investigated by the means of BET, SEM, XRD, H2-TPR and XPS. Catalytic properties of the catalysts prepared by various methods were examined using CO hydrogenation reaction. It was found that plasma enhanced method and reverse coprecipitation method under ultrasound irradiation were both effective in enhancing the catalytic properties of Cu/Co/Zn/Zr mixed oxides. The small particle size, high dispersion of active components, the improvement of specific surface area and surface contents of active phases could account for the excellent performance of the experimental Cu/Co/Zn/Zr catalysts.
    Three-dimensionally ordered macro-porous Pt/TiO2 catalyst used for water-gas shift reaction
    Hao Liang;Yuan Zhang;Yuan Liu*
    2008, 17(4): 403-408.  DOI:
    摘要 ( 7942 )   PDF  
    Three-dimensionally ordered macro-porous (3DOM) Pt/TiO2 catalysts were prepared by template and impregnation methods, and the resultant samples were characterized by using TG-DTA, XRD, SEM, TEM, and TPR techniques. The catalytic performance for water-gas shift (WGS) reaction was tested, and the influences of some conditions, such as reduction temperature of catalysts, the amount of Pt loadings and space velocity on catalytic performance were investigated. It was shown that Pt particles were homogeneously dispersed on 3DOM TiO2. The reduction of TiO2 surface was important for the catalytic performance. The activity test results showed that the 3DOM Pt/TiO2 catalysts exhibited very good catalytic performance for WGS reaction even at high space velocity, which was owing to the better mass transfer of 3DOM porous structure besides the high intrinsic activity of Pt/TiO2.
    Fuzzy self-tuning PID control of the operation temperatures in a two-staged membrane separation process
    Lei Wang*;Wencai Du;Hai Wang;Hong Wu
    2008, 17(4): 409-414.  DOI:
    摘要 ( 7807 )   PDF  
    A two-staged membrane separation process for hydrogen recovery from refinery gases is introduced. The principle of the gas membrane separation process and the influence of the operation temperatures are analyzed. As the conventional PID controller is difficult to make the operation temperatures steady, a fuzzy self-tuning PID control algorithm is proposed. The application shows that the algorithm is effective, the operation temperatures of both stages can be controlled steadily, and the operation flexibility and adaptability of the hydrogen recovery unit are enhanced with safety. This study lays a foundation to optimize the control of the membrane separation process and thus ensure the membrane performance.
    Communctions
    Comparison of LaFeO3, La0.8Sr0.2FeO3, and La0.8Sr0.2Fe0.9Co0.1O3 perovskite oxides as oxygen carrier for partial oxidation of methane
    Xiaoping Dai;Changchun Yu*;Qiong Wu
    2008, 17(4): 415-418.  DOI:
    摘要 ( 8436 )   PDF  
    Comparison of LaFeO3, La0.8Sr0.2FeO3, and La0.8Sr0.2Fe0.9Co0.1O3 perovskite oxides as oxygen carrier for partial oxidation of methane in the absence of gaseous oxygen was investigated by continuous flow reaction and sequential redox reaction. Methane was oxidized to syngas with high selectivity by oxygen species of perovskite oxides in the absence of gaseous oxygen. The sequential redox reaction revealed that the structural stability and continuous oxygen supply in redox reaction decreased over La0.8Sr0.2Fe0.9Co0.1O3 oxide, while LaFeO3 and La0.8Sr0.2FeO3 exhibited excellent structural stability and continuous oxygen supply.