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Photocatalytic activity of TiO_2 supported SiO_2-Al_2O_3 aerogels prepared from industrial fly ash 被引量:8
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作者 王慧龙 齐慧萍 +2 位作者 魏晓娜 刘潇彧 姜文凤 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2016年第11期2025-2033,共9页
A ternary composite of TiO2 and a SiO2-Al2O3 aerogel with good photocatalytic activity was prepared by a simple sol-gel method with TiO2 nanoparticles and SiO2-Al2O3 aerogels derived from industrial fly ash.The struct... A ternary composite of TiO2 and a SiO2-Al2O3 aerogel with good photocatalytic activity was prepared by a simple sol-gel method with TiO2 nanoparticles and SiO2-Al2O3 aerogels derived from industrial fly ash.The structural features of the TiO2/SiO2-Al2O3 aerogel composite were investigated by X-ray powder diffraction,Fourier transform infrared spectroscopy,transmission electron microscopy,gas adsorption measurements and diffuse reflectance UV-visible spectroscopy.The optimal conditions for photocatalytic degradation of 2-sec-butyl-4,6-dinitrophenol(DNBP],included an initial DNBP concentration of 0.167 mmol/L at pH = 4.86 with a catalyst concentration of 6 g/L,under visible light irradiation for 5 h.A plausible mechanism is proposed for the photocatalytic degradation of DNBP.Our composite showed higher photocatalytic activity for DNBP degradation than that of pure TiO2.This indicates that this material can serve as an efficient photocatalyst for degradation of hazardous organic pollutants in wastewater. 展开更多
关键词 Titania Sio2-al2o3 aerogel Composite photocatalyst Industrial fly ash 2-sec-butyl-4 6-dinitrophenol Wastewater treatment
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Elaboration of an Easy Aqueous Sol-Gel Method for the Synthesis of Micro- and Mesoporous <i>γ</i>-Al<sub>2</sub>O<sub>3</sub>Supports
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作者 Vincent Claude Hugo Solis Garcia +1 位作者 Cédric Wolfs Stéphanie D. Lambert 《Advances in Materials Physics and Chemistry》 2017年第7期294-310,共17页
An aqueous sol-gel method for the synthesis of γ-Al2O3 supports has been developed for the use in tar reforming applications. It was determined the influences of two different aluminum precursors (aluminum sec-butoxi... An aqueous sol-gel method for the synthesis of γ-Al2O3 supports has been developed for the use in tar reforming applications. It was determined the influences of two different aluminum precursors (aluminum sec-butoxide (Al[OCH(CH3)CH2CH3]3) and aluminum nitrate (Al(NO3)3)) on the textural and crystallographic properties of Al2O3 supports. Only the formation of γ-Al2O3 is aimed in order to use these alumina materials as catalytic supports, because it presents high specific surface area and pore volume values. Additionally, the synthesis of γ-Al2O3 was realized with the use of a functionalized silicon precursor, [3-(2-aminoethylamino)propyl]trimethoxysilane, called EDAS. By the presence of an ethylenediamine group in this molecule, it is possible to chelate metallic ions and to highly increase their dispersion at a molecular level during the synthesis of metallic catalysts supported on alumina, which is an asset for catalytic applications. So it was developed a synthesis sol-gel procedure for the cogelation between the functionalized silicon alkoxide EDAS and alumina precursor. The alumina supports synthesized with Al(NO3)3 as precursor presented higher porous values than the ones obtained with aluminium sec-butoxide precursor. Since nitrate salts are much easier to handle than alkoxides, these observations allowed validating Al(NO3)3 as aluminum source for the future synthesis procedures for metallic catalysts supported on alumina. 展开更多
关键词 Sol-Gel Process γ-al2o3 supports AQUEoUS Synthesis Cogelation Method
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Support Effects on Thiophene Hydrodesulfurization over Co-Mo-Ni/Al_2O_3 and Co-Mo-Ni/TiO_2-Al_2O_3 Catalysts 被引量:7
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作者 刘超 周志明 +2 位作者 黄永利 程振民 袁渭康 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2014年第4期383-391,共9页
A carbon-based sulfonated catalyst was prepared by direct sulfonation and carbonization (in moderate conditions:200 &#176;C, 12 h) of red liquor solids, a by-product of paper-making process. The prepared sulfonate... A carbon-based sulfonated catalyst was prepared by direct sulfonation and carbonization (in moderate conditions:200 &#176;C, 12 h) of red liquor solids, a by-product of paper-making process. The prepared sulfonated cata-lyst (SC) had aromatic structure, composed of carbon enriched inner core, and oxygen-containing (SO3H, COOH, OH) groups enriched surface. The SO3H, COOH, OH groups amounted to 0.74 mmol·g^-1, 0.78 mmol·g^-1, 2.18 mmol·g^-1, respectively. The fresh SC showed much higher catalytic activity than that of the traditional solid acid catalysts (strong-acid 732 cation exchange resin, hydrogen type zeolite socony mobile-five (HZSM-5), sulfated zir-conia) in esterification of oleic acid. SC was deactivated during the reactions, through the mechanisms of leaching of sulfonated species and formation of sulfonate esters. Two regeneration methods were developed, and the catalytic activity can be mostly regenerated by regeneration Method 1 and be fully regenerated by regeneration Method 2, respectively. 展开更多
关键词 HYDRoDESULFURIZATIoN support hierarchically macro-/mesoporous structure AL2o3 Tio2-al2o3
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Preparation and evaluation of α-Al2O3 supported lithium ion sieve membranes for Li^+ extraction 被引量:7
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作者 Feng Xue Xiaoxian Zhang +3 位作者 Yue Niu Chenhao Yi Shengui Ju Weihong Xing 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2020年第9期2312-2318,共7页
Spinel lithium manganese oxide ion-sieves have been considered the most promising adsorbents to extract Li^+ from brines and sea water.Here,we report a lithium ion-sieve which was successfully loaded onto tubular α-A... Spinel lithium manganese oxide ion-sieves have been considered the most promising adsorbents to extract Li^+ from brines and sea water.Here,we report a lithium ion-sieve which was successfully loaded onto tubular α-Al2 O3 ceramic substrates by dipping crystallization and post-calcination method.The lithium manganese oxide Li4 Mn5 O(12)was first synthesized onto tubular α-Al2 O3 ceramic substrates as the ion-sieve precursor(i.e.L-AA),and the corresponding lithium ion-sieve(i.e.H-AA) was obtained after acid pickling.The chemical and morphological properties of the ion-sieve were confirmed by X-ray diffraction(XRD) and scanning electron microscopy(SEM).Both L-AA and H-AA showed characteristic peaks of α-Al2 O3 and cubic phase Li4 Mn5 O(12) and the peaks representing cubic phase could still exist after pickling.The lithium manganese oxide Li4 Mn5 O(12) could be uniformly loaded not only on the surface of α-Al2 O3 ubstrates but also inside the pores.Moreover,we found that the equilibrium adsorption capacity of H-AA was 22.9 mg·g^-1.After 12 h adsorption,the adsorption balance was reached.After 5 cycles of adsorption,the adsorption capacity of H-AA was 60.88% of the initial adsorption capacity.The process of H-AA adsorption for Li^+correlated with pseudo-second order kinetic model and Langmuir model.Adsorption thermodynamic parameters regarding enthalpy(△N), Gibbs free energy(△G) and entropy(AS) were calculated.For the dynamic adsorptiondesorption process of H-AA,the H-AA exhibited excellent adsorption performance to Li^+ with the Li^+ dynamic adsorption capacity of 9.74 mg·g^-1 and the Mn^2+dissolution loss rate of 0.99%.After 3 dynamic adsorption-desorption cycles,80% of the initial dynamic adsorption capacity was still kept. 展开更多
关键词 LITHIUM α-al2o3 tube Ion sieve ADSoRPTIoN Li4Mn5o(12)
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Autothermal reforming of methane over Ni catalysts supported over ZrO2-CeO2-Al2O3 被引量:6
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作者 Xiulan Cai Yuanxing Cai Weiming Lin 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2008年第2期201-207,共7页
Ni catalysts supported on Al2O3, ZrO2-Al2O3, CeO2-Al2O3 and ZrO2-CeO2-Al2O3 were prepared by coprecipitation method, and their catalytic performances for autothermal reforming of methane to hydrogen were investigated.... Ni catalysts supported on Al2O3, ZrO2-Al2O3, CeO2-Al2O3 and ZrO2-CeO2-Al2O3 were prepared by coprecipitation method, and their catalytic performances for autothermal reforming of methane to hydrogen were investigated. The Ni-supported catalysts were characterized by XRD, TPR and XPS. The relationship between the structures and catalytic activities of the catalysts was discussed. The results showed that the catalytic activity and stability of the Ni/ZrO2-CeO2-Al2O3 catalyst was better than those of other catalysts with the highest CH4 conversion, H2/CO and H2/COx ratio at 750 ℃. The catalyst showed a little deactivation along the reaction time during its 72 h on stream with the mean deactivation rate of 0.08%/h. The catalytic performance of the Ni/ZrO2-CeO2-Al2O3 catalyst was also affected by reaction temperature, no2 : nCH4 molar ratio and nH2O : nCH4 molar ratio. TPR, XRD and XPS measurements indicated that the formation of ZrO2-CeO2 solid solution could improve the dispersion of NiO, and inhibit the formation of NiAl2O3, and thus significantly promoted the catalytic activity of the Ni/ZrO2-CeO2-Al2O3 catalyst. 展开更多
关键词 METHANE autothermal reforming HYDRoGEN Ni/Zro2-Ceo2-al2o3
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CeO_2-ZrO_2-La_2O_3-Al_2O_3 composite oxide and its supported palladium catalyst for the treatment of exhaust of natural gas engined vehicles 被引量:4
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作者 Xiaoyu Zhang Enyan,Long +5 位作者 Yile Li Jiaxiu Guo Lijuan Zhang Maochu Gong Minghua Wang Yaoqiang Chen 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2009年第2期139-144,共6页
Composite supports CeO2-ZrO2-Al2O3(CZA) and CeO2-ZrO2-Al2O3-La2O3(CZALa) were prepared by co-precipitation method. Palladium catalysts were prepared by impregnation and their purification ability for CH4, CO and N... Composite supports CeO2-ZrO2-Al2O3(CZA) and CeO2-ZrO2-Al2O3-La2O3(CZALa) were prepared by co-precipitation method. Palladium catalysts were prepared by impregnation and their purification ability for CH4, CO and NOx in the mixture gas simulated the exhaust from natural gas vehicles (NGVs) operated under stoichiometric condition was investigated. The effect of La2O3 on the physicochemical properties of supports and catalysts was characterized by various techniques. The characterizations with X-ray diffraction (XRD) and Raman spectroscopy revealed that the doping of La2O3 restrained effectively the sintering of crystallite particles, maintained the crystallite particles in nanoscale and stabilized the crystal phase after calcination at 1000 ℃. The results of N2-adsorption, H2-temperatnre-programmed reduction (H2-TPR) and oxygen storage capacity (OSC) measurements indicated that La2O3 improved the textural properties, reducibility and OSC of composite supports. Activity testing results showed that the catalysts exhibit excellent activities for the simultaneous removal of methane, CO and NOx in the simulated exhaust gas. The catalysts supported on CZALa showed remarkable thermal stability and catalytic activity for the three pollutants, especially for NOx. The prepared palladium catalysts have high ability to remove NOx, CH4 and CO, and they can be used as excellent catalysts for the purification of exhaust from NGVs operated under stoichiometric condition. The catalysts reported in this work also have significant potential in industrial application because of their high performance and low cost. 展开更多
关键词 Pd catalysts natural gas vehicles exhaust methane oxidation Nox conversion Ceo2-Zro2-al2o3 LA2o3
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γ-Al<sub>2</sub>O<sub>3</sub>Supported SO<sub>4</sub><sup>2&#45</sup>/ZrO<sub>2</sub>Solid Superacid Catalysts for n-Pentane Isomerization 被引量:1
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作者 Li Zhao Xiaoshuang Cheng +2 位作者 Ye Hu Shuqing Ma Yingjun Wang 《Modern Research in Catalysis》 2014年第3期89-93,共5页
A solid superacid catalyst Pt-SO42-/ZrO2-A12O3 for n-pentane isomerization, was prepared by incipient-wetness impregnation. Preparetion conditions, namely, calcination temperature, concentration of sulfuric acid solut... A solid superacid catalyst Pt-SO42-/ZrO2-A12O3 for n-pentane isomerization, was prepared by incipient-wetness impregnation. Preparetion conditions, namely, calcination temperature, concentration of sulfuric acid solution used in impregnation and Al2O3 concentration, were varied to investigate the effects on catalytic performance of Pt-SO42-/ZrO2-A12O3. The results showed that the PtSZA catalyst exhibited excellent catalytic performance for n-pentane isomerization. Under optimized preparation conditions of calcination temperature of 650°C, reaction time for 3 h, concentration of sulfuric acid solution for 0.5 mol/L, 30% of Al2O3 concentration and 0.3% of Pt concentration, the n-pentane conversion and isopentane selectivity of Pt-SO42-/ZrO2-A12O3 could reach up to 62.17% and 91.60%, respectively. 展开更多
关键词 So42-/Zro2 N-PENTANE ISoMERIZATIoN γ-al2o3 supportED SUPERACID Catalysts
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CuO/γ-Al_2O_3和CuO-CeO_2-Na_2O/γ-Al_2O_3催化吸附剂的脱硝性能 被引量:17
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作者 赵清森 孙路石 +4 位作者 向军 石金明 王乐乐 殷庆栋 胡松 《中国电机工程学报》 EI CSCD 北大核心 2008年第8期52-57,共6页
利用改进的溶胶凝胶法制备CuO/γ-Al2O3和CuO-CeO2-Na2o/γ-Al2O3催化吸附剂颗粒,在固定床上测试其催化脱硝活性。2类催化吸附剂250-400℃范围内脱硝效率稳定在70%以上。在350℃时效率稳定在最高值。利用程序升温方法研究了2类催化... 利用改进的溶胶凝胶法制备CuO/γ-Al2O3和CuO-CeO2-Na2o/γ-Al2O3催化吸附剂颗粒,在固定床上测试其催化脱硝活性。2类催化吸附剂250-400℃范围内脱硝效率稳定在70%以上。在350℃时效率稳定在最高值。利用程序升温方法研究了2类催化剂对NH3和NO的氧化性能,发现NH3在高于400℃下急剧氧化生成N2、NO和N2O,是脱硝效率下降的主要原因。CuO/γ-Al2O3催化剂能将NO氧化生成N02,NO在催化剂上的吸附对脱硝过程有重要作用。改进的CuO-CeO2-Na2o/γ-Al2O3催化剂能使NH3在高温400℃下不被氧化,也促进了NO在催化剂表面的吸附,从而提高了催化剂脱硝效率。催化反应的机理为NO吸附在催化剂表面,氧化生成吸附态的NO2,再与吸附催化剂上的NH3反应。 展开更多
关键词 溶胶凝胶法 CUo/γ-al2o3 Cuo—Ceo2-Na2o/γ-al2o3 NH3 No 选择性催化还原
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α-Al_2O_3的晶体结构与价电子结构 被引量:25
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作者 谭训彦 王昕 +3 位作者 尹衍升 刘英才 张金升 孟繁琴 《中国有色金属学报》 EI CAS CSCD 北大核心 2002年第z1期18-23,共6页
对α Al2 O3 的晶体结构进行了详细的讨论 ,通过各种立体插图 ,对比分析了α Al2 O3 的菱面体晶胞和六方晶胞 ,并对每种晶胞中各种原子的排列位置进行了深入分析 ,确定了某一具体位置的O2 -或Al3 + 与其它离子之间的主要键距 ,最后根据... 对α Al2 O3 的晶体结构进行了详细的讨论 ,通过各种立体插图 ,对比分析了α Al2 O3 的菱面体晶胞和六方晶胞 ,并对每种晶胞中各种原子的排列位置进行了深入分析 ,确定了某一具体位置的O2 -或Al3 + 与其它离子之间的主要键距 ,最后根据“固体与分子经验电子理论 (EET)”计算出了α Al2 O3 晶体的价电子结构 ,并以图示的方式把主要的键及键距标示在图中 ,使能直观地看到α Al2 O3 晶体中最强键及次强键等在晶体中的方位 ,便于分析α Al2 O3 的结构与性能的相互关系。 展开更多
关键词 α -al2o3 晶体结构 价电子结构
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TiO_2和α-Al_2O_3晶体的生长习性 被引量:23
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作者 李汶军 郑燕青 +2 位作者 施尔畏 陈之战 殷之文 《无机材料学报》 SCIE EI CAS CSCD 北大核心 2000年第6期968-976,共9页
通过水热法制备粉体的实验观察到金红石、锐钛矿和а-Al2O3晶体的生长习性.采用配位多面体生长习性法则合理地解释了TiO2和а-Al2O3的生长习性.其主要结果为а-Al2O3晶体的生长习性为平板{0001},其各晶... 通过水热法制备粉体的实验观察到金红石、锐钛矿和а-Al2O3晶体的生长习性.采用配位多面体生长习性法则合理地解释了TiO2和а-Al2O3的生长习性.其主要结果为а-Al2O3晶体的生长习性为平板{0001},其各晶面的生长速度为:V{0001}<V{1123}<V{0112}=V{1120}<V{0110}。金红石的生长习性为柱状,其各晶面的生长速度为:V<110><V<100>< V<101>< V<001>< V<111>;锐钛矿的生长习性为四面体,其各晶面的生长速度为K<010>=V<001>>V<010>>V<111>.而PBC理论很难合理地解释а-Al2O3晶体的生长习性. 展开更多
关键词 TIo2 Α-al2o3 生长习性 水热法 晶体生长
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钡改性的Ni/γ-Al_2O_3催化剂用于甲烷部分氧化的研究 被引量:16
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作者 王越 叶季蕾 +1 位作者 段华超 刘源 《燃料化学学报》 EI CAS CSCD 北大核心 2005年第6期750-754,共5页
800℃、80 000h-1、CH4/O2/N2=14/7/79下比较了质量分数20%的N i/-γA l2O3和Ba改性的N i/-γA l2O3催化剂,用于甲烷部分氧化反应的活性和选择性。结果表明,Ba的添加提高了镍基催化剂的活性和稳定性。BET和XRD表明,Ba的加入有利于高温... 800℃、80 000h-1、CH4/O2/N2=14/7/79下比较了质量分数20%的N i/-γA l2O3和Ba改性的N i/-γA l2O3催化剂,用于甲烷部分氧化反应的活性和选择性。结果表明,Ba的添加提高了镍基催化剂的活性和稳定性。BET和XRD表明,Ba的加入有利于高温焙烧下抑制大颗粒的N iA l2O4的形成,保持了高比例的活性镍组分,提高了催化剂催化活性。常压下,xCH4接近100%,sCO、sH2达到92.2%和98.1%,催化剂15h内活性稍微下降。Ba的加入使A l2O3的晶型转化温度由800℃提高到900℃,提高了载体的稳定性。 展开更多
关键词 甲烷 部分氧化 BA 活性 NiAl2o4 Ni/γ-al2o3
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二苯并噻吩和4-甲基二苯并噻吩在Mo和CoMo/γ-Al_2O_3催化剂上加氢脱硫的反应机理 被引量:16
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作者 徐永强 赵瑞玉 +2 位作者 商红岩 赵会吉 刘晨光 《石油学报(石油加工)》 EI CAS CSCD 北大核心 2003年第5期14-21,共8页
研究了二苯并噻吩(DBT)和4-甲基二苯并噻吩(4-MDBT)在Mo/γ-Al_2O3和CoMo/γ-Al_2O_3上加氢脱硫反应的产物分布及其可能的反应网络,并通过反应压力和温度对产物分布的影响,揭示了加氢脱硫反应的可能机理。DBT在Mo/γ-Al_2O_3上的加氢脱... 研究了二苯并噻吩(DBT)和4-甲基二苯并噻吩(4-MDBT)在Mo/γ-Al_2O3和CoMo/γ-Al_2O_3上加氢脱硫反应的产物分布及其可能的反应网络,并通过反应压力和温度对产物分布的影响,揭示了加氢脱硫反应的可能机理。DBT在Mo/γ-Al_2O_3上的加氢脱硫反应主要通过直接氢解路径和加氢路径进行,两种途径的作用相近;在CoMo/γ-Al_2O_3催化剂上的加氢脱硫主要通过直接氢解路径进行。4-MDBT在Mo/γ-Al_2O_3和CoMo/γ-Al_2O_3上的加氢脱硫反应主要通过加氢路径进行。Co的加入有助于提高Mo/γ-Al_2O_3催化剂的加氢脱硫活性,尤其是直接氢解脱硫活性。4-MDBT加氢脱硫反应中加氢路径的相对作用显著大于DBT加氢脱硫反应的加氢路径,间接证明4-MDBT的加氢脱硫过程存在对“端连吸附”的空间位阻。4-MDBT分子中甲基的供电子作用有利于促进苯环的加氢反应,从而有助于缩小与DBT分子间加氢脱硫活性的差别。在DBT和4-MDBT加氢脱硫反应中,反应压力和温度对加氢路径的影响大于对氢解路径的影响。 展开更多
关键词 二苯并噻吩 4-甲基二苯并噻吩 氧化铝 Mo/γ-al2o3 CoMo/γ-al2o3 催化剂 加氢脱硫 反应机理
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Ni^(2+)在γ-Al_2O_3上的分散状态及负载型Ni/γ-Al_2O_3催化剂的α-蒎烯加氢活性(英文) 被引量:15
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作者 任世彪 邱金恒 +3 位作者 王春燕 许波连 范以宁 陈懿 《无机化学学报》 SCIE CAS CSCD 北大核心 2007年第6期1021-1028,共8页
用X-射线衍射(XRD)、紫外-可见漫散射光谱(UV-VisDRS)、程序升温还原(TPR)、CO化学吸附和微反测试等方法研究了Ni2+在γ-Al2O3上的分散状态和负载型Ni/γ-Al2O3催化剂的α-蒎烯加氢催化活性。结果表明,当Ni2+负载量远低于其在γ-Al2O3... 用X-射线衍射(XRD)、紫外-可见漫散射光谱(UV-VisDRS)、程序升温还原(TPR)、CO化学吸附和微反测试等方法研究了Ni2+在γ-Al2O3上的分散状态和负载型Ni/γ-Al2O3催化剂的α-蒎烯加氢催化活性。结果表明,当Ni2+负载量远低于其在γ-Al2O3载体表面分散容量时,Ni2+优先嵌入载体表面四面体空位,随着Ni2+负载量的增加,嵌入载体表面八面体空位Ni2+的比例增大。由于八面体Ni2+易被还原为金属态Ni0,NiO/γ-Al2O3样品的还原度随Ni2+负载量的增加而大幅度地增加,经氢还原所得Ni/γ-Al2O3催化剂的CO吸附量和α-蒎烯加氢催化活性大幅度增加。对La2O3助剂的作用进行了研究,结果表明分散在γ-Al2O3上的La3+物种可阻止Ni2+嵌入γ-Al2O3表面四面体空位,增大了八面体Ni2+物种所占比例,提高了催化剂的还原度,故Ni-La2O3/γ-Al2O3催化剂催化活性高于Ni/γ-Al2O3催化剂。 展开更多
关键词 Ni/γ-al2o3茹Nio/γ-al2o3 分散状态 催化加氢 Α-蒎烯
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焙烧温度对CuO/γ-Al_2O_3和CeO_2-CuO/γ-Al_2O_3催化剂NO还原活性的影响 被引量:12
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作者 顾立军 谢颖 +2 位作者 刘宝生 陈小平 王乐夫 《燃料化学学报》 EI CAS CSCD 北大核心 2004年第2期235-239,共5页
用浸渍法制备了CuO γ Al2O3催化剂和CeO2改性的CeO2 CuO γ Al2O3催化剂,考察了焙烧温度对CuO γ Al2O3和CeO2 CuO γ Al2O3催化剂C3H6还原NO反应活性的影响,以及CeO2的添加量对CeO2 CuO γ Al2O3催化剂C3H6还原NO反应活性的影响。结... 用浸渍法制备了CuO γ Al2O3催化剂和CeO2改性的CeO2 CuO γ Al2O3催化剂,考察了焙烧温度对CuO γ Al2O3和CeO2 CuO γ Al2O3催化剂C3H6还原NO反应活性的影响,以及CeO2的添加量对CeO2 CuO γ Al2O3催化剂C3H6还原NO反应活性的影响。结果表明,在200℃~500℃的焙烧温度范围内,焙烧温度对CuO γ Al2O3催化剂的活性影响很小;在500℃~800℃的焙烧温度范围内,随着焙烧温度的升高CuO γ Al2O3催化剂的活性急剧下降,由XRD物相测定结果可知,归因于对反应表现惰性的尖晶石CuAl2O4相的生成。当焙烧温度为500℃时,CeO2的添加对CuO γ Al2O3催化剂的活性影响很小;当焙烧温度为800℃时,CeO2的添加对CuO γ Al2O3催化剂有明显的助催化作用,当Ce和Cu的摩尔比为1∶10时,NO转化率较为理想。 展开更多
关键词 焙烧温度 CUo/γ-al2o3 CEo2 SCR No
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碳酸铝铵低温热分解制备α-Al_2O_3超细粉末 被引量:30
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作者 杨晔 吴玉程 +1 位作者 李勇 崔平 《过程工程学报》 CAS CSCD 北大核心 2002年第4期325-329,共5页
利用硫酸铝铵溶液和碳酸氢铵溶液的沉淀反应制备碳酸铝铵前驱体,通过在碳酸铝铵中同时添加Al2O3籽晶和硝酸铵, 使得相的转变温度从1150oC降低到950oC, 获得了尺寸均匀、团聚较小、平均粒径为90 nm的球形Al2O3超细粉末. 相变过程为:无定... 利用硫酸铝铵溶液和碳酸氢铵溶液的沉淀反应制备碳酸铝铵前驱体,通过在碳酸铝铵中同时添加Al2O3籽晶和硝酸铵, 使得相的转变温度从1150oC降低到950oC, 获得了尺寸均匀、团聚较小、平均粒径为90 nm的球形Al2O3超细粉末. 相变过程为:无定型→g→g+→,并没有出现高温过渡型相q相. 展开更多
关键词 α-al2o3超细粉末 碳酸铝铵 制备 相变
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P改性NiW/γ-Al_2O_3的低温焦油芳烃组分加氢性能研究 被引量:19
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作者 佟瑞利 王永刚 +4 位作者 张旭 张海永 戴谨泽 林雄超 许德平 《燃料化学学报》 EI CAS CSCD 北大核心 2015年第12期1461-1469,共9页
以γ-Al2O3为载体,采用浸渍法制备了不同P添加量的负载型NiW加氢催化剂,采用固定床加氢装置,对模型化合物萘和低温焦油富集的芳烃组分进行了催化加氢。催化剂采用N2吸附、XRD、H2-TPR、XPS以及NH3-TPD的方法进行表征,加氢产物采用GC-MS... 以γ-Al2O3为载体,采用浸渍法制备了不同P添加量的负载型NiW加氢催化剂,采用固定床加氢装置,对模型化合物萘和低温焦油富集的芳烃组分进行了催化加氢。催化剂采用N2吸附、XRD、H2-TPR、XPS以及NH3-TPD的方法进行表征,加氢产物采用GC-MS和GC×GC-TOFMS进行分析。结果表明,P助剂能够扩大催化剂的孔径并促进活性金属组分在载体表面的分散;当P含量为1.0%1.5%时,能够促进Ni-W-O混合相生成,并提高催化剂表面弱酸的含量;萘加氢反应的转化率和十氢萘的选择性也在添加1.0%的P时达到最高,分别为80%和50%左右;低温焦油芳烃组分的催化加氢结果显示,芳烃饱和加氢反应占优,绝大部分芳烃转化为环烷烃,且催化剂具有显著的脱除杂原子效果。 展开更多
关键词 NiW/γ-al2o3 P助剂 芳烃 加氢作用
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SO_3/γ-Al_2O_3固体酸催化剂的制备、结构与酸性表征 被引量:17
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作者 姚瑞平 张铭金 +5 位作者 杨俊 易德莲 徐君 邓风 岳勇 叶朝辉 《化学学报》 SCIE CAS CSCD 北大核心 2005年第4期269-273,共5页
用酸中和法制备了活性γ-Al2O3,并在其表面负载SO3得到固体酸催化剂SO3/γ-Al2O3,用XRD,TG-DTA,FT-IR,NMR,NH3-TPD等对其进行了结构和酸性研究.结果表明:在SO3/γ-Al2O3的制备过程中形成少量的Al2(SO4)3,同时SO3与γ-Al2O3表面上的羟基... 用酸中和法制备了活性γ-Al2O3,并在其表面负载SO3得到固体酸催化剂SO3/γ-Al2O3,用XRD,TG-DTA,FT-IR,NMR,NH3-TPD等对其进行了结构和酸性研究.结果表明:在SO3/γ-Al2O3的制备过程中形成少量的Al2(SO4)3,同时SO3与γ-Al2O3表面上的羟基反应,形成强的Br?nsted酸位,根据H/27Al双共振(TRAPDOR)MASNMR与FT-IR实验1结果提出了Br?nsted酸结构模型.SO3/γ-Al2O3表面存在两种不同强度的酸中心,其酸强度大于分子筛HZSM-5,但弱于传统的固体超强酸SO24/γ-Al2O3.- 展开更多
关键词 So3 γ-al2o3 固体酸催化剂 制备 FT-IR 固体超强酸 分子筛 酸性 NH3-TPD NMR
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CuO/CeO_2-Al_2O_3催化剂中CuO物种的原位XRD、Raman和TPR表征 被引量:12
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作者 何迈 方萍 +3 位作者 谢冠群 谢云龙 闫宗兰 罗孟飞 《物理化学学报》 SCIE CAS CSCD 北大核心 2005年第9期997-1000,共4页
采用原位XRD、激光Raman光谱和TPR(程序升温还原)技术研究了CuO(w,%)/CeO2-Al2O3催化剂中CuO物种的存在形式及其CuO物种的迁移.低温焙烧(300℃)催化剂,CuO以高分散和晶相两种形式存在于CeO2-Al2O3载体表层.随着焙烧温度的升高,CuO开始... 采用原位XRD、激光Raman光谱和TPR(程序升温还原)技术研究了CuO(w,%)/CeO2-Al2O3催化剂中CuO物种的存在形式及其CuO物种的迁移.低温焙烧(300℃)催化剂,CuO以高分散和晶相两种形式存在于CeO2-Al2O3载体表层.随着焙烧温度的升高,CuO开始从表层向CeO2内层迁移.处于内层的CuO部分以晶相形式存在,部分与Al2O3载体反应生成CuAl2O4.高温有利于表层CuO向CeO2内层迁移,同时促进CuAl2O4生成.结果表明结合原位XRD、激光Raman光谱和TPR技术可以有效地观察催化剂中CuO物种的存在形式和分布. 展开更多
关键词 Cuo/Ceo2-al2o3 XRD RAMAN TPR Cuo迁移 固相反应
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VOCs催化燃烧催化剂Mn/γ-Al_2O_3和CuMn/γ-Al_2O_3的性能研究 被引量:45
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作者 黄海凤 陈银飞 +1 位作者 唐伟 卢晗锋 《高校化学工程学报》 EI CAS CSCD 北大核心 2004年第2期152-155,共4页
用浸渍法制备了两种负载型的Mn/y-Al2O3和Cu-Mn/γ-Al2O3复合氧化物催化剂,同时用共沉淀法制备了Cu-Mn-O复合氧化物催化剂.以气相色谱为检测手段,用常压气体流动评价装置考察了这三种催化剂对苯、甲苯、二甲苯等挥发性有机化合物VOCs的... 用浸渍法制备了两种负载型的Mn/y-Al2O3和Cu-Mn/γ-Al2O3复合氧化物催化剂,同时用共沉淀法制备了Cu-Mn-O复合氧化物催化剂.以气相色谱为检测手段,用常压气体流动评价装置考察了这三种催化剂对苯、甲苯、二甲苯等挥发性有机化合物VOCs的催化燃烧性能.发现负载型的催化剂转化率达到99%时的反应温度比非负载型的降低30~40℃C,其中Cu-Mn/γ-Al2O3催化剂具有更好的低温活性,催化燃烧反应的速率明显提高.负载型催化剂表面的活性组分以高度分散状态存在和催化剂高的比表面积是性能好的主要原因. 展开更多
关键词 VoCS 催化燃烧 Cu-Mn复合氧化物 γ-al2o3载体 负载型催化剂
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Fe_2O_3/YSZ-γ-Al_2O_3催化剂在甲烷催化燃烧中的催化性能研究 被引量:19
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作者 李丽娜 陈耀强 +1 位作者 龚茂初 向云 《高等学校化学学报》 SCIE EI CAS CSCD 北大核心 2003年第12期2235-2238,共4页
以 Fe2 O3 为活性组分 ,γ-Al2 O3 ,Zr O2 -γ-Al2 O3 及 YSZ-γ-Al2 O3 ( YSZ是用 Y2 O3 稳定 Zr O2 的催化剂载体 )为载体 ,制备了 3种甲烷燃烧催化剂 .其中以 YSZ-γ-Al2 O3 为载体的催化剂催化性能最好 .XPS检测发现 ,Zr O2 和 Y2 ... 以 Fe2 O3 为活性组分 ,γ-Al2 O3 ,Zr O2 -γ-Al2 O3 及 YSZ-γ-Al2 O3 ( YSZ是用 Y2 O3 稳定 Zr O2 的催化剂载体 )为载体 ,制备了 3种甲烷燃烧催化剂 .其中以 YSZ-γ-Al2 O3 为载体的催化剂催化性能最好 .XPS检测发现 ,Zr O2 和 Y2 O3 的存在可以增加和稳定 Fe2 O3 的表面浓度 ,同时也可减弱 Fe2 O3 与γ-Al2 O3 之间的相互作用 .Fe2 O3 质量分数为 1 0 %的 Fe2 O3 /YSZ-γ-Al2 O3 催化剂具有最佳的催化活性 .XRD测试结果表明 ,该催化剂的活性与 Fe2 O3 在载体上的分散状况有关 . 展开更多
关键词 Fe2o3/YSZ-γ-al2o3 催化剂 甲烷 催化燃烧 催化性能 氧化铝 三氧化铁 制备
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