Fe、N共掺杂TiO2纳米管阵列的制备及可见光光催化活性

应用电化学阳极氧化法结合浸渍和退火后处理制备了Fe和N共掺杂的TiO2纳米管阵列光催化剂,并用场发射扫描电镜(FESEM)、X射线衍射(XRD)、X射线光电子能谱(XPS)和俄歇电子能谱(AES)仪对其进行了表征.结果表明,Fe、N共掺杂对TiO2纳米管阵列的形貌和结构没有明显影响,Fe和N均掺入了TiO2晶格.紫外-可见(UV-Vis)漫反射光谱显示Fe和N共掺杂TiO2纳米管阵列的吸收带边较纯TiO2纳米管阵列和单一掺杂TiO2纳米管阵列红移,可见光吸收增强.以可见光催化降解罗丹明B(RhB)考察了材料的光催化活性,Fe和N共掺杂TiO2纳米管阵列对RhB的降解速率较纯TiO2纳米管阵列和单一掺杂TiO2纳米管阵列明显提高,证明了Fe、N共掺杂产生的协同效应提高了TiO2纳米管阵列在可见光照射下的光催化活性.     

利用SnO2:Sb干凝胶部分升华产物处理ZnS:Mn荧光粉

以SnCl2•2H2O、SbCl3为原料, 通过溶胶-凝胶法制备SnO2:Sb干凝胶. 利用干凝胶氧化过程中的部分升华产物对新制的ZnS:Mn荧光粉进行了表面处理. 在固定氧气流量和氧化时间的条件下, 考察了SnO2:Sb干凝胶与ZnS:Mn荧光粉的质量比和氧化温度对处理后荧光粉电阻率的影响. 当干凝胶粉与荧光粉的质量比为3.0, 氧化温度为500 ℃处理后荧光粉的电阻率明显下降. 对处理后的荧光粉进行了室温光致荧光(PL)光谱、X射线衍射(XRD)以及透射电镜(TEM)分析. 结果表明对荧光粉进行表面处理没有改变荧光粉的光致发光性质和晶体结构.     

双金属同构金属-有机框架材料CAU-21-Al/M的合成、氮气吸附及复合膜性能

通过掺杂金属的方式实现了双金属同构金属-有机框架材料的制备, 采用X射线粉末衍射(PXRD)确定了多种金属在双金属CAU-21材料中的最大掺杂量, 使用扫描电子显微镜(SEM)观察了掺杂金属对材料形貌的影响. 热重分析(TGA)结果表明, CAU-21系列材料均具有较好的热稳定性. 氮气气体吸附测试及以CAU-21-Al/M为填料的混合基质膜对N₂气的渗透实验结果与掺杂金属离子尺寸大小呈相反的关系, 证实了双金属可实现对孔道结构及气体吸附性能的调控.     

过渡金属掺杂TiO_2/活性炭复合体的制备及双协同光催化性能

以活性炭为载体,通过溶胶-凝胶法分别制备了Fe、Ag、Zn、Mn和Cr过渡金属离子掺杂TiO2/活性炭(X-TiO2/AC,X-TA;X:过渡金属离子)复合体,利用X射线衍射(XRD)、比表面积(BET)、X光电子能谱(XPS)、扫描电镜(SEM)、电子自旋共振谱(ESR)和荧光光谱(FS)对其结构进行表征.以罗丹明B的光催化降解为探针实验,评价掺杂负载型复合体的双协同光催化性能和使用寿命,提出双协同光催化扩增机制,并探讨了掺杂率和负载率对双协同扩增效果影响.结果表明:通过活性炭吸附和离子掺杂对TiO2光催化性能表现出双协同扩增作用,导致X-TA对罗丹明B的降解速率常数kapp大于掺杂X-TiO2粉体和TA负载体之和.同时,掺杂率和负载率共同影响协同效应,当Fe离子掺杂率和Fe-TiO2负载率分别为0.3%和10%时,Fe-TA复合体kapp最大为0.0208min-1.另外,过渡金属离子掺杂对TiO2光催化性能提高程度按掺杂离子Ag、Zn、Mn、Cr、Fe递增.掺杂后金属离子的价态、得电子能力、比表面积和掺杂TiO2颗粒尺寸上的差异决定了不同离子掺杂负载型复合体催化性能不同,复合体寿命降低的主要原因是由于活性组分从载体上流失所引起.     

钯/掺杂锰氧八面体分子筛催化一步合成碳酸二苯酯

采用浸渍法制备出Ce3＋, Cu2＋, Pb2＋, Ag＋, Fe3＋掺杂锰氧八面体分子筛, 负载钯后用于一步氧化羰基化合成碳酸
二苯酯(DPC)反应. Pd/Cu-OMS-2 催化活性最高, DPC 收率为12.1%. 通过X 射线衍射(XRD), 扫描电镜(SEM), 氮气吸
附(BET)和X 射线光电子能谱(XPS)对催化剂样品进行了表征. 表征结果表明, 不同金属离子掺杂后, 催化剂的晶型仍
保持隐钾锰矿结构. 从电位滴定测试数据来看, 杂质离子引入后, 锰的平均氧化态增加. 在催化反应过程中, Mn4＋/
Mn2＋和Pd2＋/Pd0 构成了氧化还原循环链, Mn3＋的存在可以补充反应过程中消耗掉的Mn4＋. XPS 分析了晶体中氧物种的
存在形式, 化学吸附氧/(晶格氧＋化学吸附氧)的比值越高, 催化活性越好.     

锂电池正极材料Li1.06Mn0.8Cr0.14O2的水热合成及其光谱研究

采用水热方法合成了掺铬锂锰氧化合物, X射线衍射和Raman光谱分析结果表明, 所得材料为具有NaFeO2结构的晶体. 由等离子发射光谱(CIP)确定其组分为Li1.06Mn0.8Cr0.14O2. X射线光电子能谱(XPS)研究结果表明, 与未掺杂的LiMnO2相比, 所得材料中Mn的平均价态增加, 这将抑制因Mn3+离子的存在而产生的Jahn-Teller畸变, 有利于提高材料的电化学循环性能.     

Mn离子掺杂对α-FeOOH结构和形貌的影响

本文采用水热合成方法,在120℃碱性条件下制备出形貌均一的短棒状α-FeOOH纳米粒子,对其进行了金属离子Mn的掺杂。系统研究了Mn离子掺杂对产物物相结构和形貌的影响,对产物进行了X射线衍射(XRD)、红外光谱(IR)、穆斯堡尔谱(MES)、场发射扫描电镜(FE-SEM)和高分辨透射电子显微镜(HRTEM)表征。结果表明:低浓度Mn离子掺杂对α-FeOOH的形成起了形貌和物相调控作用。α-FeOOH纳米棒的长径比随着Mn离子加入量的增大逐渐增加;当nMn(Ⅱ)/nFe(Ⅲ)=0.30时,产物变成了α-(Fe,Mn)OOH和MnFe2O4的混合物,形貌为纳米棒和纳米颗粒。     

掺杂纳米TiO2光催化性能的研究

利用浸渍法分别制备了Cr、Mn、Fe、Co、Ni、Cu六种过渡金属离子掺杂改性的二氧化钛光催化剂，以乙酸水溶液的光催化氧化反应和二氧化碳还原反应为探针,评价了掺杂催化剂的光催化性能.借助光电子能谱（XPS）、X射线衍射分析（XRD）等手段对掺杂催化剂进行了表征.研究结果表明，经过渡金属离子掺杂后，光催化性能均有不同程度的改善，改善程度按Cr、Co、Ni、Fe、Mn、Cu递增.掺杂后催化剂表面吸附氧的活泼性、金属离子的价态及得电子能力上的差异决定了不同离子掺杂纳米二氧化钛光催化性能的差异.     

钛离子掺杂对LiFe0.6Mn0.4PO4/C 电化学性能的影响

采用固相法合成了钛离子掺杂LiFe0.6Mn0.4PO4/C正极材料.通过X射线衍射(XRD)、扫描电镜(SEM)以及电化学测试,对合成材料的结构、形貌和电化学性能进行了表征.结果表明:钛离子掺杂未影响材料的晶型结构,但显著改善了材料的电化学性能;Li(Fe0.6Mn0.4)0.96Ti0.02PO4/C材料表现出优异的倍率性能,0.1C倍率下其比容量为160.3mAh.g-1;在10C倍率下,比容量为134.7mAh.g-1;特别是在20C高倍率下仍然具有124.4mAh.g-1的放电比容量.电化学交流阻抗谱(EIS)和循环伏安(CV)测试结果说明,通过钛离子掺杂导致材料阻抗和极化的减少是材料倍率性能改善的主要原因.     

氮掺杂还原氧化石墨烯负载铂催化剂的制备及甲醇电氧化性能

采用高温热解聚苯胺修饰的氧化石墨烯(PANI-GO),得到了氮掺杂的还原氧化石墨烯碳材料(N-RGO),以其负载Pt制备了Pt/N-RGO纳米结构电催化剂.采用透射电镜(TEM)、X射线光电子能谱(XPS)、X射线衍射(XRD)谱及拉曼光谱等技术对N-RGO和Pt/N-RGO的形貌及结构进行了表征,用循环伏安、计时电流等电化学技术研究了Pt/N-RGO电极催化剂对CO溶出反应和甲醇电氧化反应的催化性能.结果表明:高温热解PANIGO可同时实现GO的还原及其氮掺杂的过程,氮掺杂引起还原氧化石墨烯碳材料表面缺陷结构和导电性的增加;与相应的未掺杂氮样品Pt/RGO相比较,Pt/N-RGO样品上Pt颗粒的分散更均匀,显示出更强的抗CO毒化能力和更高的甲醇电氧化催化活性及稳定性.     

CuZnAl mixed-metal oxides prepared by a novel sol–gel route and the application for synthesis of 2- methylpyrazine

Metal (Cu, Zn, Al) nitrates and chlorides were used for preparing CuZnAl xerogels by a sol–gel route with propylene oxide as gelation initiator. The CuZnAl mixed-metal oxides were further obtained by thermal treatment the xerogels at 500 °C for 5 h in air. Thermal decomposition behavior of the CuZnAl xerogels, the microstructures and the reducibility of the calcined xerogels were investigated by thermogravimetry (TG), scanning electron microscope (SEM), powder X-ray diffraction (XRD), N₂ adsorption/desorption (BET, BJH) and temperature-programmed reduction (TPR) techniques. The catalytic activity in dehydrocyclization of ethylenediamine (ED) with 1, 2-propyleneglycol (PG) to 2-methylpyrazine (2-MP) was carried out at 380 °C. The results displayed that the CuZnAl mixed-metal oxides prepared using nitrates as the metal precursors had a higher metallic Cu dispersion and a superior low-temperature reducibility than those prepared by chlorides, which results in a higher catalytic activity for the synthesis of 2-methylpyrazine. Especially when the molar ratio of Cu/Zn/Al = 2:1:2, the catalyst using nitrates as the metal precursors improved the selectivity of 2-MP to 87.5%.     

Vanadia-Silica Catalysts Prepared by Sol–Gel Method: Application for Epoxidation Reaction

Vanadia-silica xerogel and aerogel catalysts, with various V/Si molar ratios (0.05, 0.1, and 0.2), were prepared by sol–gel processing. Gels were obtained under acid catalysed conditions (HNO₃) from vanadium (III) acetylacetonate (V(acac)₃) and tetraethoxysilane (TEOS). Under these conditions, it was found that the gelation time increased with V/Si molar ratio. The structure and catalytic properties of the mixed oxides were found to be mainly influenced by the V/Si molar ratio and drying mode. The catalytic behaviour of the xerogels and aerogels was tested in the epoxidation reaction of trans-2-hexen-1-ol. The results showed that the V/Si molar ratio did not significantly influence the catalytic activity, although the effect of drying (xerogel vs. aerogel) was remarkable. Using a molar ratio TBHP/alcohol = 4/7, the epoxide yield was about 50% in the presence of xerogels, with ca. 8 h required to achieve stationary-conversion conditions in this heterogeneous-catalysis system. In contrast, the aerogel catalysts required only 2 h to reach stationary conversion conditions, due to partial leaching of the vanadium species from the solid and the associated contribution of a relatively rapid homogeneous catalysis mechanism to the overall conversion. These differences in catalytic behaviour were related to the vanadium speciation and the texture of the catalysts. To explore the origin of these differences, the catalysts were characterised by nitrogen physisorption, XPS, Raman spectroscopy, TGA/DTA and XRD.     

Methane reforming With CO2 to syngas over CeO2-promoted Ni/Al2O3-ZrO2 catalysts Prepared Via a direct sol-gel process

CeO2-promoted Ni/Al2O3-ZrO2 (Ni/Al2O3-ZrO2-CeO2) catalysts were prepared by a direct sol-gel process with citric acid as gelling agent. The catalysts used for the methane reforming with CO2 was studied by infrared spectroscopy (IR), thermal gravimetric analysis (TGA), microscopic analysis, X-ray diffraction (XRD) and temperature-programmed reduction (TPR). The catalytic performance for CO2 reforming of methane to synthesis gas was investigated in a continuous-flow micro-reactor under atmospheric pressure. TGA, IR, XRD and microscopic analysis show that the catalysts prepared by the direct sol-gel process consist of Ni particles with a nanostructure of around 5 nm and an amorphous-phase composite oxide support. There exists a chemical interaction between metallic Ni particles and supports, which makes metallic Ni well dispersed, highly active and stable. The addition of CeO2 effectively improves the dispersion and the stability of Ni particles of the prepared catalysts, and enhances the adsorption of CO2 on the surface of catalysts. The catalytic tests for methane reforming with CO2 to synthesis gas show that the Ni/Al2O3-ZrO2-CeO2 catalysts show excellent activity and stability compared with the Ni/Al2O3 catalyst. The excellent catalytic activity and stability of the Ni/Al2O3-ZrO2-CeO2 are attributed to the highly, uniformly and stably dispersed small metallic Ni particles, the high reducibility of the Ni oxides and the interaction between metallic Ni particles and the composite oxide supports.     

Mechanism of One-Step Hydrothermally Synthesized Titanate Catalysts for Ozonation

A titanate nanotube catalyst for ozonation was synthesized with a simple one-step NaOH hydrothermal treatment without energy-consuming calcination. The synthesized titania catalysts were characterized by X-ray diffraction (XRD), Raman, porosimetry analysis, high-resolution transmission electron microscopy (HR-TEM), Fourier transformed infrared (FTIR), and electron paramagnetic resonance (EPR) analysis. The catalyst treated with a higher concentration of NaOH was found to be more catalytically active for phenol removal due to its higher titanate content that would facilitate more OH groups on its surface. Furthermore, the main active oxidizing species of the catalytic ozonation process were recognized as singlet oxygen and superoxide radical, while the hydroxyl radical may only play a minor role. This work provides further support for the correlation between the properties of titania and catalytic performance, which is significant for understanding the mechanism of catalytic ozonation with titania-based materials.     

CeO2-Al2O3负载金催化剂用于水煤气变换反应的催化活性

采用浸渍法和沉积 沉淀法制备了CeO₂-Al₂O₃复合氧化物,比较了复合氧化物负载纳米金催化剂对水煤气变换反应的催化活性。通过N2物理吸附、XRD、TEM、H₂-TPR等表征手段对复合氧化物及其负载金催化剂的物相和结构进行分析,发现复合氧化物的制备方法及其焙烧温度对其比表面积、孔结构及水煤气变换反应活性有明显的影响。与沉积 沉淀法相比,浸渍法制备的CeO₂-Al₂O₃复合氧化物具有较大的CeO₂晶粒尺寸,经500℃焙烧后再负载金,所得催化剂具有更高的活性,250℃时CO转化率可达78.1%。     

Nickel ferrite spinel as catalyst precursor in the dry reforming of methane:Synthesis,characterization and catalytic properties

Dry reforming of methane by CO2 using nickel ferrite as precursor of catalysts was investigated.Nickel ferrite crystalline particles were prepared by coprecipitation of nitrates with NaOH or ammonia followed by calcination,or by hydrothermal synthesis without calcination step.The textural and structural properties were determined by a number of analysis methods,including X-ray diffraction (XRD),Raman spectroscopy and X-ray photoelectron spectroscopy (XPS),among which X-ray diffraction (XRD) was at room and variable temperatures.All synthesized oxides showed the presence of micro or nanoparticles of NiFe2O4 inverse spinel,but Fe2O3 (hematite) was also present when ammonia was used for coprecipitation.The reducibility by hydrogen was studied by temperature-programmed reduction (TPR) and in situ XRD,which showed the influence of the preparation method.The surface area (BET),particle size (Rietveld refinement),as well as surface Ni/Fe atomic ratio (XPS) and the behavior upon reduction varied according to the synthesis method.The catalytic reactivity was investigated using isopropanol decomposition to determine the acid/base properties.The catalytic performance of methane reforming with CO2 was measured with and without the pre-treatment of catalysts under H2 in 650-800 C range.The catalytic conversions of methane and CO2 were quite low but they increased when the catalysts were pre-reduced.A significant contribution of reverse water gas shift reaction accounted for the low values of H2 /CO ratio.No coking was observed as shown by the reoxidation step performed after the catalytic reactions.The possible formation of nickel-iron alloy observed during the study of reducibility by hydrogen was invoked to account for the catalytic behavior.     

溶胶-凝胶法制备Ni-SiO2催化剂的表征与性能

以正硅酸乙酯和硝酸镍为原料,采用溶胶-凝胶法,将硝酸镍分别溶于水和乙醇制得凝胶,分别经超临界干燥和常规干燥制备了一系列Ni-SiO2气凝胶和干凝胶催化剂,运用BET、XRD、TPR、IR、H2-TPD和活性评价等方法对催化剂的物理化学性质和催化间二硝基苯加氢性能进行研究.结果表明,Ni-SiO2气凝胶催化剂均具有较高的比表面积,但由于金属镍烧结导致活性比表面积较小,加氢性能较差;以乙醇为溶剂制备的干凝胶催化剂的镍物种分散度较高,但镍与载体之间的相互作用过强,致使催化剂的还原度降低,活性组分利用率下降;以水为溶剂制备的干凝胶催化剂具有较高的活性比表面积,表现出很高的催化活性和选择性.     

Ni-Al类水滑石的制备及其Ni/Al2O3加氢脱硫研究

采用共沉淀方法合成了不同Ni/Al比的镍铝类水滑石,将其作为催化剂前驱体,制备了Ni/Al2O3加氢脱硫催化剂.通过X射线衍射法(XRD),程序升温还原(H2-TPR),热重分析(TG),傅里叶变换红外光谱(FT-IR)等技术对催化剂进行了表征.利用10 mL固定床装置在不同温度,压力,体积空速和氢油比条件下对Ni/Al2O3催化剂的加氢脱硫活性进行了评价.结果表明,XRD图和FT-IR图中均出现了Ni-Al类水滑石的特征峰,TG图呈现出两个明显阶段的失重,在Ni-Al2O3-HT的XRD图中最强的衍射角对应单质金属Ni粒子的(111)晶面.脱硫结果显示Ni-Al类水滑石作为前驱体在适当的条件下,FCC汽油的硫含量降至10 ppm以下.类水滑石作为前驱体的Ni/Al2O3加氢脱硫活性很好,说明类水滑石作为前驱体在加氢脱硫领域有好的应用前景.     

NiO/LaMnO3催化剂用于乙醇水蒸气重整反应

采用柠檬酸络合-浸渍法制备了NiO/LaMnO3钙钛矿型复合氧化物催化剂并将其应用于乙醇水蒸汽重整制氢反应, 考察了NiO含量、焙烧温度对催化剂性能的影响, 采用XRD、TPR和热分析等手段对催化剂进行了表征. 结果表明, 该催化剂具有高活性、高选择性和良好的稳定性. 催化剂中的NiO含量和焙烧温度对催化性能有显著影响. 在原料气体积组成为20%(体积分数, φ) C2H5OH 和水以及80%(φ)N2, 其中水醇摩尔比为3:1, 空速为80000 mL·h-1·g-1 cat, 反应温度为400 ℃时, 15%(质量分数, w)的NiO/LaMnO3上, 乙醇转化率接近100%. 关联催化剂活性和TPR及XRD实验结果, 发现催化剂的高活性源于由催化剂前驱体中进入钙钛矿型复合氧化物晶格中的镍离子被还原所得的金属镍.     

铈镧比对CexNi0.5La0.5-xO系催化剂甘油氧化蒸汽重整制氢性能的影响

利用共沉淀法制备了CeO₂和La₂O₃复合载体的Ce_xNi_0.5La_0.5-xOO(CeNiLaO)系催化剂,在固定床反应器中考察其甘油氧化蒸汽重整制氢(OSRG)性能,并采用X射线衍射(XRD)、程序升温还原(H₂-TPR)、激光拉曼光谱(Raman)、扫描电子显微镜(SEM)、透射电子显微镜(TEM)和X射线光电子能谱(XPS)等手段对催化剂进行表征分析。结果表明：La₂O₃能够有效地分散Ni颗粒,减弱Ni颗粒在反应过程中的烧结,CeO₂提供的晶格氧能够消除催化剂表面的积碳,同时La会部分进入Ce的晶格取代部分Ce⁴⁺造成晶格畸变,提高表面的氧空穴数。La₂O₃和CeO₂的共同作用有利于减弱Ni因为烧结和积碳引起的失活。在不同Ce/La摩尔比的催化剂中,Ce_0.4Ni_0.5La_0.1O表现出最好的催化活性,并且该催化剂在长达210 h的稳定性测试中,甘油的转化率都在95%以上,气相产物中的氢气浓度达50%。