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1.
以γ-Al2O3为载体,采用等体积浸渍法,制备了不同K2CO3含量的Ni-Cu-Mn-K/Al2O3水煤气变换催化剂,采用低温N2吸附、XRD、TPD和TPR,考察了K2CO3含量对催化剂结构和性能的影响。结果表明:K2CO3的加入使催化剂的还原温度有所提高,适量的K2CO3能增加活性组分的电子密度,从而增强其给电子活化CO的能力,提高催化剂的活性。但过量的K2CO3使得催化剂比表面积和孔容降低,且导致催化剂对CO吸附过强,催化活性降低。当Ni-Cu-Mn-K/γ-Al2O3催化剂中K2CO3的添加量为7.5%时,且催化剂经530 ℃耐热15 h后,在350 ℃时水煤气变换反应中CO转化率达62.29%。  相似文献   

2.
通过水热法合成具有协同机制的三元复合材料Bi2Fe4O9/g-C3N4/UiO-66,研究表明三元复合光催化剂的催化活性要高于二元材料和纯材料。这主要是由于Bi2Fe4O9更易于和g-C3N4结合形成稳定的Z-scheme异质结结构,使三元复合材料增强了可见光响应能力,提高了电子-空穴分离能力,增强了空穴和电子的氧化还原能力。  相似文献   

3.
通过水热法合成具有协同机制的三元复合材料Bi2Fe4O9/g-C3N4/UiO-66,研究表明三元复合光催化剂的催化活性要高于二元材料和纯材料。这主要是由于Bi2Fe4O9更易于和g-C3N4结合形成稳定的Z-scheme异质结结构,使三元复合材料增强了可见光响应能力,提高了电子-空穴分离能力,增强了空穴和电子的氧化还原能力。  相似文献   

4.
基于低成本、无毒害、光吸收性强的四氧化三铁(Fe3O4)和大比表面、高稳定性的水滑石(LDHs),制备了Fe3O4@MAl-LDHs (M=Zn、Co、Ni)复合物并用于典型偶氮染料亚甲基蓝的光催化降解。通过X射线粉末衍射(XRD)、紫外可见(UV-Vis)吸收光谱、扫描电子显微镜(SEM)、透射电子显微镜(TEM)以及N2吸附-脱附测试表征了复合材料的组成与结构。光催化实验表明,最佳反应条件为催化剂用量50 mg、光照强度500 W、pH=9、反应温度40℃,此时,Fe3O4@MAl-LDHs复合材料对亚甲基蓝的降解率从LDHs的23.2%大幅提升到87.0%。LDHs对亚甲基蓝的降解主要来自·OH,而Fe3O4@CoAl-LDHs光降解活性的贡献主要由·OH和空穴提供。此外,LDHs和Fe3O4@CoAl-LDHs的电化学性质也存在较大差异。  相似文献   

5.
首次采用简单的一锅法制备了Fe2O3/Fe2TiO5异质结纳米材料。构建S型异质结后,与纯的Fe2O3和Fe2TiO5相比,Fe2O3/Fe2TiO5复合材料表现出更高的光催化降解速率和效率。经过2.5 h的光照后,Fe2O3/Fe2TiO5可以降解接近100%的亚甲基蓝(MB)。在Fe2O3/Fe2TiO5复合材料中,Fe2O3和Fe2TiO5之间形成了内建电场,可以促进光生电子-空穴对的分离。因此,具有更高能量的Fe2TiO5导带中的电子和具有更高能量的Fe2O3价带中的空穴可以得到有效的保留,从而使它们更加有效地扩散到催化剂表面,并参加降解反应。此外,Fe2O3/Fe2TiO5复合材料具有很好的光催化稳定性。  相似文献   

6.
采用溶胶-凝胶法制备了一系列不同Al2O3含量的SiO2-Al2O3复合氧化物,以该系列复合氧化物为载体,采用等体积浸渍法制备了Ni负载量15%(重量百分比)的催化剂,用于催化乙酰丙酸加氢制γ-戊内酯.采用N2物理吸附、X射线衍射(XRD)、H2程序升温还原(H2-TPR)、H2程序升温脱附(H2-TPD)、NH3程序升温脱附(NH3-TPD)和吡啶吸附红外(Py-IR)等手段对催化剂进行了表征.结果表明,不同载体催化剂的活性组分分散度及表面酸性质存在明显差异,显著影响了催化剂吸附、活化H2与C=O键的能力,进而影响了催化剂的乙酰丙酸加氢活性.其中,Ni/SiO2-Al2O3催化剂上的L酸中心能够促进C=O键的吸附、活化,与金属Ni上的H2吸附活性位协同作用,大大提高了乙酰丙酸加氢活性.因此,具有最多L酸中心和丰富H2吸附活性位的Ni/SiO2-8Al2O3催化剂表现出最高的乙酰丙酸加氢活性,在180℃、4 MPa氢气压力下,乙酰丙酸转化率达到90.5%,目标产物γ-戊内酯选择性为100%.  相似文献   

7.
采用色谱-微反流动法反应装置考察了w%CuO/15%TiO2/γ-Al2O3催化剂对NO+CO的反应活性;催化剂经空气氛或氢气氛预处理后,NO转化率达100%的反应温度分别是325和275 ℃;XRD仅能检测到γ-Al2O3晶相,负载15%CuO后可以检测到微弱的CuO晶相;H2-TPR能检测到2个CuO的还原峰(α和β峰),将其归属于高度分散的CuO分别在裸露的γ-Al2O3和TiO2/γ-Al2O3载体上的还原;原位红外分析结果表明催化剂经空气氛或氢气氛预处理后,吸附NO+CO反应气后,反应的中间产物N2O出现的温度分别为200和150 ℃。  相似文献   

8.
王挺  吴礼光  蒋新 《无机化学学报》2011,27(8):1477-1482
利用吸附相反应技术制备得到了掺杂不同浓度的Fe2O3的TiO2复合光催化剂。通过透射电子显微镜(TEM)、紫外可见光谱和X射线衍射(XRD)研究不同掺杂浓度对TiO2形貌和结晶过程的影响,并利用3种波长光源下的甲基橙光降解实验考评了各个复合光催化剂的催化活性。结果表明,掺杂后复合光催化剂中Fe2O3分散性较好较均匀。在TiO2紫外可见吸收光谱中由于Fe2O3的掺杂而出现了红移,而且随着掺杂浓度增加红移越来越明显,复合光催化剂的禁带宽度也越来越小。在焙烧过程中无定形Fe2O3或Fe3+进入了TiO2的晶格结构,从而抑制了TiO2的结晶过程。半导体禁带宽度的减少以及TiO2结晶过程的抑制作用,都导致紫外光下复合光催化剂催化活性的降低。但Fe2O3的掺杂也使得复合光催化剂在可见光区出现了一定的光催化活性。  相似文献   

9.
采用高温固相法在空气中合成了Ba1.97-yZn1-xMgxSi2O7:0.03Eu,yCe3+系列荧光粉。分别采用X-射线衍射和荧光光谱对所合成荧光粉的物相和发光性质进行了表征。在紫外光330~360 nm激发下,固溶体荧光粉Ba1.97-yZn1-xMgxSi2O7:0.03Eu的发射光谱在350~725 nm范围内呈现多谱峰发射,360和500 nm处有强的宽带发射属于Eu2+离子的4f65d1-4f7跃迁,590~725 nm红光区窄带谱源于Eu3+5D0-7FJ (J=1,2,3,4)跃迁,这表明,在空气气氛中,部分Eu3+在Ba1.97-yZn1-xMgxSi2O7基质中被还原成了Eu2+;当x=0.1时,荧光粉Ba1.97Zn0.9Mg0.1Si2O7:0.03Eu的绿色发光最强,表明Eu3+被还原成Eu2+离子的程度最大。当共掺入Ce3+离子后,形成Ba1.97-yZn0.9Mg0.1Si2O7:0.03Eu,yCe3+荧光粉体系,其发光随着Ce3+离子浓度的增大由蓝绿区经白光区到达橙红区;发现名义组成为Ba1.96Zn0.9Mg0.1Si2O7:0.01Ce3+,0.03Eu的荧光粉的色坐标为(0.323,0.311),接近理想白光,是一种有潜在应用价值的白光荧光粉。讨论了稀土离子在Ba2Zn0.9Mg0.1Si2O7基质中的能量传递与发光机理。  相似文献   

10.
SrAl12O19:Mn4+是一种用于高显色性白光发光二极管的候选红色荧光材料。本论文研究了Mg2+、Zn2+和Ge4+离子的掺杂效应以及Ge3+、Ca2+和Ba2+离子的取代效应SrAl12O19:Mn4+荧光材料性能的影响。样品通过高温固相反应制备,焙烧温度在1 250~ 1 500℃之间。利用X射线衍射技术表征了材料的相纯度,用荧光激发光谱和发射光谱表征了材料的荧光性能。研究结果指出,与未进行Mg2+或Zn2+掺杂的样品相比,Mg2+或Zn2+离子对Al3+格位的掺杂可以使材料的发光强度提高~60%,其原因被认为是掺杂促进了激活剂Mn4+离子进入晶格,其过程可以表示为:MO+MnO2=MAl''+MnAl·+3OO×(M=Mg,Zn),电子顺磁共振谱支持这一结果。Ge4+离子的掺杂使材料的发光性能明显下降。Ge3+离子可以取代Al3+离子形成全范围的固溶体,其中少量Ge3+离子的掺杂可以使材料的荧光发射强度提高~13%,而掺杂量进一步提高使材料的荧光性能下降。Ca2+和Ba2+对Sr2+的取代仅形成有限范围的固溶体。Ca2+的取代使材料的发光性能提高;而 Ba2+的取代使材料的发光强度下降。  相似文献   

11.
用溶胶凝胶法制备了一组NixCo1-xCoAlO4尖晶石型复合氧化物,并采用表面润湿浸渍K2CO3溶液进行了K掺杂改性,用于有氧气氛下的N2O催化分解反应.采用N2物理吸附、X-射线衍射(XRD)、扫描电镜(SEM)、H2-程序升温还原(H2-TPR)等技术对催化剂进行了表征,考察了催化剂组成、母液pH值、K负载量等制备参数对其催化活性的影响.结果表明,母液pH值为3、K/(Ni+Co)物质的量比为0.1的K/Ni0.15Co0.85CoAlO4催化剂具有较高的N2O分解活性,450 ℃ N2O可完全分解.助剂K的加入弱化了催化剂表面金属氧键,提高了催化剂的还原性、催化活性和抗水性.  相似文献   

12.
N2O decomposition was examined over a series of Al2O3-Fe2O3 mixed oxidic solids with composition ranging from 0 to 100% of Fe2O3. The catalytic activity of the solids runs parallel to the number of atoms of iron in the Al2−x FexO3 solid solution phase. Two compensation effects are present. The first corresponds to catalysts rich in alumina, and the second one to catalysts rich in hematite. This revised version was published online in June 2006 with corrections to the Cover Date.  相似文献   

13.
Mixtures of NiCo2O4 and FeO x were obtained by thermal decomposition of the nitrates of Ni, Co, and Fe in appropriate proportions. Two series of electrodes were prepared: (1) at constant composition (20 mol% FeO x ) and various calcination temperatures in the range 200 to 480 °C and (2) at constant calcination temperature (300 °C) and various compositions in the whole composition range 0 to 100 mol% FeO x . The oxide layers were characterized by thermogravimetric analysis, X-ray diffraction, scanning electron microscopy, and cyclic voltammetry. Experimental data showed that the layers consist of a mixture of phases in which Fe oxide is present as Fe2O3. The electrocatalytic properties were assessed by means of quasi-stationary potentiostatic current-potential curves for the O2 evolution reaction from alkaline solution. Results have shown that the mechanism of O2 evolution depends on composition moderately. The electrocatalytic activity appears to depend on composition only slightly. Dedicated to Professor Oleg Petrii on the occasion of his 70th birthday on August 24th, 2007.  相似文献   

14.
Thermal analysis has been used to investigate the crystallization of ZrxCe1-xO2 mixed oxides, prepared by co-precipitation of corresponding hydroxides. For x≤0.5, small crystals of CeO2, were formed at low temperatures (373 K). For x>0.5an exothermic peak at 420°C (693 K) was observed after calcination under a flow of air ofhydroxide samples. This peak was associated with the formation of a ZrxCe1-xO2 solid solution (XRD) in a tetragonal phase (Raman). The solids calcined at 700°C (973 K) present a reactivity towards the carbon black oxidation. The thermal analysis coupled with a gas chromatograph (GC) were used to follow this reactivity. Simultaneous study of the activity (thermal analysis) and the selectivity (GC) in CO or CO2 of the different catalysts revealed an important parameter: acatalyst-soot particle contact. We also obtained a more precise comparison of ZrxCe1-xO2 oxides in the catalytic soot combustion. This revised version was published online in August 2006 with corrections to the Cover Date.  相似文献   

15.
层状Li(Ni1-xCox)O2结构研究   总被引:5,自引:0,他引:5  
0引言层状钴酸锂是目前锂离子电池主要正极材料,但是,随着锂离子电池的广泛使用,急需比钴酸锂价格低和来源广泛的正极材料,层状锰酸锂和层状镍酸锂受到重视。由于锰氧化物存在有J-T效应,因此,严格意义上的层状锰酸锂的制备极其困难。制备层状镍酸锂也非常困难,高温反应极易生成Li1-xNi1 xO2,具有此种结构的镍酸锂存在严重首次能量衰减和循环性能下降的缺点。采用其他元素掺杂镍酸锂克服其缺点的研究已经很多,其中钴掺杂镍酸锂由于显示了良好的效果而被认为是最有希望替代钴酸锂的锂离子电池正极材料。有关层状镍钴酸锂的研究很多,但不少的…  相似文献   

16.
A series of spinel-type CoxNi1−xFe2O4 (x = 0, 0.2, 0.4, 0.5, 0.6, 0.8, 1.0) magnetic nanomaterials were solvothermally synthesized as enzyme mimics for the eletroctrocatalytic oxidation of H2O2. X-ray diffraction and scanning electron microscope were employed to characterize the composition, structure and morphology of the material. The electrochemical properties of spinel-type CoxNi1−xFe2O4 with different (Co/Ni) molar ratio toward H2O2 oxidation were investigated, and the results demonstrated that Co0.5Ni0.5Fe2O4 modified carbon paste electrode (Co0.5Ni0.5Fe2O4/CPE) possessed the best electrocatalytic activity for H2O2 oxidation. Under optimum conditions, the calibration curve for H2O2 determination on Co0.5Ni0.5Fe2O4/CPE was linear in a wide range of 1.0 × 10−8–1.0 × 10−3 M with low detection limit of 3.0 × 10−9 M (S/N = 3). The proposed Co0.5Ni0.5Fe2O4/CPE was also applied to the determination of H2O2 in commercial toothpastes with satisfactory results, indicating that CoxNi1−xFe2O4 is a promising hydrogen peroxidase mimics for the detection of H2O2.  相似文献   

17.
A series of NixCo1-xCo2O4(0 ≤ x ≤ 1) spinel catalysts were prepared by the co-precipitation method and used for direct N2O decomposition. The decomposition pathway of the parent precipitates was characterized by thermal analysis. The catalysts were calcined at 500 °C for 3 h and characterized by powder X-ray diffraction, Fourier transform infrared, and N2 adsorption-desorption. Nickel cobaltite spinel was formed in the solid state reaction between NiO and Co3O4. The N2O decomposition measurement revealed significant increase in the activity of Co3O4 spinel oxide catalyst with the partial replacement of Co2+ by Ni2+. The activity of this series of catalysts was controlled by the degree of Co2+ substitution by Ni2+, spinel crystallite size, catalyst surface area, presence of residual K+, and calcination temperature.  相似文献   

18.
The iron rich part of the system was examined in the temperature range of 1200-1380 °C in air, with focus on the solid solutions of M-type hexaferrites. Samples of suitable compositions were studied by electronprobe microanalysis (EPMA). Substituted Sr-hexaferrites in the system Sr-La-Co-Fe-O do not follow the 1:1 substitution mechanism of La/Co in M-type ferrites. Due to the presence and limited Co2+-incorporation Fe3+-ions are reduced to Fe2+ within the crystal lattice to obtain charge balance. In all examined M-type ferrites divalent iron is formed, even at 1200 °C. The substitution principle Sr2++Fe3+↔La3++(Fe2+, Co2+) yields to the general substitution formula for the M-type hexaferrite Sr2+1-xLa3+xFe2+x-yCo2+yFe3+12-xO19 (0≤x≤1 and 0≤yx). In addition Sr/La-perovskiteSS (SS=solid solution), Co/Fe-spinelSS, hematite and magnetite are formed. Sr-hexaferrite exhibits at 1200 °C a limited solid solution with small amounts of Fe2+ (SrFe12O19↔Sr0.3La0.7Co0.5Fe2+0.2Fe11.3O19). At 1300 and 1380 °C a continuous solid solution series of the M-type hexaferrite is stable. SrFe12O19 and LaCo0.4Fe2+0.6Fe11O19 are the end members at 1300 °C. The maximum Fe2+O content is about 13 mol% in the M-type ferrite at 1380 °C (LaCo0.1Fe2+0.9Fe11O19).  相似文献   

19.
The sol-gel combustion synthesis (SGCS) for oxygen carrier (OC) to be used in chemical looping combustion (CLC) was first designed and experimented in this work, which is a new method of OC synthesis by combining sol-gel technique and solution combustion synthesis. Cheap hydrated metal nitrates and urea were adopted as precursors to prepare Fe2O3/Al2O3 OC at the molar ratio to unity (Fe1Al1), which was characterized through various means, including Fourier transforms infrared (FTIR) spectroscopy, thermogravimetric analysis (TGA), differential thermal analysis (DTA), X-ray diffractor (XRD), and N2 isothermal adsorption/desorption method. FTIR analysis on the chemical structure of the dried gel of Fe1Al1 indicated that urea was partly hydrolyzed and the hydrated basic carbonate was formed by the combination of groups such as (Fe(1−yAly)1−xO1−3x, CO32− and -OH-. By analyzing the staged products during SGCS, calcination was found as a necessary step to produce Fe2O3/Al2O3 OC with separate phases of α-Fe2O3 and α-Al2O3. Through TGA-DTA, the decomposition of the dried gel was found to undergo five stages. The analysis of the evolved gases from the gel decomposition using FTIR partially confirmed the staged decomposition and assisted a better understanding of the mechanism of SGCS. XRD identification further substantiated the necessity of calcination to synthesize Fe2O3/Al2O3 OC with separate phases of α-Fe2O3 and α-Al2O3, though it was not necessary for the synthesis of single phase α-Fe2O3 and α-Al2O3. Structural characterization performed on N2 adsorption analyzer displayed that the pore shape of Fe1Al1 particles was heterogeneous. Finally, H2 temperature-programmed reduction (TPR) of Fe1Al1 products in TGA indicated that the reduction reaction of Fe1Al1 OC after calcination was a single step reaction from α-Fe2O3 to Fe, and calcination benefited to improve the transfer rate of the lattice oxygen from the OC to fuel H2. Furthermore, four times of reduction and oxidization (redox) reaction by alternating with H2 and air demonstrated the synthesized OC had good reactivity and sintering-resistance, much suitable to be used in the realistic CLC. Overall, the SGCS method was found superior to other existent methods to prepare Fe2O3/Al2O3 OC for CLC application.  相似文献   

20.
通过溶胶-凝胶法制备出不同Ni掺杂比例的双钙钛矿Sr_2Ni_xCo_(2-x)O_6(x=0.2,0.4,0.6,0.8),通过热分解法制备出具有层状结构的纳米颗粒g-C_3N_4,并制备其复合物催化剂。将双钙钛矿和g-C_3N_4分别制备成双功能电极片,用于测试其对氧还原(ORR)和氧析出(OER)的催化活性,然后选取具有最佳氧催化活性的Ni掺杂比例x=0.4的双钙钛矿与一定重量比例的g-C_3N_4进行复合,测试复合催化剂的氧催化活性。结果表明,复合后的催化剂催化效果明显优于单一催化剂,当g-C_3N_4添加量占双钙钛矿的30%(w/w)时复合催化剂催化氧还原反应的最大电流密度为395.7 mA·cm~(-2)(-0.6 V vs Hg/HgO),氧析出反应的最大电流密度为372.0mA·cm~(-2)(1 V vs Hg/HgO),这表明g-C_3N_4与Sr_2Ni_(0.4)Co_(1.6)O_6复合后协同催化能够提高双钙钛矿的氧催化活性。  相似文献   

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