Pt/CexZr1-xO2催化剂上丙烷完全氧化性能研究

采用沉淀法制备了ZrO2,CeO2和Ce0.7Zr0.3O2载体,并用浸渍法制备负载型Pt催化剂。考察了500和900℃焙烧催化剂的丙烷完全氧化性能和水汽对丙烷氧化反应的影响。对于500℃焙烧的催化剂,催化剂的丙烷氧化活性顺序为:Pt/ZrO2-500>Pt/CeO2-500>Pt/Ce0.7Zr0.3O2-500;而经900℃焙烧的催化剂活性顺序为:Pt/ZrO2-900>Pt/Ce0.7Zr0.3O2-900>Pt/CeO2-900。反应气氛中水汽的存在对两种Pt/ZrO2催化剂的活性均有抑制作用(T50温度均提高了10~15℃);而对于Pt/CeO2-500催化剂有抑制作用(T50温度提高10℃),但对Pt/CeO2-900催化剂活性有促进作用(T50温度下降25℃);对于两种Pt/Ce0.7Zr0.3O2催化剂活性具有促进作用(T50温度均下降5~25℃)。表征结果表明催化剂的活性与其表面Pt物种价态密切相关,催化剂表面上Pt0物种有利于活性的提高。Pt/Ce0.7Zr0.3O2-500催化剂中只含有氧化态Pt物种(Pt^2+),而Pt/Ce0.7Zr0.3O2-900催化剂中则含有部分金属态Pt物种,因此其活性高于Pt/Ce0.7Zr0.3O2-500催化剂。     

Co3O4/CeO2的氧化还原性能及反应条件对其CO氧化活性的影响

采用沉淀氧化法制备了Co₃O₄/CeO₂催化剂。运用XRD、BET和TPR表征手段,考察了不同钴铈比及焙烧温度对钴铈复合氧化物物理及化学性能的影响,并分别在干、湿条件下进行了一氧化碳氧化反应研究。结果表明,与纯的Co₃O₄相比,在不同比例的Co₃O₄/CeO₂均经723 K焙烧的各种催化剂中,钴铈原子比为9∶1的复合氧化物粒径较小,比表面积较大,说明适当比例铈的添加能使Co₃O₄具有较小的粒径。此氧化物经538 K温度焙烧制得的钴铈比为9∶1的复合氧化物中Co₃O₄平均粒径为7.2 nm, BET比表面积为167.6 m²/g。经TPR考察发现其具有最优的氧化还原性能。     

不同铈添加量对CeO2-ZrO2-Al2O3材料性能的影响

采用共沉淀法制备了一系列不同铈添加量的CeO2-ZrO2-Al2O3(CZA)储氧材料,并通过XRD、低温N2吸附-脱附、氧脉冲吸附(OSC)和H2-TPR等手段进行了表征。XRD结果表明,在1 000和1 100℃高温焙烧后,当CeO2添加量为8%时样品具有最好的结构稳定性能。N2吸附-脱附结果表明,CeO2添加量为8%时样品具有最好的织构性能,1 000℃时,比表面积和孔容分别为:136.6 m2.g-1和0.38 mL.g-1;1 100℃时,比表面积和孔容分别为:83.7 m2.g-1和0.23 mL.g-1。OSC结果显示,CeO2添加量为8%时样品具有最大的储氧量,1 000℃和1 100℃分别为70μmol.g-1和31μmol.g-1。H2-TPR结果表明,CeO2添加量为8%时样品具有最佳的还原性能。     

Pt-CeO2/SiO2催化剂用于室温湿空气中CO氧化反应

开发室温CO氧化催化剂的主要挑战是CO自中毒和慢的表面动力学,同时湿气的存在也可导致催化剂失活.本文开发了高活性CeO2促进的Pt基催化剂4%Pt-12%CeO2/SiO2,用于室温湿气(湿度10%?90%,25°C)中CO氧化反应,在低CO浓度(<500 ppm)和高CO浓度(>2500 ppm)时,CO转化率高于99%.优化了催化剂制备变量,如Pt和CeO2负载量、CeO2沉积方法、CeO2和Pt前驱体的干燥和焙烧条件.采用CO/H2化学吸附、O2-H2滴定、X射线衍射和BET比表面积测定表征了催化剂的表面特性,并将其与催化剂活性相关联.结果表明,CeO2沉积方法对催化剂活性影响显著,当用浸渍法沉积CeO2时,所得催化剂的反应速率(5.77μmol/g/s)比用沉积沉淀法(1.96μmol g?1 s?1)或CeO2嫁接法(1.31μmol g?1 s?1)制得催化剂的高3倍.O2-H2滴定结果表明,当用浸渍法沉积CeO2时,CeO2和Pt的紧密结合导致了催化剂的高活性.催化剂载体的选择也非常重要,硅胶负载的催化剂活性(5.77μmol g?1 s?1)是氧化铝负载的(1.05μmol g?1 s?1)5倍.当反应受内扩散控制时,催化剂载体的粒径和孔结构影响非常大.另外,CeO2和Pt前驱体的干燥和焙烧条件对催化剂活性的影响至关重要.当Pt和CeO2含量分别大于2.5和15 wt%时,所得催化剂在室温条件下活性高(TOF>0.02 s?1),稳定性好(反应15 h,CO转化率≥99%).     

贵金属原子在CeO2(111)表面吸附的密度泛函理论研究

利用密度泛函理论系统研究了贵金属原子(Au、Pd、Pt和Rh)在CeO₂(111)表面的吸附行为。结果表明,Au吸附在氧顶位最稳定,Pd、Pt倾向吸附于氧桥位,而Rh在洞位最稳定。当金属原子吸附在氧顶位时,吸附强度依次为Pt > Rh > Pd > Au。Pd、Pt与Rh吸附后在Ce 4f、O 2p电子峰间出现掺杂峰;Au未出现掺杂电子峰,其d电子峰与表面O 2p峰在-4～-1 eV重叠。态密度分析表明,Au吸附在氧顶位、Pd与Pt吸附在桥位、Rh吸附在洞位时,金属与CeO₂(111)表面氧原子作用较强,这与Bader电荷分析结果相一致。     

Enhanced reducibility of Ce1-xTixO2 compared to that of CeO2 and higher redox catalytic activity of Ce1-x-yTixPtyO2-delta compared to that of Ce1-xPtxO2-delta

Nanocrystalline Ce(1)(-)(x)Ti(x)O(2) (0 < or = x < or = 0.4) and Ce(1-)(x)(-)(y)Ti(x)Pt(y)O(2)(-)(delta) (x = 0.15, y = 0.01, 0.02) solid solutions crystallizing in fluorite structure have been prepared by a single step solution combustion method. Temperature programmed reduction and XPS study of Ce(1)(-)(x)Ti(x)O(2) (x = 0.0-04) show complete reduction of Ti(4+) to Ti(3+) and reduction of approximately 20% Ce(4+) to Ce(3+) state compared to 8% Ce(4+) to Ce(3+) in the case of pure CeO(2) below 675 degrees C. The substitution of Ti ions in CeO(2) enhances the reducibility of CeO(2). Ce(0.84)Ti(0.15)Pt(0.01)O(2)(-)(delta) crystallizes in fluorite structure and Pt is ionically substituted with 2+ and 4+ oxidation states. The H/Pt atomic ratio at 30 degrees C over Ce(0.84)Ti(0.15)Pt(0.01)O(2)(-)(delta) is 5 and that over Ce(0.99)Pt(0.01)O(2)(-)(delta) is 4 against just 0.078 for 8 nm Pt metal particles. Carbon monoxide and hydrocarbon oxidation activity are much higher over Ce(1-)(x)(-)(y)Ti(x)Pt(y)O(2) (x = 0.15, y = 0.01, 0.02) compared to Ce(1)(-)(x)Pt(x)O(2) (x = 0.01, 0.02). Synergistic involvement of Pt(2+)/Pt degrees and Ti(4+)/Ti(3+) redox couples in addition to Ce(4+)/Ce(3+) due to the overlap of Pt(5d), Ti(3d), and Ce(4f) bands near E(F) is shown to be responsible for improved redox property and higher catalytic activity.     

A new type of strong metal-support interaction and the production of H2 through the transformation of water on Pt/CeO2(111) and Pt/CeO(x)/TiO2(110) catalysts

The electronic properties of Pt nanoparticles deposited on CeO(2)(111) and CeO(x)/TiO(2)(110) model catalysts have been examined using valence photoemission experiments and density functional theory (DFT) calculations. The valence photoemission and DFT results point to a new type of "strong metal-support interaction" that produces large electronic perturbations for small Pt particles in contact with ceria and significantly enhances the ability of the admetal to dissociate the O-H bonds in water. When going from Pt(111) to Pt(8)/CeO(2)(111), the dissociation of water becomes a very exothermic process. The ceria-supported Pt(8) appears as a fluxional system that can change geometry and charge distribution to accommodate adsorbates better. In comparison with other water-gas shift (WGS) catalysts [Cu(111), Pt(111), Cu/CeO(2)(111), and Au/CeO(2)(111)], the Pt/CeO(2)(111) surface has the unique property that the admetal is able to dissociate water in an efficient way. Furthermore, for the codeposition of Pt and CeO(x) nanoparticles on TiO(2)(110), we have found a transfer of O from the ceria to Pt that opens new paths for the WGS process and makes the mixed-metal oxide an extremely active catalyst for the production of hydrogen.     

Preferential oxidation of CO in excess H2 over CeO2/CuO catalyst:Effect of calcination temperature

Different from the classical configuration CuO/CeO2 catalyst,the inverse configuration CeO2 /CuO catalyst (atomic ratio of Ce/Cu=10/100) was prepared by impregnation method.Five calcination temperatures were selected to investigate the interaction between CeO2 and CuO support.It is found that as calcination temperature increased from 500 to 900 C,sintering of CeO2 particles on the support occurred together with the diffusion of a portion of Ce 4+ ions into CuO crystals,forming solid solution.Formation of interface complex Ce-O-Cu was suggested by TPR measurements.The catalyst calcined at 700 C gives the highest activity for preferential oxidation of CO in excess H2 stream.     

Pt/Al2O3和Pt/CeO2/Al2O3催化甲烷部分氧化制合成气反应

研究了Pt/Al₂O₃和Pt/CeO₂/Al₂O₃对甲烷部分氧化制合成气反应的催化活性,发现Pt/CeO₂/Al₂O₃显示了更高的甲烷转化率和合成气选择性.用H₂-TPR、H₂-TPD、SEM-EDX和XRD等技术对催化剂进行了表征.CeO₂和Pt相互作用促进Pt在催化剂表面的分散,抑制Pt在催化剂表面的迁移;降低了催化剂的燃烧活性,提高了催化剂的部分氧化活性和选择性,可避免因催化剂床层局部温度过高而导致催化剂活性下降或失活,提高了催化剂的稳定性.同时,CeO₂通过促进水汽变换反应使反应体系迅速达到平衡,提高了催化剂对H₂的选择性.     

硫酸溶液中Ce3+在铂电极上阳极氧化动力学

用分解极化曲线法研究了铂电极上Ce（Ⅳ）阳极形成动力学与机理．实验结果表明，电位在1．7—1．9V（vs．SCE）的高极化区，分解得到的O2和Ce（Ⅳ）的极化曲线Tafel斜率分别为2．303RT／βF和2×2．303RT／βF，两者的动力学方程可分别用下式表示：
i(O2)=k1aw4exp(βφF/RT)
i(Ce4+)=k2aw2[Ce3+]exp(βφF/2RT)
假设了Ce3＋是通过反应中间基MCe（OH）3•Oad氧化的机理．由此所导出的动力学方程与实验结果相符．     

Pt/CeO2/CNTs催化剂对甲醇电催化氧化的研究

通过微波乙二醇法制备了Pt/CeO2/CNTs催化剂用于碱性体系中的甲醇电催化氧化,考察了不同的CeO2含量对其电催化活性的影响.X射线衍射(XRD)和透射电镜(TEM)结果表明,Pt/CeO2/CNTs催化剂中Pt颗粒较小,在载体上分散性较好.循环伏安曲线和计时电流测试结果表明,Pt/CeO2/CNTs催化剂表现出良...     

Dissolution Extraction of Uranium Oxides and Cerium Oxide with TBP-HNO3 Complex in Supercritical CO2

Dissolution extraction of uranium oxides, CeO2 and (U, Ce)O2 solid solution with TBP-HNO3 complex in supercritical CO2 (SC-CO2) was investigated. It is difficult to dissolve and extract directly UO2 pellets and CeO2 with TBP-HNO3 complex in SC-CO2. After UO2 pellets spontaneously turns into U3O8 powders under O2 flow and 600 °C, the extraction efficiency can reach more than 98%. For dissolution extraction of (U, Ce)O2 solid solution with TBP-HNO3 complex in SC-CO2 under 60 and 20 MPa, the extraction efficiency of U and Ce is 98.61% and 98.1% respectively.     

Kinetics of oxygen exchange over CeO2-ZrO2 fluorite-based catalysts

The kinetics of 18O/16O isotopic exchange over CeO2-ZrO2-La2O3 and Pt/CeO2-ZrO2 catalysts have been investigated under the conditions of dynamic adsorption-desorption equilibrium at atmospheric pressure and a temperature range of 650-850 degrees C. The rates of oxygen adsorption-desorption on Pt sites, support surface, oxygen transfer (spillover) from Pt to the support as well as the amount of oxygen accumulated in the oxide bulk, and oxygen diffusion coefficient were estimated. The nanocrystalline structure of lanthana-doped ceria-zirconia prepared via the Pechini route with a developed network of domain boundaries and specific defects guarantees a high oxygen mobility in the oxide bulk (D = (1.5 / 2.0).10-18 m2 s-1 at 650 degrees C) and allows accumulation of over-stoichiometric/excess oxygen. For Pt/CeO2-ZrO2, oxygen transfer from Pt to support (characteristic time < 10-2 s) was shown to be responsible for the fast exchange between the gas-phase oxygen and oxygen adsorbed on the mixed oxide surface. The rate of direct exchange between the gas phase and surface oxygen is increased as well due to the increased concentration (up to 2 monolayers) of surface/near subsurface oxygen species accumulated on the oxygen vacancies (originated from the incorporation of highly dispersed Pt atoms). The characteristic time of diffusion of the oxygen localized in the subsurface layers is about 1 s. The overall quantity of over-stoichiometric oxygen and/or hydroxyl groups accumulated in the bulk can reach the equivalent of 10 monolayers, and characteristic time of oxygen diffusion within the bulk is about 20 s. All these kinetic data are required for the further step of modeling partial oxidation of hydrocarbons under steady- and unsteady-state conditions.     

氧化铈稳定的CuO簇在CO,C3H6和NO消除中的催化性能（英文）

研究了CuO与γ-Al2O3和CeO2的相互作用,并由此制备出能有效脱除CO,C3H6和NO的催化剂,考察了不同载体表面CuO簇的分散稳定性和耐老化性能.结果发现,随CuO负载量的增加,CuO簇因与CeO2载体的强相互作用而稳定存在;而在γ-Al2O3表面,CuO簇易聚集成较大的颗粒.另一方面,由于CeO2本身较差的热稳定性,表面分散的CuO在950oC高温处理后烧结.因此,基于γ-Al2O3载体优越的耐老化性能,在γ-Al2O3载体分散CeO2,然后再担载CuO,从而得到了稳定的CuO簇,所得催化剂比CuO/γ-A12O3和CuO/CeO2具有更好的催化性能和抗热老化性能.     

Effects of deposited Pt particles on the reducibility of CeO2(111)

The interaction of Pt particles with the regular CeO(2)(111) surface has been studied using Pt(8) clusters as representative examples. The atomic and electronic structure of the resulting model systems have been obtained through periodic spin-polarized density functional calculations using the PW91 exchange-correlation potential corrected with the inclusion of a Hubbard U parameter. The focus is on the effect of the metal-support interaction on the surface reducibility of ceria. Several initial geometries and orientations of Pt(8) with respect to the ceria substrate have been explored. It has been found that deposition of Pt(8) over the ceria surface results in spontaneous oxidation of the supported particle with a concomitant reduction of up to two Ce(4+) cations to Ce(3+). Oxygen vacancy formation on the CeO(2)(111) surface and oxygen spillover to the adsorbed particle have also been considered. The presence of the supported Pt(8) particles has a rather small effect (～0.2 eV) on the O vacancy formation energy. However, it is predicted that the spillover of atomic oxygen from the substrate to the metal particle greatly facilitates the formation of oxygen vacancies: the calculated energy required to transfer an oxygen atom from the CeO(2)(111) surface to the supported Pt(8) particle is only 1.00 eV, i.e. considerably smaller than 2.25 eV necessary to form an oxygen vacancy on the bare regular ceria surface. This strongly suggests that the propensity of ceria systems to store and release oxygen is directly affected by the presence of supported Pt particles.     

负载型铈基催化剂在NH3-SCR反应中的载体效应

近年来,氨-选择催化还原(NH3-SCR)技术被公认为是控制燃煤烟气和柴油车尾气氮氧化物(NOx)排放的最有效手段之一.V2O5-WO3/TiO2和V2O5-MoO3/TiO2催化剂在300–400°C范围内表现出优异的脱硝性能和抗H2O和SO2中毒性能,因而被广泛用于NH3-SCR过程.然而,钒基催化剂存在一些缺点,如氧化SO2到SO3的活性较高、高温下将部分NH3非选择性地氧化成N2O、V2O5具有生物毒性等.因此,非钒基脱硝催化剂的研制引起人们越来越多的关注.二氧化铈(CeO2)因具有氧化还原性能优异、储/释氧能力强和Ce3+/Ce4+转换容易等优点而广泛用于NH3-SCR反应.然而,单纯CeO2的脱硝性能并不理想.研究表明,将CeO2制备成铈基复合金属氧化物催化剂和负载型铈基催化剂可显著提高其在NH3-SCR反应中的催化性能.尤其是负载型铈基催化剂由于催化性能优异、比表面积大、热稳定性高及活性组分用量少而成为研究热点.众所周知,对于负载型金属氧化物催化剂,载体并不只是惰性材料,它会显著影响表面负载组分的物理化学性质和催化性能.因此,关于载体与组分间相互作用的研究常见诸报道.但是,对于负载型铈基催化剂,具有不同晶相结构的载体对其理化性质和NH3-SCR催化性能的影响规律尚不明晰.此外,SiO2,γ-Al2O3,ZrO2和TiO2是工业上常用的四种催化剂载体,它们具有不同的晶相结构和应用场合,究竟哪一个最适合作为负载型铈基催化剂的载体用于NH3-SCR反应尚无定论.因此,为了阐明负载型铈基催化剂在NH3-SCR反应中的载体效应,筛选出最佳的催化剂载体,我们首先采用溶胶-凝胶法和沉淀法合成了SiO2,γ-Al2O3,ZrO2和TiO2四个载体,再通过浸渍法制备了一系列负载型铈基催化剂(CeO2/SiO2,CeO2/γ-Al2O3,CeO2/ZrO2和CeO2/TiO2)用于NH3-SCR反应.并借助于X射线衍射(XRD)、拉曼光谱(Raman)、比表面积测定(BET)、X射线光电子能谱(XPS)、氢气-程序升温还原(H2-TPR)以及氨气-程序升温脱附(NH3-TPD)等表征手段对上述载体和催化剂进行了较为全面的分析.研究结果表明,这些负载型铈基催化剂的理化性质和脱硝性能强烈地依赖于催化剂载体.首先,CeO2/γ-Al2O3催化剂的表面Ce3+含量明显大于CeO2/SiO2,CeO2/ZrO2和CeO2/TiO2催化剂,有利于氧空位的产生以促进NO分子的解离,进而导致优异的NH3-SCR反应性能.其次,CeO2/γ-Al2O3催化剂具有最佳的还原性能,有利于NO氧化为NO2,进而通过"快速NH3-SCR"途径提升其催化性能.再者,CeO2/γ-Al2O3催化剂表面酸性位最多,能够促进反应物NH3分子的吸附与活化,从而提高脱硝性能.最后,CeO2/γ-Al2O3催化剂在H2O和SO2存在的条件下同样表现出最佳的催化性能,表明其有望用于实际燃煤烟气脱硝.     

Pt/CeO2-ZrO2变换催化剂的制备、表征与性能

 用共沉淀法制备了不同Ce/Zr比的CeO2-ZrO2复合氧化物,用浸渍法制备了Pt/CeO2-ZrO2水煤气变换催化剂,并对该催化剂进行了活性评价. 结果表明,与传统的Cu基低变催化剂相比,该催化剂具有操作温度范围宽和抗氧化冲击等优点,具有应用于车载重整制氢过程的潜力. 考察了温度、空速和汽/气比等条件对催化剂活性的影响,对催化剂的制备参数和工艺参数进行了研究. 结果表明,不同Ce/Zr比的Pt/CeO2-ZrO2催化剂的活性相差很大,其中Pt/Ce0.8Zr0.2O2变换催化剂活性最高. XRD结果表明,制备的Pt/Ce0.8Zr0.2O2形成了固溶体. 通过增加单位质量催化剂表面的Pt原子数可提高催化剂的活性.     

超声波振动在Ce-Zr-La/Al2O3及负载型Pd三效催化剂制备中的应用

制备了CeO2-ZrO2-La2O3/Al2O3材料, 在制备过程中使用超声波振动对材料进行处理, 并以此材料为载体制备了单Pd三效催化剂. 对所制备的载体进行了织构性能分析(BET)和X射线衍射(XRD)表征. 对催化剂进行了NO程序升温脱附(NO-TPD)及H2程序升温还原(H2-TPR)表征, 并对催化剂进行了活性测试. BET结果表明, 900 ℃焙烧后, 超声波振动处理的载体比表面积为130 m2·g-1, 而没有进行处理的载体比表面积为117 m2·g-1. 超声波处理的CeO2-ZrO2-La2O3/Al2O3材料介孔直径为11.4 nm, 相对较大, 载体更加稳定. XRD测试结果表明, 超声波处理的载体在1150 ℃焙烧5 h后仍然只有Ce0.5Zr0.5O2一个单一物相, 而未经过超声波处理的载体此时出现相分离, 体相中有θ-Al2O3出现. 以超声波处理材料为载体的Pd催化剂新鲜和老化后NO-TPD测试结果变化很小. H2-TPR测试中, 超声波振动处理的材料制备的催化剂中活性组分和载体的还原峰温较未超声处理材料制备的催化剂稍高, 而峰面积远大于未超声处理材料制备的催化剂. 活性测试结果说明, 由超声波振动处理过的载体制备的三效催化剂对汽车尾气中的三种污染物的起燃温度更低, 有更好的活性以及温度特性.     

Determination of O and OH adsorption sites and coverage in situ on Pt electrodes from Pt L(2,3) X-ray absorption spectroscopy

The adsorption of atomic oxygen and hydroxide on a platinum electrode in 0.1 M HClO4 or H2SO4 electrolytes was studied in situ with Pt L(2,3) X-ray absorption spectroscopy (EXAFS and XANES). The Pt L3 edge absorption data, mu, were collected at room temperature in transmission mode on beamline X-11A at the National Synchrotron Light Source using a custom built cell. The Pt electrode was formed of highly dispersed 1.5-3 nm particles supported on carbon. A novel difference procedure (delta mu = mu(O[H]/Pt) - mu(Pt)) utilizing the L3 XANES spectra at different applied voltages was used to isolate the effects of O[H] (O or OH) adsorption in the XANES spectra. The Deltamu results are compared with results obtained from real-space full-multiple scattering calculations utilizing the FEFF8 code on model clusters. The experimental results, when compared with theoretical calculations, allow the adsorption site to be identified. At low coverages OH adsorbs primarily in 1-fold coordinated atop sites. As the coverage increases, O binds in the bridge/fcc sites, and at still higher coverages above 1.05 V RHE, O adsorbs into a higher coordinated n-fold or subsurface site, which is thought to be the result of Pt-O site exchange and oxide formation. These results are similar to those found in the gas phase. Direct specific adsorption of bisulfate anions in H2SO4 is spectroscopically seen in both the EXAFS and XANES data and is seen to impede oxygen adsorption consistent with previous reports.     

TiN_(0.3)/CeO_2光阳极材料的构筑及其光电催化性能(英文)

采用高温氮化法在Ti片基底上生长一层TiN0.3薄膜,进一步利用电化学沉积法在TiN0.3薄膜上生长CeO2,制备了TiN0.3/CeO2复合材料.分别用X射线衍射和扫描电镜研究了复合材料的晶体和形貌结构,用紫外-可见光谱探究了材料的光学吸收性能.结果表明,球状CeO2颗粒均匀地分布在TiN0.3表面;该复合光阳极除了TiN0.3对可见光的吸收外,外层的CeO2同时实现了对紫外光的吸收.光电催化性能研究发现,TiN0.3/CeO2复合光阳极能够显著提高TiN0.3或CeO2的光电流密度,同时增加光电流的稳定性.TiN0.3/CeO2独特的双层结构是其光电催化性能提高的主要原因.在TiN0.3与CeO2界面处异质结构的驱动下,CeO2层中的光生电子迁移至TiN0.3层,而相应的光生空穴在界面处被Ce3+所消耗,从而提高了CeO 2层中电子和空穴的分离效率,光电流密度也随之提高;同时,位于CeO2与电解液界面处的Ce3+作为水分子的吸附中心和反应活性中心,加快了界面处水的氧化反应,从而进一步促进了稳定光电流的产生.鉴于TiN0.3/CeO2光阳极材料优良的光电催化性能,其在太阳能光电催化领域具有潜在的应用,对于新型高效光电转化材料的设计与合成具有借鉴作用.