The first facile stereoselectivity switch in the polymerization of rac-lactide--from heteroselective to isoselective dialkylgallium alkoxides with the help of N-heterocyclic carbenes

The reaction of N-heterocyclic carbene (NHC) with dimeric dialkylgallium alkoxides, acting as nonselective or heteroselective catalysts in the polymerization of rac-LA, leads to highly active and isoselective monomeric Me(2)Ga(NHC)OR catalysts, resulting for the first time in the facile switch of stereoselectivity.     

Towards the object-oriented design of active hydrogen evolution catalysts on single-atom alloys

Given a desired property, locating relevant materials is always highly desired but very challenging in a range of areas, including heterogeneous catalysis. Obviously, object-oriented design/screening is an ideal solution to this problem. Herein, we develop an inverse catalyst design workflow in Python (CATIDPy) that utilizes a genetic-algorithm-based global optimization method to guide on-the-fly density functional theory calculations, successfully realizing the highly accelerated location of active single-atom alloy (SAA) catalysts for the hydrogen evolution reaction (HER). 70 binary and 752 ternary SAA candidate catalysts are identified for the HER. Furthermore, via considering the segregation stability and cost of materials, we extracted 6 binary and 142 ternary SAA candidate catalysts that are recommended for experimental synthesis. Remarkably, guided by these theoretical identifications, homogeneously dispersed Ni-based bimetallic catalysts (e.g., NiMo, NiAl, Ni₃Al, NiGa, and NiIn) were synthesized experimentally to test the reliability of the CATIDPy workflow, and they showed superior HER performance to bare Ni foam, indicating huge potential for use in real-world water electrolysis techniques. Perhaps more importantly, these results demonstrate the capacity of such a proposed approach for investigating unexplored chemical spaces to efficiently design promising catalysts without knowledge from the expert domain, which has far-reaching implications.

An inverse catalyst design workflow in Python (CATIDPy) for discovering unexplored chemical spaces successfully realized the highly accelerated location of active single-atom alloy (SAA) catalysts for the hydrogen evolution reaction (HER).     

Transforming nonselective into chemoselective metal catalysts for the hydrogenation of substituted nitroaromatics

It is generally accepted that good hydrogenation noble and nonnoble metal catalysts such as Pt, Ru, or Ni are not chemoselective for hydrogenation of nitro groups in substituted aromatic molecules. We have found that it is possible to transform nonchemoselective into highly chemoselective metal catalysts by controlling the coordination of metal surface atoms while introducing a cooperative effect between the metal and a properly selected support. Thus, highly chemoselective and general hydrogenation Pt, Ru, and Ni catalysts can be prepared by generating nanosized crystals of the metals on the surface of a TiO 2 support and decorating the exposed (111) and (100) crystal faces by means of a simple catalyst activation procedure. By doing this, it has been possible to change the relative rate for hydrogenating competitive groups present in the molecule by almost 2 orders of magnitude, increasing the chemoselectivity from less than 1% to more than 95%.     

高分散隔离活性位催化剂中过渡金属离子结构对丙烷选择氧化反应性能的影响

考察了碱金属K修饰的SiO2负载极低含量过渡金属的高分散隔离活性位系列催化剂(K-M/SiO2(n(K)∶n(M)∶n(Si)=10∶1∶1000),M=V,Cr,Mn,Fe,Co,Ni,Cu,Zn)的丙烷选择氧化催化性能,并运用UV-Raman和CO2-TPD等方法,对该系列催化剂进行了结构和物化性能表征,探讨了催化剂的表面离子结构与催化反应性能之间的关系。 发现钾修饰的SiO2负载过渡金属高分散隔离活性位催化剂上过渡金属离子的组态结构,对丙烷选择氧化反应性能有重要影响。相对稳定的全充满或无d电子的表面离子结构有利于选择氧化反应进行,而存在多种价态的相对不稳定的离子结构有利于深度氧化的进行。 这一离子结构与丙烷选择氧化催化性能的关系与前期乙烷选择氧化规律相似,进一步说明在高分散隔离活性位催化剂中,过渡金属离子的电子组态结构是影响低碳烷烃选择氧化反应性能的最重要因素。     

过渡金属原子对掺杂g-CN单层作为高效氮电催化剂性能

由于氨是药物、肥料和树脂等领域的基础,氨合成一直广受关注.工业中主要通过Haber-Bosch反应制备氨,反应需要在高温高压下进行.因此,探索其它氨合成技术对减轻能源消耗和缓解温室效应具有重大意义.在溶液条件下,采用水作为氢质子源,电化学还原氮合成氨方法受到了极大关注.然而,大多数电催化剂难以活化氮气分子且电催化氮气还...     

限域纳米空间制备高效HCl氧化CuO-CeO_2催化剂

利用KIT-6的有序介孔作为限域空间制备了一系列的介孔Cu O-Ce O2催化剂.借助XRD、BET、Raman、ESEM、TEM和H2-TPR等手段对催化剂进行表征,并考察其在HCl氧化反应中的催化性能.结果表明:铜含量35%时,Cu O物种高度分散在催化剂的表面或者进入Ce O2晶格,催化剂具有高比表面积(140 m2·g-1)和较小的晶粒尺寸,其中25Cu O-Ce O2催化剂具备最高的表面氧空位浓度和最优的低温氧化还原性能,并在HCl氧化反应中表现出最佳的催化活性,O2/HCl=6,370℃时转化率达到90%.反应动力学结果表明,25Cu O-Ce O2中更多的高分散的Cu O促进了HCl在催化剂表面的吸附和活化,更高浓度的氧空位增强了氧分子的吸附和活化.     

Highly active iridium/iridium-tin/tin oxide heterogeneous nanoparticles as alternative electrocatalysts for the ethanol oxidation reaction

Ethanol is a promising fuel for low-temperature direct fuel cell reactions due to its low toxicity, ease of storage and transportation, high-energy density, and availability from biomass. However, the implementation of ethanol fuel cell technology has been hindered by the lack of low-cost, highly active anode catalysts. In this paper, we have studied Iridium (Ir)-based binary catalysts as low-cost alternative electrocatalysts replacing platinum (Pt)-based catalysts for the direct ethanol fuel cell (DEFC) reaction. We report the synthesis of carbon supported Ir(71)Sn(29) catalysts with an average diameter of 2.7 ± 0.6 nm through a "surfactant-free" wet chemistry approach. The complementary characterization techniques, including aberration-corrected scanning transmission electron microscopy equipped with electron energy loss spectroscopy, X-ray diffraction, X-ray photoelectron spectroscopy, and X-ray absorption spectroscopy, are used to identify the "real" heterogeneous structure of Ir(71)Sn(29)/C particles as Ir/Ir-Sn/SnO(2), which consists of an Ir-rich core and an Ir-Sn alloy shell with SnO(2) present on the surface. The Ir(71)Sn(29)/C heterogeneous catalyst exhibited high electrochemical activity toward the ethanol oxidation reaction compared to the commercial Pt/C (ETEK), PtRu/C (Johnson Matthey) as well as PtSn/C catalysts. Electrochemical measurements and density functional theory calculations demonstrate that the superior electro-activity is directly related to the high degree of Ir-Sn alloy formation as well as the existence of nonalloyed SnO(2) on surface. Our cross-disciplinary work, from novel "surfactant-free" synthesis of Ir-Sn catalysts, theoretical simulations, and catalytic measurements to the characterizations of "real" heterogeneous nanostructures, will not only highlight the intriguing structure-property correlations in nanosized catalysts but also have a transformative impact on the commercialization of DEFC technology by replacing Pt with low-cost, highly active Ir-based catalysts.     

nV-MCM-41 催化剂的制备及其催化 CO2氧化丙烷脱氢反应性能

丙烯是一种重要的化工原料, 其下游产品丰富, 用途广泛, 主要用于生产聚丙烯、丙烯腈、丙烯酸和丁醇等化工产品.丙烯的需求正在不断增长, 而传统的丙烯生产方法如蒸汽裂解和石油催化裂化, 存在反应温度高、积碳严重且丙烯收率较低等问题. 因此研制丙烷脱氢制取丙烯的高效催化剂尤为重要. 研究发现, 以 CO2作为温和氧化剂进行逆水气变换反应可有效促进丙烷脱氢. 催化剂主要由活性组分与载体构成, 本文选择可用于活化丙烷的钒作为主要活性组分. 钒氧化物在载体上的高度分散是提高丙烷脱氢反应活性的关键. MCM-41 拥有较大的比表面积和高度有序的介孔结构, 可更有效地分散活性位点. 本文采用一步法合成了不同钒含量的 nV-MCM-41 催化剂 (1.9-10.6 wt%), 并研究了其在以下条件下催化丙烷氧化脱氢制丙烯反应性能: 600 °C, 催化剂质量 0.2 g, 进料气体组成 C3H8/CO2/Ar (摩尔比) = 1/4/4, 进料气体总流量 15 mL/min. 其中 6.8V-MCM-41 催化剂具有最高的活性, 其初始丙烷转化率达 58%, 丙烯选择性达 92%, 远高于相似反应条件下早期研究的 nV-SBA-15 催化剂. 并在四次反应-再生循环中始终保持其原来的高反应活性. 本文借助于 N2吸附-脱附、拉曼光谱 (Raman)、X 射线光电子能谱 (XPS)和热重 (TG) 等手段探究了不同钒含量的 nV-MCM-41 催化剂在丙烷脱氢反应中催化性能差异的原因.氮气吸附-脱附结果表明, 所有催化剂都存在典型的高度有序的介孔结构, 并没有因为钒组分的掺杂而破坏. nV-MCM-41催化剂拥有较大比表面积,并随钒掺杂量的增加而减小. 其中,10.8V-MCM-41催化剂的比表面积急剧下降,可能是由于产生了结晶的 V2O5阻塞了孔道. Raman 结果表明, 当钒负载量超过 6.8 wt% 时, 出现了 V2O5的结晶峰. 另外根据单分散的四面体钒氧化物的特征峰面积发现, 6.8V-MCM-41 催化剂中钒物种分散度最高, 与其具有最高催化活性结果一致. XPS 结果也进一步证明 6.8V-MCM-41 钒物种的分散度最高. 在连续反应过程中 6.8V-MCM-41 催化剂失活较快,可归结于活性钒位点的还原与催化剂表面的积碳. 通过氧化再生, 可恢复催化剂活性, 并且在 4 次再生循环中始终保持其良好稳定的活性.     

Study on the Catalyst for Catalytic Air Wet Oxidation on Highly Organic Wastewater

The industrial effluents are as varied as the industries themselves, in terms of nature of contaminants, their concentration treatment, and disposal methods required. For the highly organic wastewater, the technique of wet air oxidation (WAO) is more available. Currently more than 200 full scale WAO plants are in operation for the treatment of a wide variety of effluent streams. In the recent years, the use of homogeneous and heterogeneous catalysts has received a great attention. The homogeneous catalysts are in general more effective oxidation catalysts for increasing the rates of oxidation. But it is necessary to make precipitation step to recover/remove the toxic catalyst from the final effluent In view of this, heterogeneous catalyst systems are preferable. So we investigated on the way of preparation of copper oxide on a spinel support of Al₂O₃) and its effects on the catalytic wet air oxidation (CWAO) on highly organic wastewater.     

金属载体强相互作用增强Au/TiO2催化剂在3-硝基苯乙烯选择性加氢反应的活性

自Haruta与Hutchings于上世纪八十年代末发现金纳米催化剂优异的反应活性以来,科研人员对金催化的应用领域进行了广泛而深入地研究.对金催化科学和应用领域的研究一直在进行.大量的研究表明,金催化剂在各种选择性氧化反应中具有优异的催化性能(高活性和高选择性).然而,在催化加氢反应中,尽管金催化剂相比于铂族金属显示出优越的选择性,但是由于金催化剂选择性加氢反应的活性较差,使其在选择性催化加氢反应中的应用受到了极大的限制.研究表明,金催化剂较弱的活化氢气能力是其催化加氢反应活性低的主要原因.研究发现,氢气活化的活性中心可能是界面、负价金、低配位的金原子等.金催化剂具有明显的载体效应,金属-载体之间的相互作用能够显著地改变金催化剂的催化性能.Tauster等研究发现,铂族金属与还原性载体之间存在强相互作用,能够引发载体包覆金属表面,并且使得电子从载体向金属迁移,导致金属带负电.受金属-载体强相互作用(SMSI)效应的启发,本文探究了Au/TiO2催化剂中SMSI对金催化剂加氢性能的影响.在H2或O2气氛下高温焙烧Au/TiO2,获得一系列金催化剂(Au/TiO2-TA,T为焙烧温度(oC):300、400、500和600;A为气氛:H2或O2).对比在3-硝基苯乙烯(3-NS)选择性加氢反应中的活性发现,Au/TiO2-500H的TOF值是Au/TiO2-500O的3.3倍;动力学测试表明,Au/TiO2-500H和Au/TiO2-500O的反应表观活化能分别为79.5和105.1 kJ/mol.这表明两类催化剂催化活性中心的结构存在差异.X射线光电子能谱测试结果表明,Au/TiO2-H样品中Au带部分负电,而Au/TiO2-O中Au显示为金属态.HAADF-STEM和EELS显示,Au/TiO2-H中Au NPs的表面有TiOx物种,增加了Au-TiO2的界面.EPR结果表明,Au/TiO2-H中存在表面Ti3+物种,而Au/TiO2-O样品中则没有.为确认加氢反应的活性中心到底是界面还是负价金物种,本文探究了不同温度下氢气处理的Au/TiO2的结构与性能的关系,发现Au/TiO2-300H/400H/500H催化剂都显示出较好的催化3-NS加氢活性,而Au/TiO2-600H虽然具有更多的负价金物种,但是3-NS选择性加氢反应的活性反而降低,因此,负价金不是活性中心.这是因为不同温度处理的Au/TiO2-H样品中,SMSI的强弱不同,在300、400、500 oC下,SMSI能够增加Au-TiO2的界面长度,从而增强了3-NS加氢反应的活性;而温度达到600 oC,SMSI效应太强,Au NPs被包覆更密实,导致Au/TiO2-600H的3-NS选择性加氢反应的活性下降.密度泛函理论计算表明,Au/TiO2-H样品具有更低的H2解离活化能以及氢转移活化能.氢氘交换反应也进一步验证了SMSI有利于H2的活化.     

高度隔离过渡金属催化剂及其烯烃环氧化研究

 介绍了过渡金属杂原子分子筛的骨架杂原子表征、用离子注入法和化学嫁接法制备高度隔离过渡金属催化剂及其催化烯烃环氧化研究的结果．基于共振拉曼原理,用紫外共振拉曼光谱明确鉴别了TS－1,Fe－ZSM－5和V－MCM－41等分子筛中的骨架杂原子．用离子注入法和化学嫁接法制得具有高度隔离过渡金属离子的非杂原子分子筛催化剂．烯烃环氧化反应结果表明,所制得的催化剂显示出优良的催化性能．     

Current advances in heterogeneous catalysts for the synthesis of cyclic carbonates from carbon dioxide

The novel heterogeneous catalysts are highly demanded to perform the cycloaddition reaction of carbon dioxide with epoxide to synthesize the cyclic carbonates. The heterogeneous catalysts are more preferred than homogeneous catalysts due to the easy post reaction separation, easy to recycle, high stability and cost effective nature. In this review, we have summarized the current research progress in heterogeneous catalysis for the cycloaddition of carbon dioxide (CO₂) to synthesis of cyclic carbonates. Recent advances in the design of the heterogeneous catalysts and the understanding to the role of catalysts in reaction process are summarized and discussed.     

Promotional Effect of Bismuth as Dopant in Bi-Doped Vanadyl Pyrophosphate Catalysts for Selective Oxidation of n-Butane to Maleic Anhydride

Bismuth-promoted (1% and 3%) vanadyl pyrophosphate catalysts were prepared by refluxing Bi(NO3)3·5H2O and VOPO4·2H2O in isobutanol. The incorporation of Bi into the catalysts lattice increased the surface area and lowered the overall V oxidation state. Profiles of temperature programmed reduction (TPR) in H2 show a significant shift of the maxima of major reduction peaks to lower temperatures for the Bi-promoted catalysts. A new peak was also observed at the low temperature region for the catalyst with 3% of Bi dopant. The addition of Bi also increased the total amount of oxygen removed from the catalysts. The reduction pattern and reactivity information provide fundamental insight into the catalytic properties of the catalysts. Bi-promoted catalysts were found to be highly active (71% and 81% conversion for 1% and 3% Bi promoted catalysts, respectively, at 703 K), as compared to the unpromoted material (47% conversion). The higher activity of the Bi-promoted catalysts is due to that these catalysts possess highly active and labile lattice oxygen. The better catalytic performance can also be attributed to the larger surface area.     

MgCl2/R'nAl(OR)3-n: an excellent activator/support for transition-metal complexes for olefin polymerization

A new and effective method for the activation, and simultaneously, immobilization of bis(phenoxyimine) early-transition-metal complexes for olefin polymerization (known as FI catalysts), which makes use of MgCl(2)/R'(n)Al(OR)(3-n) as an activator/support, has been developed. Ti-, Zr-, and V-FI catalysts combined with this MgCl(2)-based compound can form highly active MgCl(2)-supported single-site catalysts capable of demonstrating superior catalytic properties, compared to the corresponding homogeneous methylaluminoxane- (Ti- and Zr-FI catalysts) or alkylaluminum-activation systems (V-FI catalysts), in terms of their catalytic activity, molecular weight, stereoselectivity, and comonomer incorporation. Additionally, these new catalysts can produce polymers of significant morphology with high efficiency. Notably, the MgCl(2)-based compounds can also effectively activate and immobilize the early-to-late transition-metal complexes that have emerged recently. Thus, the application of MgCl(2)-based compounds as activators/supports for transition-metal complexes for olefin polymerization provides a conceptually new strategy for the development of methylaluminoxane- and borate-free, high-performance, single-site catalysts capable of controlling polymer morphology.     

用于NH3选择性催化还原NOx的钒基催化剂

在富氧且有催化剂存在条件下以NH3或尿素为还原剂选择性地还原NOx为N2的技术,即NH3/Urea-SCR技术,是去除固定源和移动源NOx最为有效且应用最广的技术之一,其中最重要的催化剂体系是钒基催化剂。本文从钒基催化剂的组成及其NH3-SCR反应性能、钒基催化剂的活性改进以及钒基催化剂上的NH3-SCR反应机理三个方面对该领域的研究进展做了较为全面的综述,并对NH3-SCR领域可能的发展方向做了展望。传统的V2O5-WO3(MoO3)/TiO2催化剂以及改性后的钒基催化剂在中温段具有优异的NOx净化效率和抗SO2中毒性能,其中高分散的V5+物种以及多聚的钒酸盐物种为NH3-SCR反应的活性中心。针对采用不同方法制备的或具有不同组成的钒基催化剂体系,多数学者认为NH3-SCR反应按照Eley-Rideal(E-R)机理进行,部分学者认为按照Langmuir-Hinshelwood(L-H)机理进行,这可能与催化剂的钒负载量以及反应温度区间相关。在后续工作中研究者应结合多种测试手段,具体问题具体分析,综合考虑温度的动态影响以及表面酸碱性对反应物的吸附活化,以得出更为全面、真实的反应机理。系统了解前人在钒基NH3-SCR催化剂领域的研究进展有助于现阶段开发高效稳定、可适应复杂工作条件的钒基SCR催化转化器,同时也对设计合成新型高效、环境友好且抗中毒的非钒基SCR催化剂体系具有一定的参考价值。     

Preparation of highly active silica-supported Au catalysts for CO oxidation by a solution-based technique

Although Au catalysts can be readily prepared on titania via the deposition-precipitation (DP) method, the direct application of the method similar to the preparation of silica-supported Au catalysts only results in diminished success. This paper reports a novel, efficient method to synthesize highly active Au catalysts supported on mesoporous silica (SBA-15) through a gold cationic complex precursor [Au(en)2]3+ (en = ethylenediamine) via a wet chemical process. The gold cationic precursor was immobilized on negatively charged surfaces of silica by a unique DP method that makes use of the deprotonation reaction of ethylenediamine ligands. The resulting mesoporous catalyst has been demonstrated to be highly active for CO oxidation at room temperature and even below 273 K, the activity of which is much superior to that of silica-supported Au catalysts previously prepared by various solution techniques. The pH value of the gold precursor solution plays a key role in determining the catalytic activity through the regulation of [Au(en)2]3+ deprotonation reaction and the surface interaction of silica with the gold precursor. This mesoporous gold silica catalyst has also been shown to be highly resistant to sintering because of the stabilization of Au nanoparticles inside mesopores.     

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.     

SiC Monolayers as Promising Substrates for the Development of Highly Stable Palladium Single Atom Catalysts: A Density Functional Theory Study

Single-atom catalysts have been touted as highly efficient catalysts, but the catalytic single-atom sites are unstable and tend to aggregate into nanoparticles during chemical reactions. In this study, we show that SiC monolayers are promising substrates for the development of highly stable single-atom catalysts (Pd₁/SiC) within the density functional theory. In presence of a Si-vacancy, the diffusion barrier energy of a Pd₁ atom embedded in the SiC monolayer is substantially enhanced from 2.3 to 7.8 eV, which is much higher than the reported diffusion barrier energies of graphene, boron nitride and defective MgO of the same catalytic system. Ab initio molecular dynamic calculations at 500 K also confirm the enhanced stability of Pd₁/SiC monolayer (Si-vacancy) such that the Pd₁ atom remains embedded in the vacancy. Additionally, the Pd₁/SiC monolayer (Si-vacancy) catalysts show a ∼34 % reduction of activation barrier energy for CO oxidation as compared to pristine catalysts. This work implies that nanostructured SiC materials are promising substrates for the synthesis of highly stable single-atom catalysts.     

An in-depth study of supported In2O3 catalysts for the selective catalytic reduction of NOx: the influence of the oxide support

The influence of the oxide support (i.e., Al2O3, Nb2O5, SiO2, and TiO2,) on the surface properties, reduction and oxidation properties, acid-base properties, and catalytic activity of supported indium oxide catalysts has been investigated by temperature-programmed reduction/oxidation, thermogravimetry coupled to differential scanning calorimetry, ammonia and sulfur dioxide adsorption calorimetry, and reduction of NOx by ethene in highly oxygen-rich atmosphere. Two series of In2O3-containing catalysts at low (approximately 3 wt %) and at theoretical geometric monolayer (from 20 to 40 wt %) In2O3 content were prepared and their properties were compared with unsupported In2O3 material. Supports able to disperse the In2O3 aggregates with high In stabilization gave rise to active catalytic systems. Among the studied oxide supports, Al2O3 and, to a lower extent, TiO2 were found to be the best supports for obtaining active de-NOx catalysts.     

微波-光催化耦合效应及其机理研究

采用溶胶 凝胶法制备了TiO2和/TiO2催化剂，运用XRD、BET比表面积测定及微波吸收谱等技术对催化剂的结构进行了表征，并以C2H4为模型反应物考察了微波对催化剂的光催化氧化反应性能的影响.研究结果表明，在微波场中TiO2和/TiO2催化剂的光催化氧化性能得到明显改善.时间分辨紫外 可见吸收谱证实微波场的存在有效地提高了催化剂对紫外光的吸收率.因此，微波场与紫外光的耦合使光催化活性提高的可能原因是微波场对多缺陷催化剂的极化作用,提高了光致电子的跃迁几率，并在半导体表面形成陷阱中心,降低了电子 空穴对的复合率.