在醛基化交联聚苯乙烯微球表面同步合成与固载卟啉及固载化金属卟啉的高效催化氧化性能

采用Kornblum氧化反应, 先将氯甲基交联聚苯乙烯(CMCPS)的氯甲基氧化为醛基, 制得醛基(AL)化改性微球ALCPS, 然后使改性微球ALCPS与溶液中的苯甲醛(或取代的苯甲醛)、吡咯之间发生固-液相之间的Adler反应, 成功地实现了卟啉在交联聚苯乙烯微球表面的同步合成与固载, 制得了固载有苯基卟啉(PP) 、对氯苯基卟啉(CPP)、对硝基苯基卟啉(NPP)的功能微球, 最后使功能微球与钴盐发生配合反应, 制备了固载有三种钴卟啉的固体催化剂. 研究重点有两方面: (1)考察主要因素对卟啉同步合成与固载过程的影响|(2)考察固载化钴卟啉在催化分子氧氧化环己烷羟基化过程中的催化特性. 实验结果表明, 以醛基化改性微球ALCPS与溶液中的吡咯及小分子苯甲醛(或取代的苯甲醛)为共反应物, 通过固-液之间的Adler反应, 可以顺利地实现卟啉在微球ALCPS表面的同步合成与固载, 这是制备固载化卟啉的新途径|苯甲醛的取代基结构、催化剂的酸性与溶剂的性质对卟啉的同步合成与固载都有较大的影响|所制备的固体催化剂对分子氧氧化环己烷羟基化的反应, 具有很高的催化活性(环己烷最高转化率约为40%)与选择性(环己醇的选择性在90%以上), 这是由固体催化剂特殊的化学结构所决定的.     

在交联聚苯乙烯微球表面实现苯基卟啉的同步合成与固载

以键合有对羟基苯甲醛(HBA)的交联聚苯乙烯(CPS)微球HBA-CPS、苯甲醛和吡咯为反应物, 采用Adler方法, 实现了苯基卟啉(PP)在CPS表面的同步合成与固载, 制得了固载有苯基卟啉的微球PP-CPS. 研究了卟啉同步合成与固载过程的影响因素, 同时进行了微球PP-CPS与钴盐的配合反应, 制备了固载有钴卟啉(CoP)的功能微球CoP-CPS, 初步考察了其对分子氧氧化乙苯的催化活性. 实验结果表明, 在苯基卟啉同步合成与固载的反应过程中, 催化剂的酸性与溶剂的极性是两个主要的影响因素, 使用强极性溶剂与pKa在2.8~3.4范围的酸, 微球PP-CPS表面的苯基卟啉固载量高. 微球CoP-CPS对分子氧氧化乙苯的反应具有明显的催化活性.     

在聚合物微球 GMA/MMA 表面同步合成与固载卟啉及固载化金属卟啉的催化氧化性能

 制备了甲基丙烯酸缩水甘油酯 (GMA) 与甲基丙烯酸甲酯 (MMA) 共聚微球 GMA/MMA, 并通过键合有对羟基苯甲醛 (HBA) 的改性微球 HBA-GMA/MMA 与苯甲醛 (或取代苯甲醛) 以及吡咯间的 Adler 反应, 实现了卟啉在共聚微球 GMA/MMA 表面的同步合成与固载, 制得了固载有苯基卟啉 (PP)、对氯苯基卟啉 (CPP)、对硝基苯基卟啉 (NPP) 的功能化微球 PP-GMA/MMA, CPP-GMA/MMA 和 NPP-GMA/MMA. 重点考察了影响卟啉同步合成与固载过程的因素. 制备了固载有钴卟啉的催化剂, 并以分子氧氧化乙苯为模型反应, 考察了催化剂的活性. 结果表明, 苯甲醛取代基的结构、催化剂的酸性和溶剂的极性对卟啉的同步合成与固载都有较大的影响; 钴卟啉催化剂对分子氧氧化乙苯反应具有较高的催化活性, 且当钴卟啉外环上含有强吸电子基团硝基时, 催化剂活性最高.     

含环氧基团的聚合物微球固载2,2,6,6-四甲基哌啶氮氧自由基催化剂的制备及其催化分子氧氧化苯甲醇

以甲基丙烯酸缩水甘油酯(GMA)为单体, 以乙二醇二甲基丙烯酸酯(EGDMA)为交联剂, 采用悬浮聚合法制得交联聚甲基丙烯酸缩水甘油酯(CPGMA)微球, 然后以4-羟基-2,2,6,6-四甲基哌啶氮氧自由基(4-OH-TEMPO)为试剂, 使CPGMA微球表面的环氧基团发生开环反应, 从而制得了TEMPO固载化微球TEMPO/CPGMA, 考察了制备条件对固载化反应的影响, 并采用多种方法对微球TEMPO/CPGMA进行了表征. 将微球TEMPO/CPGMA与CuCl组成共催化体系, 用于分子氧氧化苯甲醇, 考察了反应条件对催化体系性能的影响. 结果表明, 以含环氧基团的聚合物微球CPGMA为载体, 通过开环反应, 可成功地实现TEMPO的固载化, 开环反应属S_N2亲核取代反应, 适宜采用溶剂N,N''-二甲基甲酰胺和反应温度85℃. 非均相催化剂TEMPO/CPGMA与助催化剂CuCl构成共催化体系, 在室温、常压O₂条件下可高效地将苯甲醇氧化为苯甲醛, 产物选择性和产率分别为100%和90%. 主催化剂TEMPO与助催化剂CuCl适宜的摩尔比为1:1.2; 主催化剂适宜用量为0.90 g. 此外, TEMPO/CPGMA固体催化剂具有良好的循环使用性能.     

咪唑修饰硅胶配位固载锰(Ⅲ)卟啉对环己烷空气氧化的催化作用

应用3-氯丙基三甲氧基硅烷和咪唑成功地对硅胶表面进行了修饰,并通过咪唑基纵轴配位方式固载了四苯基锰(Ⅲ)卟啉.在无任何外加溶剂及共还原剂的条件下,应用此高分子金属卟啉作为催化剂,选择性地催化空气氧化环己烷为环己酮和环己醇.研究结果表明,与未固载金属卟啉相比,固载金属卟啉具有更高的催化活性和催化选择性,反应具有更高的酮醇比,催化剂的稳定性有了较大的提高,便于回收和重复使用.另外还探讨了载体在此催化体系中对催化性能的影响.     

P(4VP-co-St)/SiO2固载的取代钴卟啉对乙苯的催化氧化性能

通过轴向配位法将不同结构的钴卟啉(CoTXPP(X=H, Cl, NO2))分别固载到接枝微粒聚(4-乙烯基吡啶-co-苯乙烯)/SiO2(P(4VP-co-St)/SiO2)上, 室温下分别制备了P(4VP-co-St)/SiO2固载的金属卟啉催化剂CoTPP-P(4VP-co-St)/SiO2, CoTClPP-P(4VP-co-St)/SiO2和CoTNPP-P(4VP-co-St)/SiO2, 利用傅立叶变换红外(FTIR)光谱和电子吸收光谱对其结构及轴配过程进行了表征. 在无溶剂、无助催化剂和还原剂的体系中, 研究对比了其催化分子氧氧化乙苯为苯乙酮的性能, 考察了不同反应条件对苯乙酮产率的影响. 研究发现, 其催化活性随着环外取代基吸电子能力的增强而提高. CoTNPP-P(4VP-co-St)/SiO2的催化活性和选择性最好, 在120 ℃常压下其催化乙苯反应12 h, 苯乙酮收率达到25.53%, 产物α-甲基苄醇的含量则极少. 与普通的催化剂不同, 在催化氧化体系中, CoTNPP-P(4VP-co-St)/SiO2存在最适宜用量, 过量的CoTNPP-P(4VP-co-St)/SiO2反而会使其催化活性降低; P(4VP-co-St)/SiO2表面CoTXPP的固载密度存在一最佳值. 此外, 固载化以后, 催化剂具有较好的重复使用性. 结果表明, 接枝微粒P(4VP-co-St)/SiO2对金属卟啉不仅有明显的保护作用, 而且能提高其稳定性.     

在CPS微球表面实现N-羟基邻苯二甲酰亚胺的同步合成与固载及固体催化剂催化氧化性能初探

通过分子设计的构思,仅通过两步大分子反应,便实现了N-羟基邻苯二甲酰亚胺(NHPI)在交联聚苯乙烯(CPS)微球表面的同步合成与固载,并制得了非均相催化剂微球CPS-NHPI。以氯化偏苯三酸酐(TMAC)为试剂、Lewis酸为催化剂,通过Friedel-Crafts酰基化反应,先将邻苯二甲酸酐(PA)基团键合在CPS微球表面,得到改性微球CPS-PA;再与盐酸羟胺进行酰亚胺反应,制备出固载有NHPI基团的非均相催化剂微球CPS-NHPI。重点研究了CPS微球表面发生Friedel-Crafts酰基化反应的影响因素。采用红外光谱(FT-IR)及扫描电子显微镜(SEM)等对微球CPS-NHPI进行表征,将微球CPS-NHPI分别用于分子氧氧化乙苯及环己烷两种烃类物质的氧化过程,初步考察了该微球的催化活性。研究结果表明,对于微球CPS与TMAC之间的FriedelCrafts酰基化反应,适宜的溶剂为氯仿与N,N-二甲基乙酰胺(DMAC)混合溶剂(氯仿与DMAC的体积比为7∶3),适宜的Lewis酸催化剂为SnCl4。初步探索实验表明,催化剂微球CPS-NHPI与Co(OAc)2所构成的共催化体系,在分子氧氧化乙苯及环己烷的催化氧化过程中,都表现出了良好的催化活性,温和条件下,反应35h时乙苯氧化为苯乙酮的转化率可达37%,反应30h时环己烷氧化为环己酮的转化率可达21%。     

固载化阳离子金属卟啉/杂多阴离子复合催化剂在分子氧氧化乙苯过程中的催化特性

以交联聚苯乙烯微球(CPS)为基质载体, 采用同步合成与固载的方法, 简捷地制得了固载化阳离子苯基卟啉, 继而通过与钴盐的配合反应, 制备了固载化阳离子钴卟啉. 在此基础上, 以Keggin 型杂多酸磷钨酸(HPW)及磷钼酸(HPMo)为试剂, 凭借阳离子钴卟啉(CoP)与杂多阴离子之间的静电相互作用, 制备与表征了固载化的由阳离子钴卟啉与杂多阴离子复合而成的固体催化剂CoPPW-CPS和CoPPMo-CPS. 将两种复合催化剂用于分子氧氧化乙苯的氧化反应, 考察研究了催化特性. 结果表明: 在分子氧氧化乙苯的氧化反应中, 复合催化剂具有很高的催化活性, 可使乙苯高选择性地转化为苯乙酮, 反应12 h, 苯乙酮的产率达30.1%; 复合催化剂的催化活性比单纯的固载化钴卟啉高75%; CoPPW-CPS的催化活性高于CoPPMo-CPS. 在复合催化剂结构组分中, 固载化的杂多阴离子并无催化活性, 起催化作用的组分是钴卟啉; 但是, 杂多阴离子可有效保护钴卟啉, 使其免于被氧化失活, 从而使其保持稳定的高催化活性. 复合催化剂具有最适宜的投加量, 过量催化剂的加入, 会抑制钴卟啉的催化活性. 复合催化剂还具有良好的循环使用性能.     

聚合物微球固载的N-羟基邻苯二甲酰亚胺在分子氧氧化甲苯过程中的催化性能

以交联聚苯乙烯(CPS)微球为基质,经过几步大分子反应在微球表面合成与固载了N-羟基邻苯二甲酰亚胺(NHPI),形成固载有NHPI的聚合物微球CPS-NHPI。本文主要将CPS-NHPI与过渡金属盐组成共催化体系,用于分子氧氧化甲苯的反应,考察了该非均相催化剂的催化特性与催化氧化机理。结果表明,几种过渡金属盐中,Co(OAc)2的助催化效果最好;微球CPS-NHPI与Co(OAc)2所构成的共催化体系,在温和条件(80℃和常压氧气)下可有效地将甲苯深度氧化为苯甲酸,显现出高的催化活性(甲苯转化率达到57%)与优良的选择性(苯甲酸的选择性达到84%)。催化氧化反应遵循自由基链式反应机理。主催化剂CPS-NHPI固载的NHPI与助催化剂Co(OAc)2适宜的摩尔比为14∶1,主催化剂所含NHPI为底物的12(mol)%时,催化剂用量较为合适。固体催化剂CPS-NHPI具有良好的再循环使用性能。     

季鏻盐型三相相转移催化剂的制备及其化学结构与相转移催化活性的关系

 使用两种 ω-氯代酰氯 (氯乙酰氯与氯丁酰氯) 对交联聚苯乙烯微球 (CPS) 进行 Friedel-Crafts 酰基化反应,使用 1,4-二氯甲氧基丁烷对 CPS 微球进行氯甲基化反应, 分别将可交换的氯引入 CPS 微球表面, 制备了化学改性的 CPS 微球. 然后使用三苯基膦对改性微球进行季鏻化反应, 制备了间隔臂 (spacer arm) 长度不同的三种季鏻 (QP) 盐型三相相转移催化剂 QP-CPS. 考察了主要反应条件对制备过程的影响, 并以氯化苄与乙酸钠合成乙酸苄酯的反应体系作为三相相转移催化的模型体系, 初步考察了 QP-CPS 的相转移催化活性,探索了催化剂结构与相转移催化活性的关系. 结果表明, 季鏻盐的化学稳定性较差,在制备过程中需控制反应时间与温度, 且宜选用极性较高的溶剂. 季鏻盐型三相相转移催化剂 QP-CPS 对乙酸苄酯的合成具有较高的催化活性, 在液-固-液之间可有效地实现反应物种乙酸根的转移. 与季铵盐 (QN) 型三相相转移催化剂 QN-CPS 相比, 季鏻盐型三相相转移催化剂 QP-CPS 具有更高的相转移催化活性. 间隔臂越长, QP-CPS 的相转移催化活性越高, QP-CPS 的亲水和亲油性能对相转移催化活性也有很大的影响.     

Synthesis and catalytic activities in cyclohexane hydroxylation of metalloporphyrins supported on styrene-methylacrylic acid copolymer microspheres

Through a new synthetic strategy, metalloporphyrins (M = Fe(III), Mn(III) or Co(II)) were covalently immobilized on styrene-methylacrylic acid copolymer microspheres. These copolymer-immobilized metalloporphyrins were found to be more efficient catalysts than the analogous non-supported metalloporphyrins for cyclohexane hydroxylation in metalloporphyrin–O₂–ascrobate mixtures. The catalytic activities of the immobilized catalysts follow the order Fe>Mn>Co.     

Poly(crotonic acid-co-2-acrylamido-2-methyl-1-propanesulfonic acid)-metal complexes with copper(II), cobalt(II), and nickel(II): Synthesis, characterization and antimicrobial activity

Poly(crotonic acid-co-2-acrylamido-2-methyl-1-propanesulfonic acid) [P(CrA-co-AMPS)] (44.22:55.78) copolymer was prepared in N,N-dimethylformamide solution using the benzoyl peroxide (Bz₂O₂) as initiator. Cu(II), Ni(II) and Co(II) chelates of the copolymer were prepared and the formation constants of each complex were determined by the mole-ratio method using UV-vis spectroscopy. UV-vis studies showed that the complex formation tendency increased in the followed order: Cu(II) > Ni(II) > Co(II). The copolymer and its metal chelates were characterized by FTIR, TGA, X-ray diffraction and SEM analysis. Also, in vitro antimicrobial activity of the polymers were tested on various bacteria, and yeast.     

P改性对Mo-Ni/Al2O3煤焦油加氢脱氮性能的影响

在磷含量1.34%下,采用分步浸渍法按磷添加顺序不同制备了3种改性催化剂:MoP-Ni/Al₂O₃、Mo-NiP/Al₂O₃、Mo-Ni/PAl₂O₃.通过X射线衍射(XRD)、程序升温脱附(NH₃-TPD)、程序升温还原(H₂-TPR)、氮气吸附等技术对催化剂进行了表征.以新疆中低温煤焦油为原料,考察了不同磷改性方式对催化剂加氢脱氮(HDN)性能的影响.结果表明,适宜的磷添加方式能够改变催化剂的酸性分布,提高10~13 nm加氢脱氮有效孔的比例,并且减弱活性组分与载体的相互作用,同时使得活性组分更易被还原,进而提高催化剂加氢脱氮性能.加氢脱氮活性顺序为Mo-Ni/PAl₂O₃(74.36%)>Mo-NiP/Al₂O₃(72.74%)>Mo-Ni/Al₂O₃(71.72%)>MoP-Ni/Al₂O₃(56.13%).     

Low temperature splinting activity and catalytic behavior of nano Ag doped sulphamicacid bridged diblock copolymer

A novel silver nanoparticle doped diblock copolymer was synthesized by a 3‐step process via bulk polymerization process under nitrogen atmosphere. The above prepared polymer is characterized by FTIR spectroscopy, fluorescence emission spectroscopy, circular dichroism (CD), HRTEM, and FESEM. The sulphamicacid end capped poly(ε‐caprolactone) (P1) system exhibited higher tensile strength than the sulphamicacid bridged diblock copolymer (P2) and nano Ag doped sulphamicacid bridged diblock copolymer (P3) systems. The splinting activity of the diblock copolymers was tested and confirmed the low temperature splinting activity of the diblock copolymer. The Ag nanoparticle catalyzed catalytic reduction of p‐nitrophenol (NiP) was tested, and the apparent rate constant (k_app) was determined as 7.36 × 10⁻³ sec⁻¹. The thermal studies were carried out by DSC and TGA methods. The TGA study declared that the P1 system has higher degradation temperature than the P2 and P3 systems. The P1 system has higher melting temperature (T_m) (75.5°C) than the P2 and P3 systems. The CD study indicated that the conformation of sulphamicacid was not changed even after the formation of nano Ag doped sulphamicacid bridged diblock copolymer.     

Copolymers of poly-{acrylamide-co-[3- (acryloylamino)propyltrimethylammoniumchloride]} as carriers for platinum species and their use as catalysts in heterogeneous gas phase reactions

In the following, the binding of PtCl₆²⁻ to quarternary ammonium groups of the copolymers followed by reduction of platinum to a zerovalent state is described. At temperatures between 60 and 180°C the supported catalysts were effective in isomerization and hydrogenation of hexene(1). The dependence of catalytic activity and selectivity on copolymer composition and the average molecular weight (M_w) of the polymer have been analyzed. Copolymers of the composition 90% acrylamide/10% quarternary compound and average molecular weights of about one million were found to be the most active ones. Thermal and chemical stability of the catalysts were studied by differential thermal analyses, thermal gravimetric analyses, and elemental analyses. Morphology and structure were analyzed by raster electron microscopy, x-ray photon spectroscopy, far infrared spectroscopy, and Fourier transform infrared spectroscopy. Several particle properties of the new catalysts, such as pore volume and surface area, were also investigated. © 1996 John Wiley & Sons, Inc.     

Polyoxometalate-Derived Multi-Component X/W2C@X,N-C (X=Co,Si, Ge,B, and P) Nanoelectrocatalysts for Efficient Triiodide Reduction in Dye-Sensitized Solar Cells

Multi-component tungsten carbide-based hybrid materials featuring different heteroatom dopants coated with X,N dual-doped carbon layers (X/W₂C@X,N-C, XWXNC) were prepared by selecting Keggin-type polyoxometalates (POMs) (NH₄)_n[XW₁₂O₄₀] (X=Co, Si, Ge, B, and P) and dicyandiamide (DCA) as precursors. The electrocatalytic activity of these nanocomposites as counter electrode (CE) catalysts for dye-sensitized solar cells (DSSCs) was systematically investigated. Structure characterizations show that X,N heteroatoms were successfully introduced into the W₂C and carbon frameworks. The obtained X,N dual-doped carbon layers were modified and loaded with W₂C nanoparticles, promoting the improvement of catalytic performance by a synergistic effect. The consequence of photoelectric conversion efficiency (PCE) is CoWCoNC (6.68 %)>SiWSiNC (6.56 %)>GeWGeNC (6.49 %)>BWBNC (6.45 %)>PWPNC (6.20 %)>WNC (6.05 %). With the increase in electronegativity of the dopants, the photovoltaic performance decreases in a reverse order. This work provides a shortcut to the rational design of highly efficient and cost-effective catalysts for DSSCs.     

Propane oxidative dehydrogenation over V-containing mixed oxides derived from decavanadate-exchanged ZnAl–layered double hydroxides prepared by a sol–gel method

The catalytic properties of ZnAlVO mixed oxides derived from decavanadate-exchanged ZnAl–layered double hydroxide (LDH) precursors prepared by a sol–gel method (ZnAlVO–LDHx,y) were investigated in the oxidative dehydrogenation of propane and compared with those of supported catalysts obtained by conventional impregnation of NH₄VO₃ on ZnO (ZnVO-I,y) and ZnAlO mixed oxide (ZnAlVO-I,y) supports. The effects of composition and calcination time on the catalytic behavior were particularly examined. Higher propane conversions were achieved at higher vanadium content and calcination time of the precursors. The LDH-derived catalysts were the most active ones in all the temperature range studied (300–425 °C). The order of activity for propane conversion for the different catalyst families varies as ZnAlVO–LDHx,y > ZnAlVO-I > ZnVO-I and follows the strength of the Lewis and Brønsted acid sites determined by monitoring of pyridine adsorption by Fourier transform infrared spectroscopy, whereas the propene selectivities are close together in agreement with the similar densities of basic sites determined by CO₂–temperature-programmed desorption measurements. It was indeed established that the acidity, rather than the nature of the crystalline phases, the reducibility, or the specific surface area of the samples, governs the catalytic activity.     

Hydrogenation of acetone on technetium catalysts

The catalytic properties of supported mono- and bimetallic catalysts of the Tc/support, M/support, and M-Tc/support types (M=Pt, Pd, Rh, Ru, Ni, Re, Co; supports are γ-Al₂O₃, MgO, SiO₂) were investigated in the acetone hydrogenation. The main products of this reaction are isopropyl alcohol and propane. The catalytic activity in the acetone hydrogenation of the metals studied decreases in the consequence Pt>Tc≈Rh>Pd>Ru >Ni≈Re>Co (with γ-Al₂O₃ as the support). The influence of support nature on the catalytic activity was investigated for the Rh−Tc system as an example. A nonadditive increase in the catalytic activity of Rh−Tc/γ-Al₂O₃ in comparison with monometallic catalysts was found. The state of the surface of the catalysts was characterized by the UV-VIS diffuse reflectance spectra. Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No. 3, pp. 414–417, March, 1998.     

Mesoporous phosphated and sulphated silica as solid acid catalysts for glycerol acetylation

Sulphate- and phosphate-loaded silicas were synthesised using the sol-gel method with different sulphate and phosphate loadings. These catalysts were characterised using Fourier transform infrared spectroscopy (FT-IR), the Brunauer-Emmett-Teller (BET) method and X-ray photoelectron spectroscopy (XPS). Acidity was measured using the temperature-programmed desorption of ammonia (TPD-NH3) method. The results showed that glycerol esterification with acetic acid conversion decreased as follows: α(H₂SO₄) (100 %) > α(H₃PO₄) (99 %) > α(silica loaded with 20 % sulphuric acid) (SS-20; 98 %) > α(silica loaded with 20 % phosphoric acid) (PS-20; 83 %). These studies suggest that the solid acid catalytic activity in the esterification of glycerol is highly dependent on catalyst acidity strength, pore size and surface area.     

Oxidative dehydrogenation of ethylbenzene to styrene with CO2 over Al-MCM-41-supported vanadia catalysts

Catalytic performance of Al-MCM-41-supported vanadia catalysts (V/Al-MCM-41) with different V loading was investigated for oxidative dehydrogenation of ethylbenzene to styrene (ST) with CO₂ (CO₂-ODEB). For comparison, pure silica MCM-41 was also used as support for vanadia catalyst. The catalysts were characterized by N₂ adsorption, X-ray diffraction (XRD) pyridine-Fourier-transform infrared spectroscopy, H₂-temperature-programmed reduction, thermogravimetric analysis (TGA), UV-Raman, and diffuse reflectance (DR) UV–vis spectroscopy. The results indicate that the catalytic behavior and the nature of V species depend strongly on the V loading and the support properties. Compared with the MCM-41-supported catalyst, the Al-MCM-41-supported vanadia catalyst exhibits much higher catalytic activity and stability along with a high ST selectivity (>98%). The superior catalytic performance of the present V/Al-MCM-41 catalyst can be attributed to the Al-MCM-41 support being more favorable for the high dispersion of V species and the stabilization of active V⁵⁺ species. Together with the characterization results of XRD, TGA, and DR UV–Vis spectroscopy, the deep reduction of V⁵⁺ into V³⁺ during CO₂-ODEB is the main reason for the deactivation of the supported vanadia catalyst, while the coke deposition has a less important impact on the catalyst stability.