多位点离子液体聚合物催化CO2环加成反应研究

CO₂与环氧化物环加成反应制备环状碳酸酯是一条绿色经济的CO₂利用途径。针对现有CO₂与环氧化物环加成反应中非均相离子液体催化剂活性低和活性组分易流失等问题,设计制备了系列多位点离子液体超交联聚合物HCPs-[DmPhe]Br,研究了多位点协同作用、超交联聚合物组成和结构等因素对其催化CO₂与环氧化物环加成反应性能的影响。其中,同时含有双季铵-卤素离子对、羟基和叔胺结构的HCP-[DmPhe]Br-DCX离子液体超交联聚合物催化剂,在1.3 MPa, 130℃,8 h的条件下,可实现94%的碳酸丁烯酯收率,且催化剂循环稳定性好,重复使用5次,催化活性没有明显降低。另外,超交联聚合物的多孔结构以及大比表面积促进了离子液体的较好分散,使其与离子液体单体具有相当的活性。该工作对CO₂与环氧化物环加成反应高效非均相离子液体催化剂的开发与优化具有一定的借鉴意义。     

多孔有机聚合物催化二氧化碳合成环状碳酸酯研究进展

二氧化碳（CO₂）捕集、利用和储存（CCUS）在全球能源结构转型中是一种极具潜力的策略,能够实现能源供给、基础原料产出以及限制气候变化。多孔有机聚合物（POPs）具有高CO₂吸附容量和吸附选择性、突出的结构特性以及优异的化学可调控性,其作为极具潜力的材料广泛应用于催化CO₂参与的有机反应中。其中,CO₂与环氧化物环加成生成环状碳酸酯的反应具有100%的原子经济性,且其产物也极具工业价值。本文基于CO₂环加成反应催化机制,从催化剂的合成方法、结构性质与组成特性角度出发,综述了POPs在CO₂/环氧化物环加成反应的研究进展,包括金属配合物类、氢键供体类、离子液体类、金属配合物/离子液体和氢键供体/离子液体等有机多孔聚合物体系。通过阐述POPs在催化CO₂制备高附加值环状碳酸酯反应中的研究现状和发展趋势,为POPs的开发与应用以及CO₂综合利用的工业化探索提供具有建设性的指导意见。     

多孔超交联聚合物固载离子液体催化二氧化碳环加成反应的研究进展

CO₂是一种主要的温室气体,以CO₂为原料与环氧化物发生环加成反应可以制备各种环状碳酸酯,是一种绿色可行的CO₂捕集及利用途径。多孔超交联聚合物固载离子液体（hypercrosslinked polymers immobilized ionic liquids,HCP-ILs）催化CO₂环加成反应具有无需溶剂、金属和助催化剂等优点。本文对其近年来的最新研究进展进行了综述,总结了离子单体自聚/共聚或交联法、离子与交联一步法以及交联后修饰法三种制备超交联聚合物固载离子液体方法的特点,分析了目前还存在离子密度偏低、催化效率不够高以及制备成本偏高等不利于“CO₂化工”应用的问题,并指出为实现在常压下快速催化CO₂与环氧化物的环加成反应,应从提高离子密度、调控表面活化功能基团和离子微环境以及降低制备成本等方向加强理论研究和技术攻关。     

CO2合成醇酯类化学品和高分子材料研究进展

我国作为煤炭大国,燃烧化石燃料产生大量CO₂。通过化学作用将CO₂转化为能源燃料、基础化学品或高分子材料,有利于实现碳氧资源综合利用。从CO₂直接利用和间接利用的角度出发,分别综述了CO₂资源化利用研究进展。直接利用方面,重点阐述了CO₂直接加氢合成甲醇和乙醇;同时CO₂可作为羰化剂合成有机碳酸酯和高分子材料,包括碳酸二乙酯、聚碳酸酯和CO₂基可降解聚合物。在间接利用方面,重点综述了CO₂经碳酸乙烯酯的酯交换反应合成碳酸二甲酯,以及碳酸乙烯酯加氢制备甲醇联产乙二醇的研究进展。CO₂加氢直接合成甲醇催化剂主要包括铜基催化剂、贵金属催化剂,由于贵金属的成本高,廉价的Cu基催化剂研究较为广泛。CO₂加氢直接合成乙醇研究较广泛的催化剂为贵金属(Rh、Pd、Ru)基催化剂体系,还需进一步研究廉价、高活性和高稳定性的催化剂。CO₂与乙醇直接合成碳酸二乙酯(DEC)研究较多的催化剂为铈基多相催化剂,但由于生成物中水分的影响,限制了DEC的收率。环氧化物和CO₂耦合反应生成DEC过程中不产生水,可以有效克服热力学的限制,因此高能化合物与CO₂的耦合路线是高效制备DEC的有效途径。CO₂与环氧化物共聚制备聚碳酸酯材料多采用稀土三元催化剂体系,环氧化物的转化率和聚碳酸酯选择性较高,目前已经实现工业应用。CO₂通过碳酸乙烯酯与甲醇酯交换合成DMC,多使用碱性较强的催化剂和含碱性基团的离子交换树脂。CO₂经碳酸乙烯酯加氢制备甲醇和乙二醇的反应中,铜基催化剂展现出优异的催化性能。CO₂化学转化利用是CO₂碳氧资源综合利用的重要途径,将有效支撑我国未来碳中和目标实现。     

离子液体支撑液膜的CO2/CH4分离性能

由于离子液体对CO₂具有较好的溶解选择性,离子液体支撑液膜分离CO₂越来越受到关注。比较了含3种不同阴离子的常规离子液体([bmim][BF₄]、[bmim][PF₆]、[bmim][Tf₂N])作为支撑液膜的液膜相分离CO₂/CH₄的性能,考察了咪唑环上烷基链长对离子液体支撑液膜性能的影响。考虑向离子液体中引入胺基和羧基等亲CO₂基团,制备了1-丁基-3-甲基咪唑丙氨酸离子液体([bmim][β-Ala]),考察了 [bmim][β-Ala]支撑液膜分离CO₂/CH₄的性能,并对在CO₂渗透测试前后的支撑液膜进行了FT-IR分析,发现氨基酸离子液体中的-NH₂和CO₂的较强作用以及该离子液体的高黏性影响了CO₂的透过性,使[Bmim][β-Ala]支撑液膜的CO₂透过率低。     

醚基高铼酸盐离子液体的催化性能研究

自合成两种新型醚基高铼酸盐离子液体：1-(2-甲氧基乙基)-3-乙基咪唑高铼酸盐（[C₂2O1Im][ReO₄]）和1-(2-乙氧基乙基)-3-乙基咪唑高铼酸盐（[C₂2O2Im][ReO₄]）,并利用核磁共振氢谱/碳谱、拉曼光谱、质谱和差示扫描量热等方法表征,确定是目标产物。环氧化合物是一种化学性质活泼且易转化为其他物质的有机合成中间体,烯烃的环氧化反应是合成环氧化合物的一种重要途径,因此建立以新型醚基高铼酸盐离子液体为溶剂兼催化剂的环辛烯环氧化均相反应体系,系统研究反应温度、时间、氧化剂用量、催化剂用量及循环使用等因素的影响。结果表明,产率大于90%,反应选择性大于99%,催化剂循环5次,产率无明显下降。     

CO2环加成过程中副产物溴乙醇的催化转化研究

CO₂是温室气体之一，其在大气中快速大量积累直接导致了全球变暖和生态破坏等环境问题。从可再生碳资源利用的角度来讲，CO₂是广泛存在、价廉易得的C1资源。以环氧乙烷(EO)和CO₂为原料生产碳酸乙烯酯(EC)的工艺，具有高“原子经济”和“绿色化学”的优势，为C1资源的化学利用提供可行的工业方案。卤素离子型催化剂是该环加成反应的传统催化剂，但在反应过程中，催化剂中卤离子流失，生成副产物卤代醇分子，从而影响主产物碳酸乙烯酯的收率、增加了分离难度和对设备的要求。因此，开发理想的催化体系，将副产物卤代醇抑制并转化、促使其正向消耗十分必要。本工作设计开发了系列弱碱性离子液体，以溴乙醇(BE)为研究对象，在环加成反应条件(温度130℃、CO₂压力3 MPa、反应时间3 h)下，添加弱碱性离子液体，实现了溴乙醇的原位转化。考察了不同的反应条件和不同碱性离子液体对溴乙醇转化的影响，包括离子液体种类、反应温度、压力环境、反应时间等因素，揭示了溴乙醇转化的反应规律，其中[Bu4P][HCO3]的效果最好；采用气体氛围和溶...     

离子液体和低共熔溶剂催化二氧化碳合成有机碳酸酯的研究进展

离子液体和低共熔溶剂因其良好的溶解与催化能力,可催化CO₂转化为高附加值化学品。本文综述了离子液体和低共熔溶剂催化CO₂转化为有机碳酸酯的研究进展,分析了CO₂与醇生成直链碳酸酯以及与环氧化物生成环状碳酸酯的反应机理;介绍了传统型、质子型、功能化离子液体以及由氯化胆碱、季铵盐与季膦盐、有机碱等作为氢键受体组成的低共熔溶剂,及其在CO₂转化为直链和环状碳酸酯反应中的催化性能;总结了此两类反应中离子液体和低共熔溶剂设计的基本规律;指出了CO₂转化反应中离子液体与低共熔溶剂存在的催化效率低、稳定性不高、后续分离困难等问题,后续研究可结合计算机辅助设计方法,探索更合适的阴阳离子/氢键供受体组合,获得更高效的催化体系。     

二氧化碳与环氧化合物催化共聚反应研究进展

CO₂与环氧化物开环共聚合成聚碳酸酯(PC)是实现CO₂大规模资源化利用的有效途径。聚碳酸酯是完全生物降解的塑料,广泛用于一次性包装材料、地膜等,能够为解决石油基废旧塑料造成的“白色污染”和实现碳减排提供解决方案。开发高效催化体系是实现CO₂与环氧化物共聚反应高效合成PC的关键。本篇综述主要总结了用于CO₂与环氧化合物共聚反应的金属配合物和有机催化剂,涉及多种金属配合物,以及新兴的非金属催化剂。     

CO2甲烷化催化剂的研究进展

CO₂甲烷化反应因其可以将温室气体CO₂转化为清洁能源(CH₄)而受到广泛关注。本文介绍了CO₂甲烷化反应的机理与热力学研究进展,分析了CO₂甲烷化催化剂活性中心、粒子尺寸和载体效应对催化剂反应性能的影响规律。介绍了高熵合金、溶出型金属等新型催化剂在CO₂甲烷化反应中的应用,总结了影响Ni基CO₂甲烷化催化剂反应稳定性的2个主要因素(粒子烧结和硫中毒)以及提高Ni基催化剂抗烧结和抗硫中毒的举措(利用限域效应、添加CeO₂等),从而为新型CO₂甲烷化催化剂的研究和开发提供理论基础。最后,对CO₂甲烷化催化剂的研究开发进行了展望。     

Improvement of coke resistance of Ni/Al2O3 catalyst in CH4/CO2 reforming by ZrO2 addition

This work investigates the improvement of Ni/Al₂O₃ catalyst stability by ZrO₂ addition for H₂ gas production from CH₄/CO₂ reforming reactions. The initial effect of Ni addition was followed by the effect of increasing operating temperature to 500–700 °C as well as the effect of ZrO₂ loading and the promoted catalyst preparation methods by using a feed gas mixture at a CH₄:CO₂ ratio of 1:1.25. The experimental results showed that a high reaction temperature of 700 °C was favored by an endothermic dry reforming reaction. In this reaction the deactivation of Ni/Al₂O₃ was mainly due to coke deposition. This deactivation was evidently inhibited by ZrO₂, as it enhances dissociation of CO₂ forming oxygen intermediates near the contact between ZrO₂ and nickel where the deposited coke is gasified afterwards. The texture of the catalyst or BET surface area was affected by the catalyst preparation method. The change of the catalyst texture resulted from the formation of ZrO₂–Al₂O₃ composite and the plugging of Al₂O₃ pore by ZrO₂. The 15% Ni/10% ZrO₂/Al₂O₃ co-impregnated catalyst showed a higher BET surface area and catalytic activity than the sequentially impregnated catalyst whereas coke inhibition capability of the promoted catalysts prepared by either method was comparable. Further study on long-term catalyst stability should be made.     

Mixed oxides Ca2Fe2O5 and Ca2Co2O5 as anode materials for Li-ion batteries

The electrochemical performance of mixed oxides, Ca₂Fe₂O₅ and Ca₂Co₂O₅ for use in Li-ion batteries was studied with Li as the counter electrode. The compounds were prepared and characterized by X-ray diffraction and SEM. Ca₂Fe₂O₅ showed a reversible capacity of 226 mAh/g at the 14th cycle and retained 183 mAh/g at the end of 50 cycles at 60 mA/g in the voltage window 0.005-2.5 V. A reversible capacity in the range, 365-380 mAh/g, which is stable up to 50 charge-discharge cycles is exhibited by Ca₂Co₂O₅ in the voltage window, 0.005-3.0 V and at 60 mA/g. This corresponds to recycleable moles of Li of 3.9±0.1 (theoretical: 4.0). Significant improvement in the cycling performance and attainable reversible capacity were noted for Ca₂Co₂O₅ on cycling to an upper cut-off voltage of 3.0 V as compared to 2.5 V. Coulombic efficiency for both compounds is >98%. Electrochemical impedance spectroscopy (EIS) data clearly indicate the reversible formation/decomposition of polymeric surface film on the electrode surface of Ca₂Co₂O₅ in the voltage window, 0.005-3.0 V. Cyclic voltammetry results compliment the galvanostatic cycling data.     

Phase diagram of the Al2O3-HfO2-Y2O3 system

The phase diagram of the Al₂O₃-HfO₂-Y₂O₃ system was first constructed in the temperature range 1200-2800 °C. The phase transformations in the system are completed in eutectic reactions. No ternary compounds or regions of appreciable solid solution were found in the components or binaries in this system. Four new ternary and three new quasibinary eutectics were found. The minimum melting temperature is 1755 °C and it corresponds to the ternary eutectic Al₂O₃ + HfO₂ + Y₃Al₅O₁₂. The solidus surface projection, the schematic of the alloy crystallization path and the vertical sections present the complete phase diagram of the Al₂O₃-HfO₂-Y₂O₃ system.     

Al2O3-coated SnO2/TiO2 composite electrode for the dye-sensitized solar cell

A novel Al₂O₃-coated SnO₂/TiO₂ composite electrode has been applied to the dye-sensitized solar cell. In such an electrode, two kinds of energy barriers (SnO₂/TiO₂ and TiO₂/Al₂O₃) were designed to suppress the recombination processes of the photo-generated electrons and holes. After the SnO₂ was modified by colloid TiO₂, the photoelectric conversion efficiency of the SnO₂/TiO₂ composite cell increased to 2.08% by a factor of 2.8 comparing with that of the SnO₂ cell. The Al₂O₃ layer on the SnO₂/TiO₂ composite electrode further suppressed the generation of the dark current, resulting in 37% improvement in device performance comparing with the SnO₂/TiO₂ cell.     

The catalytic performance in oxidative coupling of methane and the surface basicity of La2O3, Nd2O3, ZrO2 and Nb2O5

The catalytic performance in oxidative coupling of methane (OCM) of unmodified pure La₂O₃, Nd₂O₃, ZrO₂ and Nb₂O₅ has been investigated under various conditions. The results confirmed that the activity of La₂O₃ and Nd₂O₃ was always much higher than that of the remaining two. The surface basicity/base strength distribution of pure La₂O₃, Nd₂O₃, ZrO₂ and Nb₂O₅ was measured using a test reaction of transformation of 2-butanol and a temperature-programmed desorption of CO₂. Both methods showed that La₂O₃ and Nd₂O₃ had high basicity and contained medium and strong basic sites (lanthanum oxide more and neodymium oxide somewhat less). ZrO₂ had only negligible amount of weak basic sites and Nb₂O₅ was rather acidic. The confrontation of the basicity and catalytic performance indicated that in the case of investigated oxides, the basicity (especially strong basic sites) could be a decisive factor in determination of the catalytic activity in OCM. Only in the case of ZrO₂ it was observed a moderate catalytic performance in spite of negligible basicity. The influence of a gas atmosphere used in the calcination of oxides (flowing oxygen, helium and nitrogen) on their basicity and catalytic activity in OCM had been also investigated. Contrary to earlier observations with MgO, no effect of calcination atmosphere on the catalytic performance of investigated oxides in OCM and on their basicity was observed.     

SO2 and NO removal from flue gas over V2O5/AC at lower temperatures — role of V2O5 on SO2 removal

Supporting V₂O₅ onto an activated coke (AC) has been reported to significantly increase the AC's activity in simultaneous SO₂ and NO removal from flue gas. To understand the role of V₂O₅ on SO₂ removal, V₂O₅/AC is studied through SO₂ removal reaction, surface analysis, X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS) and Fourier transform infrared (FTIR) techniques. It is found that the main role of V₂O₅ in SO₂ removal over V₂O₅/AC is to catalyze SO₂ oxidation through a VOSO₄-like intermediate species, which reacts with O₂ to form SO₃ and V₂O₅. The SO₃ formed transfers from the V sites to AC sites and then reacts with H₂O to form H₂SO₄. At low V₂O₅ loadings, a V atom is able to catalyze as many as 8 SO₂ molecules to SO₃. At high V₂O₅ loadings, however, the number of SO₂ molecules catalyzed by a V atom is much less, due possibly to excessive amounts of V₂O₅ sites in comparison to the pores available for SO₃ and H₂SO₄ storage.     

Simultaneous easy CO2 recovery and drastic reduction of SOx and NOx in O2/CO2 coal combustion with heat recirculation

Coal combustion with O₂/CO₂ is promising because of its easy CO₂ recovery, extremely low NO_x emission and high desulfurization efficiency. Based on our own fundamental experimental data combined with a sophisticated data analysis, its characteristics were investigated. It was revealed that the conversion ratio from fuel-N to exhausted NO in O₂/CO₂ pulverized coal combustion was only about one fourth of conventional pulverized coal combustion. To decrease exhausted NO further and realize simultaneous easy CO₂ recovery and drastic reduction of SO_x and NO_x, a new scheme, i.e. O₂/CO₂ coal combustion with heat recirculation, was proposed. It was clarified that in O₂/CO₂ coal combustion, with about 40% of heat recirculation, the same coal combustion intensity as that of coal combustion in air could be realized even at an O₂ concentration of as low as 15%. Thus exhausted NO could be decreased further into only one seventh of conventional coal combustion. Simultaneous easy CO₂ recovery and drastic reduction of SO_x and NO_x could be realized with this new scheme.     

Electrocatalytic activity of IrO2-RuO2 supported on Sb-doped SnO2 nanoparticles

Electrocatalytic IrO₂-RuO₂ supported on Sb-doped SnO₂ (ATO) nanoparticles is very active towards the oxygen evolution reaction. The IrO₂-RuO₂ material is XRD amorphous and exists as clusters on the surface of the ATO. Systematic changes to the surface chemical composition of the ATO as a function of the IrO₂:RuO₂ ratio suggests an interaction between the IrO₂-RuO₂ and ATO. Cyclic voltammetry indicates that the electrochemically active surface area of IrO₂-RuO₂ clusters is maximised when the composition is 75 mol% IrO₂-25 mol% RuO₂. Decreasing the loading of IrO₂-RuO₂ on ATO reduces the electrochemically active surface area, although there is evidence to support a decrease in the clusters size with decreased loading. Tafel slope analysis shows that if the clusters are too small, the kinetics of the oxygen evolution reaction are reduced. Overall, clusters of IrO₂-RuO₂ on ATO have similar or better performance for the oxygen evolution reaction than many previously reported materials, despite the low quantity of noble metals used in the electrocatalysts. This suggests that these oxides may be of economic advantage if used as PEM water electrolysis anodes.     

Influence of TiO2 and CeO2 on the hydrogenation activity of bulk Ni2P

TiO₂- and CeO₂-promoted bulk Ni₂P catalysts were prepared by impregnation and in-situ H₂ temperature-programmed reduction method. The prepared catalysts were characterized by XRD and XPS. The hydrogenation activities of the catalysts were studied using 1.5 wt.% 1-heptene in toluene and 1.0 wt.% phenylacetylene in ethanol as the model feeds. The results indicate that bulk Ni₂P possesses low hydrogenation activity but is tunable by simply controlling the content of the additives (TiO₂ or CeO₂), suggesting that TiO₂ and CeO₂ are effective promoters to enhance the hydrogenation activity of Ni₂P.     

Dynamic corrosion of Al2O3-ZrO2-SiO2 and Cr2O3-containing refractories by molten frits. Part I: Macroscopic analysis

Manufacturing of enamels and frits has undergone dramatic changes since the 1980s. This has required significant efforts in research and development. Typical compositions of frits for ceramic tiles are silica-based with fluxing agents; some of the components are highly corrosive. Improvements in the production of frits would imply the selection of the most adequate refractories as a function of the chemical composition of the considered frit and the fabrication procedure.The refractories currently used in frit furnaces are Al₂O₃-ZrO₂-SiO₂ (AZS) fused cast materials and Cr₂O₃-based materials. In this work, results on dynamic corrosion studies of AZS and Cr₂O₃-based materials by two ZnO-containing frits are described. Experiments have been performed using the “Merry Go Round” test at ≅1500 °C. Macroscopic results are analysed in terms of the remaining volume after the tests, as usually done in the glass industry. The significance and limits of such an approach are discussed.