丁烷氧化制顺丁烯二酸酐催化剂活性相的研究

通过活性测试及催化剂表征研究了用于丁烷氧化制顺酐VPO催化剂的反应控制步骤-脱氢反应的机理,分析了(VO)2P2O7(020)面的催化脱氢过程,同时对β—VOPO4相在催化脱氢过程中的作用进行了研究。丁烷氧化制顺酐VPO催化剂中,最重要的活性相是(VO)2P2O7,而(020)面是(VO)2R2O7的活性面。与此同时,β—VOPO4相也是重要的活性相,只有在β—VOPO4相与(VO)2R2O7协同作用下,方可对丁烷分子进行较适当地活化,使脱氢作为控制步骤能够顺利进行。     

Synthesis and catalytic oxidation properties of polymer‐bound cobalt complexes

Polymer‐bound 2,2′‐bipyridine cobalt complexes PSBPY‐Co, PSBPY‐Co‐bipy, PSBPY‐Co‐oxine, and PSBPY‐Co‐phen (where PSBPY: polystyrene bound‐2,2′‐bipyridine; bipy: 2,2′‐bipyridine; phen: 1,10‐phenanthroline) were synthesized and investigated by IR, X‐ray photoelectric spectroscopy, thermogravimetry–differential thermal analysis, inductively coupled plasma atomic emission spectrometry, and elemental analysis. The complexes were found to be catalysts for the oxidation of alkylbenzenes and cyclohexene in the presence of molecular oxygen in the absence of solvent. © 2000 John Wiley & Sons, Inc. J Appl Polym Sci 75: 1068–1074, 2000     

谷氨酸希夫碱钴配合物对环己烯的催化氧化性能研究

研究了谷氨酸水杨醛希夫碱配合物(Sal—Glu—M)对环己烯的催化氧化性能,详细探讨了谷氨酸水杨醛希夫碱钴配合物(Sal—Glu—Co)在不同反应条件下对环己烯的催化氧化性能,找到了谷氨酸水杨醛希夫碱钴配合物对环己烯较好的催化氧化反应条件。     

晶格氧用于轻烃的选择氧化

In this paper, selective oxidation of n-butane to maleic anhydride (MA) and partial oxidation of methane to synthesis gas with lattice oxygen instead of molecular oxygen are investigated. For the oxidation of butane to MA in the absence of molecular oxygen, the Ce-Fe promoted VPO catalyst has more available lattice oxygen and provides higher conversion and selectivity than that of the unpromoted one. It is supposed that the introduction of Ce-Fe complex oxides improves redox performance of VPO catalyst and increases the activity of lattice oxygen.For partial oxidation of methane to synthesis gas over LaFeO3 and Lao.8Sro.gFeO3 oxides, the reaction with flow switched between 11% O2-Ar and 11% CH4-He at 900℃ was carried out. The results show that methane can be oxidized to CO and H2 with selectivity over 93% by the lattice oxygen of the catalyst in an appropriate reaction condition, while the lost lattice oxygen can be supplemented by air re-oxidation. It is viable for the lattice oxygen of the LaFeO3 and La0.8Sr0.2FeO3 catalyst instead of molecular oxygen to react with methane to synthesis gas in the redox mode.     

鸡西褐煤碱氧氧化的研究

选用鸡西褐煤 ,在 1 80～ 2 4 0℃下 ,于氢氧化钠和水溶液中用氧气氧化 ,考察了碱煤比、反应温度、氧初压、反应时间及水量对芳香羧酸产率的影响。实验结果表明 ,碱煤比和氧初压是影响芳香羧酸产率的主要因素     

高浓度乙烯液相烷基化研究

乙苯是一种重要的石油化工基础原料,近年来需求增长较快。介绍了液相乙稀烷基生产优质乙苯工艺技术,运用独特的沸石催化剂进行催化,并且运用EBMax技术使其产品更加优质,反应效率提高,对未来开发新型工艺奠定了基础。     

醇类的分子氧催化氧化反应研究进展

目前,国外广泛地使用分子氧(或空气)催化氧化醇类以合成羰基化合物。分子氧是化工生产中很受欢迎的一种“绿色”氧化剂而且便宜易得。此处介绍的是目前国外已发现的多种这类反应的以铂系金属为主的催化剂。它们大多数具有高的催化转化率和很好的选择性。     

高分子担载谷氨酸希夫碱铜配合物催化氧化环己烯研究

研究了高分子担载水杨醛谷氨酸希夫碱配合物（PS-Sal-Glu-M）催化氧化环己烯的性能,详细探讨了反应温度、反应时间、催化剂用量、反应添加剂对高分子担载水杨醛谷氨酸希夫碱铜配合物催化氧化环已烯的反应性能的影响。研究表明,在常压下,用分子氧作作为氧化剂,不需要溶剂及共还原剂,环己烯可以被氧化生成环己烯醇和环已烯酮,产物的分离提纯比较容易,催化剂可以循环使用。     

分子氧/乙醛/过渡金属盐体系氧化环己烯的研究

采用分子氧／乙醛／过渡金属盐催化剂体系氧化环己烯合成环氧环己烷,此方法与传统的有机过氧化物氧化的方法相比,具有安全、简便、高效的特点。通过对影响此反应的过渡金属盐催化剂种类、用量以及反应物配比等主要因素的考察,可使氧化反应产物1,2-环氧环己烷的收率最高可达78．2％。     

Propane Oxidation on MoVTeNbO Mixed Oxide Catalysts: Study of the Phase Composition of Active and Selective Catalysts

Several phases reported as minor or major phases in the active MoVTeNbO catalysts have been prepared and investigated for the oxidation of propane into acrylic acid. Activity and selectivity of pure phases and mixtures of phases obtained either directly from synthesis or by co-grinding have been compared. The results obtained confirmed that the orthorhombic M1 phase is the most active and selective phase and is responsible for the major part of the efficiency of the best catalysts. However, they also clearly demonstrated that a synergism due to a cooperation between phases occurs, similar to that previously proposed between the M1 [(Te₂O)M₂₀O₅₆] and M2 [(TeO)M₃O₉] phases for the ammoxidation of propane. The origin of this phase cooperation is discussed.     

环己烯制备中几种催化剂比较

探索了几种常见催化剂对催化环己醇脱水制备环己烯的催效果。研究了催化剂用量对反应时间、收率等方面的影响,并对实验过程中的现象进行比较,结果表明几种常见固体酸作催化剂催化环己醇脱水制备环己烯时有较的高催化活性,并有较高的收率。可用于教学或工业生产中。     

Kinetics and Active Surfaces for CO Oxidation on Pt-Group Metals Under Oxygen Rich Conditions

This mini review summaries recent works on identifying the active surfaces for CO oxidation on Pd, Pt, and Rh under oxygen rich conditions. A significantly high reaction rate for CO oxidation under oxygen rich conditions has been observed. Results using in situ characterization methods of ambient scanning tunneling microscope, surface X-ray diffraction, ambient pressure X-ray photoemission spectroscopy, X-ray absorption spectroscopy, and infrared reflection adsorption spectroscopy (IRAS), were included. Most X-ray related methods reveal that the achievements of the high reaction rates for CO oxidation on Pd, Pt, and Rh under oxygen rich conditions are accompanied with the appearance of oxides on the surface, leading to that the oxide phase is considered to be the active surface. In contrast, recent in situ IRAS results conclude that a chemisorbed oxygen covered metallic surface is the active surface. Kinetic data support that the reaction on the metallic surfaces can reach the high rate, e.g. a mass-transfer limit turnover frequency, without the necessity of the presence of oxide. Therefore, we point out that the appearance of oxides on Pt-group metals during CO oxidation is possibly due to the transfer-limit of CO gas, resulting in exposing the catalyst surface to an ambient atmosphere much richer in oxygen and thus building-up the oxide. Moreover, photons in X-ray related experiments may aid to overcome the formation barrier of oxide on a chemisorbed oxygen covered metallic surface. The formation of oxide is also affected by the mass-transfer properties of the in situ reaction cells. If the amount of incoming CO molecules under the mass-transfer limit of CO is high enough, the build-up of oxide may be precluded being consumed by reacting with CO.     

A Model for the Phosphorus Dynamics of VPO Catalysts during the Selective Oxidation of n‐Butane to Maleic Anhydride in a Tubular Reactor

A model for the phosphorus dynamics in vanadium‐phosphorus oxide (VPO) catalysts for the oxidation of n‐butane to maleic anhydride was developed. According to the model, reversible sorption processes determine the phosphorus content of the catalyst. Simulations reveal that several phenomena can be successfully described. If no phosphorus is added to the reactant feed, the catalytic activity increases until runaway occurs. With addition of a proper amount of phosphorus, the loss can be compensated while excessive phosphorus addition results in complete catalyst deactivation. Adjusting the model parameters to experimental data may result in a model that can be used to optimize the performance of maleic anhydride reactors.     

Study of Mn-based Catalysts for Oxidative Dehydrogenation of Cyclohexane to Cyclohexene

The gas-phase oxidative dehydrogenation (ODH) of cyclohexane to cyclohexene in the presence of molecular oxygen has been studied over various Mn-based catalysts. It is found that LiCl/MnO_x/PC (Portland cement) catalyst exhibits the highest catalytic performance, and a 42.8% cyclohexane conversion, 58.8% cyclohexene selectivity and 25.2% cyclohexene yield can be achieved under 600 °C, 20,000 h⁻¹ and C₆H₁₂/O₂/N₂=14/7/79. There are good correlations between the selectivities to cyclohexene and the electrical conductivities of Li doped Mn-based catalysts, from which it is deduced that the non-fully reduced oxygen species (O₂⁻, O₂²⁻, O⁻) involved in a new phase of LiMn₂O₄ might be responsible for the high selectivity toward cyclohexene, whereas the Mn₂O₃ crystal phase results in the CO_x formation. The selectivity to cyclohexene increases with increasing molar ratio of Li to Mn in LiCl/MnO_x/PC.     

分子氧氧化环己烯制备环己烯酮

针对分子氧氧化环己烯制备环己烯酮的催化反应体系,以Co(Ⅱ)为活性中心,3,5-二氯水杨醛与邻苯二胺为配体,胺化的MCM-41型介孔分子筛为载体,用化学键联法制备出一种固载型希夫碱催化剂。进而考察了该催化剂对分子氧氧化环己烯制备环己烯酮的工艺条件,结果表明,在常压、催化剂用量0.15 g(2 mL环己烯)、乙腈20 mL、氧气流量5 mL/min、反应温度60℃、反应时间8 h、叔丁基过氧化氢(TBHP)0.04 mL的条件下,环己烯酮的单程收率达54.87%,催化剂容易分离回收,可重复使用。     

重芳烃副产的烷基化及富集均三甲苯的提取

通过实验得出重芳烃副产烷基化反应优惠条件 ,并为均三甲苯的分离创造了有利条件     

活化过程对正丁烷氧化制顺酐钒磷氧系催化剂性能影响的研究

本文在丁烷/空气气氛下,系统地考察了活化过程对正丁烷氧化制顺酐钒磷氧系催化剂性能的影响.活化前后的催化剂用XRD、IR、SEM、EPMA、TEM和比表面进行了较全面地表征,并与催化剂的活性进行了关联.结果表明:活化过程对催化剂相转变、比表面积、表面磷钒比(P/V)等有明显的影响.活化前后催化剂的形貌基本不变.实验证明(VO)_2P_2O_7是正丁烷选择性生成顺酐的活性相.催化剂活性防活化时间的增加而增长,并趋于稳定,但活性诱导期随之缩短.通过研究找到了工业催化剂的适宜活化条件,在该条件下活化的催化剂具有活性高、选择性好、活性诱导期短的特点.     

The Effect of Synthesis Methods on Active Oxygen Species of MnOx-CuO in Soot Combustion

Catalysis Letters - The activity of the catalyst is closely related to the synthesis method. Hereon, we prepared a series of XMn1Cu (X?=?2, 4, 6, 8) catalysts by hydrolysis driven...     

重氮盐芳环上的羟基取代反应研究

报道了对苯二酚、邻/对甲氧基苯酚的合成方法。研究了重氮水解液的酸浓度、水解温度、硫酸铜用量对产物收率的影响。改进了常用的后处理提纯方法,采用了层析柱法分离浓缩产物,研究了不同的脱附剂对产物收率的影响。实验结果表明层析柱分离方法提高了产物收率,并比较分析了不同基团对水解收率的影响。     

环氧环己烷的催化合成研究

采用杂多离子复合相转移催化剂,环己烯为原料、低含量过氧化氢为氧源合成了环氧环己烷,筛选了相转移催化剂,探讨了催化活性物种的生成原理及环氧化反应的作用机制.实验结果表明,双十六烷基二甲基氯化铵和双十八烷基二甲基氯化铵与磷钨杂多离子复配表现出较好的环氧化反应活性;较优的反应条件为:n(Q3[PW4])∶n(C6H10)∶n(H2O2)=1∶200∶130,反应温度50～60 ℃,pH=4.5～5.5,时间1～4 h;环己烯转化率40%～50%,过氧化氢利用率80%～90%,环氧环己烷的收率为80%～86%(扣除回收的环己烯).与传统的环氧化工艺相比,工艺简单、污染少、收率高,工业化可行性强.