铁酸镁系列超微粒子催化剂的氧化脱氢反应行为:乙苯和环己烷的氧化脱氢反应

采用四种不同的方法制备了系列铁酸镁超微粒子催化剂，考察了其对乙苯和环已烷的氧化脱氢反应性能，结果表明，（Ｄ）样品具有最佳的乙苯氧化脱氢反应活性：４００℃，Ｏ２／Ｃ６Ｈ５Ｃ２Ｈ５（ｍｏｌ）＝３．０时，乙苯转化率为５０％，苯乙烯选择性为８０％，苯乙烯单收达４０％，催化剂对乙苯氧化脱氢反应的活性随样品的粒径变小而提高；对环已烷氧化脱氢反应则恰好相反，即活性随粒径变小而降低，这种差别归因于反应物分子结构与     

FeZSM－5沸石上乙苯的吸附态及氧化脱氢

ＦｅＺＳＭ－５吸附乙苯前后的ＩＲ、ＸＰＳ、ＥＳＲ及Ｍｏｓｓｂａｕｅｒ谱表明，乙苯分子的侧链和苯环与ＦｅＺＳＭ－５的活性位（以Ｆｅ为中心的结构单元）同时发生配位络合作用，减弱了乙苯分子侧链的α和β位Ｃ－Ｈ键，使其活化，在氧存在下易发生氧化脱氢反应生成苯乙烯．Ｆｅ（Ⅲ）是乙苯氧化脱氢的活性中心，尤其是骨架不饱和配位的Ｆｅ（Ⅲ）对活化乙苯分子起到了关键作用，碱金属平衡阳离子起到了助催化剂的作用．骨架Ｆｅ（Ⅲ）比非骨架Ｆｅ（Ⅲ）具有更高的氧化脱氢活性     

FeZSM-5沸石上乙苯的吸附态及氧化脱氢

ＦｅＺＳＭ－５吸附乙苯前后的ＩＲ，ＸＰＳ，ＥＳＲ及Ｍｏｓｓｂａｕｅｒ谱表明，乙苯分子的侧链和苯环与ＦｅＺＳＭ－５的活性以（以Ｆｅ为中心的结构单元）同时发生配位络合作用，减弱了乙苯分子侧链的α和β位Ｃ－Ｈ键，使其活化，在氧存在下易发生氧化脱氢反应生成苯乙烯，Ｆｅ（Ⅲ）是乙苯氧化脱氢的活性中心，尤其是骨架不饱和配位的Ｆｅ（Ⅲ）对活化乙苯分子起到了关键作用，碱金属平衡阳离子起到了助催化剂的作用，骨架Ｆｅ     

铁硅酸盐分子筛乙苯氧化脱氢催化性能研究Ⅱ．FeZSM－5的酸碱性质和积炭对反应活性的影响

本文应用碱性气体吸附的红外光谱和ＴＰＤ技术研究了ＦｅＺＳＭ－５（Ｆ＿４）的酸性，酸性顺序为：Ｈ－Ｆ＿４＞Ｆｅ＿２Ｏ＿３／Ｆ＿４＞Ｆ＿４原粉＞水热处理的Ｋ－Ｆ＿４＞Ｌｉ－Ｆ＿４＞ＮａＦ＿４＞Ｋ－Ｆ＿４＞ＮａＯＨ／Ｆ＿４，比较了酸强度和积炭对乙苯氧化脱氢性能的影响，以及催化剂酸碱性质与积炭的关系．结果表明，乙苯氧化脱氢反应是在酸碱协同作用下进行的，积炭也参与了氧化脱氢反应，催化剂表面上Ｌ酸中心产生的具有一定Ｃ、Ｈ、Ｏ比的积炭具有高的氧化脱氢活性．碱金属阳离子改性的具有Ｌ酸中心的ＦｅＺＳＭ－５是乙苯氧化脱氢的高活性催化剂。     

乙苯氧化脱氢反应Fex/TiO2的催化性能研究

新型氧化钛负载铁催化剂Fex/TiO2在低温乙苯空气氧化脱氢制苯乙烯反应中具有良好的催化活性。350 ℃,使用Fe7/TiO2催化剂,当Fe的质量分数为7%时,可获得14.6%乙苯单程转化率和99.0%的苯乙烯选择性。通过X衍射、表面吸附、热分析及扫描电镜仪器分析表征,考察氧化钛负载铁催化剂在乙苯低温氧化脱氢反应中的催化作用。350 ℃乙苯可被活化,催化剂活性的高低取决于活性物种Fe(III)的分布状态和质量分数。     

FeZSM－5中不同化学环境的铁上乙苯氧化脱氢制苯乙烯的催化活性

ＦｅＺＳＭ－５中不同化学环境的铁上乙苯氧化脱氢制苯乙烯的催化活性张春雷，吴志芸，阚秋斌（吉林大学化学系，长春１３００２３）关键词ＦｅＺＳＭ－５沸石，铁，化学环境，乙苯，氧化脱氢，苯乙烯，多功能催化剂杂原子引入分子筛，除能调变分子筛的酸性和微孔孔径外，...     

乙苯氧化脱氢反应中铁酸镁,铁酸锌超微粉的催化行为

超微粉铁酸镁、铁酸锌对乙苯氧化脱氢反应具有良好的性能．３００℃时能使乙苯分子活化，３５０℃时实现了对活性氧物种的稳定活化．反应活性氧物种被证明是Ｏ_２~－物种．其中，过量尿素爆炸分解法系本工作首创．由此法制得的Ｄ型样品具有最佳的反应性能．ＥＳＲ分析表明Ｄ型样品的原子配置对称性较差．     

MgO、Al_2O_3、SiO_2催化剂上湿天然气中乙烷氧化脱氢的研究(英文)

研究了ＭｇＯ、Ａｌ２Ｏ３、ＳｉＯ２催化剂对湿天然气中乙烷氧化脱氢反应的影响，发现ＭｇＯ对乙烷脱氢有较好的活性，７００Ｃ时，Ｃ２Ｈ４选择性达４１．８５％，收率达１８．７５％。考察了催化剂酸碱性对反应的影响，适当碱性的催化剂有利于反应的进行，催化剂活性顺序与碱性大小顺序相一致为ＭｇＯ＞Ａｌ２Ｏ３＞ＳｉＯ２。催化剂活性顺序与其晶格氧流动性有顺应关系。     

氧化镍中非化学计量氧在乙烷氧化脱氢中的作用

以纯ＮｉＯ为模型催化剂考察了乙烷氧化脱氢（ＯＤＨＥ）性能，发现非化学计量氧的存在与反应的活性及选择性密切相关．ＴＧＡ研究结果表明，５００℃制备的样品具有ｘ≈６％的非化学计量氧．Ｈ２ＴＰＲ结果表明，非化学计量氧与晶格氧的可还原性明显不同；Ｏ２ＴＰＤＭＳ又把非化学计量氧区分为两个氧物种，Ｏ－２和Ｏ－（或Ｏ２－２）．脉冲试验结果表明，非化学计量氧对ＯＤＨＥ制乙烯是选择性反应的活性氧物种，晶格氧是完全氧化反应的活性氧物种．一旦催化剂中非化学计量氧耗尽并动用晶格氧时，催化剂便有Ｎｉ０生成，表现出自催化性能，使反应活性迅速提高，但产物均为ＣＯ２，ＣＯ，ＣＨ４等完全燃烧或裂解产物．为保持有较高的乙烯收率，反应处于稳态时Ｎｉ必须处于高价态．电导测定结果表明，优良的ＯＤＨＥ催化剂应有Ｐ型半导性．     

铁硅酸盐分子筛乙苯氧化脱氢催化性能研究：II.FeZSM—5的酸碱性质和…

本文应用碱性气体吸附的红外光谱和ＴＰＤ技术研究了ＦｅＺＳＭ－５（Ｆ４）的酸性，酸性为：Ｈ－Ｆ４〉Ｆｅ２Ｏ３／Ｆ４〉Ｆ４原粉〉水热处理的Ｋ－Ｆ４〉Ｌｉ－Ｆ４〉Ｎａ－Ｆ４〉Ｋ－Ｆ４〉ＮａＯＨ／Ｆ４。比较了酸强度和积炭对乙苯氧化脱氢性能的影响，以及催化剂酸碱性质与积炭的关系。结果表明，乙苯氧化脱氢反应是在酸碱协同作用下进行的，积炭也参与了氧化脱氢反应，催化剂表面上Ｌ酸中心产生的具有一定Ｃ、Ｈ、Ｏ比的积炭     

Tantalum-containing catalysts for oxydehydrogenation of hydrocarbons and alcohols

The first methods were developed for introducing tantalum(V) into Mg-Al hydrotalcites, which are precursors of oxide catalysts for oxydehydrogenation of hydrocarbons and alcohols. Samples of oxide tantalum(V)-containing catalysts were synthesized. Their catalytic properties were studied in the oxydehydrogenation of ethane to ethylene and ethylbenzene to styrene, oxydehydrocyclization of octane to ethylbenzene and styrene, and oxydehydrogenation of sec-butanol to ketone (octan-2-one). The transformation of ethane to ethylene over the tantalum-containing catalyst occurs with a high selectivity (92–97%) at relatively low temperatures (500°C), and the catalyst is quite efficient in conversion of ethylbenzene to styrene, dehydrocyclization of n-octane to ethylbenzene and styrene, and oxydehydrogenation of sec-butanol to octan-2-one. Comparison with a niobium-containing catalyst showed that it ensures higher yields and selectivities in similar reactions than its tantalum-containing analogue does.     

Niobium-containing catalysts for oxydehydrogenation of hydrocarbons and alcohols

The first methods are developed for introducing niobium(V) into Mg-Al hydrotalcites used as precursors of oxide catalysts for oxydehydrogenation (OD) of alkanes and alcohols. Samples of niobium(V)-containing oxide catalysts are synthesized. Their catalytic properties are studied in oxydehydrogenation of ethane and ethylbenzene to styrene, oxidation dehydrocyclization of octane into ethylbenzene and styrene, and oxydehydrogenation of sec-butanol to ketone (octane-(2)-one). It is ascertained that ethane transformation into ethylene is highly a selective highly process (92–97%) at low temperatures (450–500°C) in the presence of a niobium-containing catalyst; the catalyst is appreciably efficient in ethylbenzene transformation to styrene and dehydrocyclization of n-octane to ethylbenzene and styrene, and in oxydehydrogenation of secbutanol to octane-(2)-one. All the catalysts studied operate stably in OD reactions; no decrease in their activity or selectivity was detected after 50 h operation.     

Oxydehydrogenation of ethylbenzene to styrene on a P?Ni?Mn based catalyst

The oxydehydrogenation of ethylbenzene to styrene over a P−Ni−Mn catalyst, has been studied in the range of 650–770 K. The kinetic behavior of the main reaction can be described by a redox type model and the oxidation of styrene with a power law. The model predictions are in good agreement with the experimental observations.     

镧-镍复合氧化物纳米微粒的固相合成及其催化性能

The La-Ni complex oxide catalyst was prepared by solid state reactions under microwave. The structure and reducibility of the catalyst were characterized by using TG-DTA, XRD, TEM and TPR methods. At the same time the catalytic activity of oxidative dehydrogenation of ethylbenzene to styrene with carbon dioxide over the complex oxide nanoparticle was investigated.The Results show that the product is K2NiF4 nanoparticles,and the size is 13nm.The complex oxide sample had high activity for the oxidative dehydrogenation of ethylbenzene to styrene.     

神华煤流化床气化带出细粉的粒径分离及分离后细粉的CO_2气化特性研究

按粒径将神华煤流化床气化带出细粉(简称细粉)依次筛分为七个组分。采用工业分析仪、元素分析仪、热重分析仪、X射线粉末衍射仪、物理吸附仪等对各组分细粉的基本物化特性、CO2恒温和程序升温气化行为进行了考察。在此基础上,对气化活性差异及其原因进行初步探索。结果表明,细粉经历部分气化后,由于挥发分的析出,细粉的固定碳含量较原煤高,但较相应半焦低。细粉的粒径分布范围较宽,呈近似"M"形分布。随细粉粒径减小,灰分含量增大,而含碳量减少。CO2恒温气化与程序升温气化获得的气化反应活性顺序一致:均随细粉粒径的减小先逐渐降低而后又逐渐升高。不同细粉气化反应活性的差异与其自身的石墨化程度及灰分含量有关,而在研究实验条件下与孔径结构关系不大。     

乙苯脱氢氧化铁系催化剂的活性相及钾的助催作用

与机械混合法相比,用KOH水溶液浸渍法制成的K_2O-Fe_2O_3催化剂性能较佳。负载型多元催化剂的性能与C-64I相近。SEM、XPS和EDAX证实,经使用后,上述负载型多元催化剂表面形态明显改变,表面铁/钾原子比上升。连续升温XRD证实,在乙苯脱氢通常所采用的温度区间,载于表面的KOH会迅速和氧化铁相互作用生成K_2Fe_2O_4。本文认为K_3Fe_2O_4可能是活性相并据此对实验结果作出较为合理的解释。     

Dispersion copolymerization of styrene and glycidyl methacrylate in polar solvents

Monodispersed copolymer microspheres consisting of styrene and glycidyl methacrylate have been prepared by dispersion polymerization. The effects of various polymerization parameters on the particle size and size distribution were systematically investigated. The initial solubility parameter of the system had a significant effect on the final particle size and size distribution. With decreasing initial solubility parameter, the particle size increased and the size distribution broadened. The particle size decreased with increasing stabilizer concentration, the amount of styrene in the monomer mixture, and decreasing initiator concentration. Received: 30 September 1998 Accepted in revised form: 10 December 1998     

Effect of structural stress on the intercalation rate of kaolinite

Particle size in kaolinite intercalation showed an inverse reactivity trend compared with most chemical reactions: finer particles had lower reactivity and some of the fine particles cannot be intercalated. Although this phenomenon was noted in the early 1960s and several hypotheses have been reported, there is no widely accepted theory about the unusual particle size response in the intercalation. We propose that structural stress is a controlling factor in the intercalation and the stress contributes to the higher reactivity of the coarser particles. In this study, we checked the structural deformation spectroscopically and indirectly proved the structural stress hypothesis. A Georgia kaolinite was separated into nine size fractions and their intercalations by hydrazine monohydrate and potassium acetate were investigated with X-ray diffraction (XRD) and Fourier-transform infrared (FTIR) analyses. The apical Si-O band of kaolinite at 1115 cm(-1) shifted to 1124 cm(-1) when the mineral was intercalated to 1.03 nm by hydrazine monohydrate, and its strong pleochroic properties became much weaker. Similar reduction in pleochroism was observed on the surface OH bands of kaolinite after intercalation. Both the bending vibrations of the inner OH group at 914 cm(-1) and of the surface OH group at 937 cm(-1) shifted to 903 cm(-1) after intercalation by hydrazine. A new band for the inner OH group appeared at 3611 cm(-1) during the deintercalation of the 1.03 nm hydrazine kaolinite complex. Pleochroism change in the apical Si-O band suggested the tetrahedra had increased tilt with respect to the (001) plane. The tilt of the Si-O apical bond could occur only if the octahedra had also undergone structural rearrangement during intercalation. These changes in the octahedral and tetrahedral sheets represent some change in the manner of compensation for the structural misfit of the tetrahedral sheet and octahedral sheet. As the lateral dimensions of a kaolinite particle increases, the cumulative degree of misfit increases. Intercalation breaks the hydrogen bonds between layers and allows for the structure to reduce the accumulated stress in some other manner. The reversed size effect on intercalation probably was not caused by crystallinity differences as reported in the literature, because the Hinckley and Lietard crystallinity indices of the four clay fractions were very close to each other. Impurities, such as dickite- or nacrite-like phases are not significant in the studied sample as suggested by the XRD and IR results, they are not the main reasons for the lower reactivity of the finer particles.