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The Adsorption of Nitric Oxide on Supported Co-Mo Hydrodesulfurization Catalysts: A Review 负载型Co-Mo加氢脱硫催化剂对一氧化氮的吸附研究进展
IF 10.9 2区 化学 Q1 CHEMISTRY, PHYSICAL Pub Date : 1995-11-01 DOI: 10.1080/01614949508006452
L. Portela, B. Delmon, P. Grange
Introduction Regulations about maximum sulfur contents of oil fractions and consequent SO, emissions from their combustion are becoming increasingly more stringent. Simultaneously, the oil industry has to deal with oil chargesthat are heavier and have higher concentrations of sulfur-containing compounds, leading to more severe desulfurization conditions. Therefore, catalysts with higher performance in hydrodesulfurization (HDS) are sought in order to cope with these new needs. ∗ Present address: GRECAT—Dep. Eng. Quimica, Instituto Superior Tecnico, Universidade Tecnica de Lisboa, Av. Rovisco Pais, P-1096 Lisboa Codex, Portugal.
关于石油馏分的最大硫含量及其燃烧产生的二氧化硫排放的规定越来越严格。与此同时,石油工业必须处理更重、含硫化合物浓度更高的原油,从而导致更严重的脱硫条件。因此,寻求具有更高性能的加氢脱硫催化剂以满足这些新的需求。*目前地址:great - dep。Eng。Quimica,里斯本科技大学高等技术研究所,Av. Rovisco Pais, P-1096里斯本法典,葡萄牙。
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引用次数: 49
The Mechanism of HDS Catalysis HDS催化机理研究
IF 10.9 2区 化学 Q1 CHEMISTRY, PHYSICAL Pub Date : 1995-08-01 DOI: 10.1080/01614949508006446
A. N. Startsev
Introduction The mechanism of heterogeneous catalytic reactions is much more difficult to elucidate than that of homogeneous systems. Despite the facilities provided by physical methods for investigating the surface of solids, obtaining detailed information on the structure of the active component in real heterogeneous catalysts presents difficulties due to the nonuniform chemical composition of the surface species. Some of these surface species are totally inactive in catalysis, and others can catalyze the given chemical reaction by different pathways and according to different mechanisms. This results in a change of selectivity to the desired product and the appearance of intermediates and reaction by-products. Furthermore, the effect of the reaction medium on the catalyst gains importance during a catalytic process when, at high temperature and pressure, one type of surface species is transformed into another, thus changing the mechanism and direction of the catalyzed reaction. ∗ Telex: 133122 Sovet SU...
非均相催化反应的机理比均相催化反应的机理更难阐明。尽管物理方法为研究固体表面提供了便利,但由于表面物质的化学组成不均匀,获得实际非均相催化剂中活性成分结构的详细信息存在困难。这些表面物质有的完全不具有催化活性,有的则可以通过不同的途径,根据不同的机理催化给定的化学反应。这导致对期望产物的选择性改变以及中间产物和反应副产物的出现。此外,在高温高压催化过程中,当一种表面物质转化为另一种表面物质,从而改变催化反应的机理和方向时,反应介质对催化剂的影响就显得尤为重要。*电传:133122 Sovet SU…
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引用次数: 190
Mechanism of Selective Paraffin Ammoxidation 选择性石蜡氨氧化机理
IF 10.9 2区 化学 Q1 CHEMISTRY, PHYSICAL Pub Date : 1995-08-01 DOI: 10.1080/01614949508006447
V. Sokolovskii, A. Davydov, O. Ovsitser
Introduction Selective ammoxidation of paraffins into corresponding nitriles is of a prime practical significance as it could add to the sources for synthesis of a number of valuable organic products currently produced from oil. On the whole these processes seem to be more promising for commercial synthesis than partial oxidation of paraffins, as nitriles are more stable than corresponding oxy products and a higher yield of the desirable product may potentially be achieved.
石蜡选择性氨氧化生成相应的腈具有重要的实际意义,因为它可以为目前从石油中生产的许多有价值的有机产品的合成增加来源。总的来说,这些方法似乎比部分氧化石蜡更有希望用于商业合成,因为腈比相应的氧产物更稳定,并且可能获得更高的期望产物收率。
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引用次数: 64
Molecular Aspects of Catalytic Reactivity. Application of EPR Spectroscopy to Stuies of the Mechanism of Heterogeneous Catalytic Reactions 催化反应性的分子方面。EPR光谱在多相催化反应机理研究中的应用
IF 10.9 2区 化学 Q1 CHEMISTRY, PHYSICAL Pub Date : 1995-08-01 DOI: 10.1080/01614949508006448
Z. Sojka
Introduction The basic objective of mechanistic studies of real catalytic processes is to dissect the course of the reaction into individual steps; ascertain their sequence; and determine the stoichiometry, structure, and electronic states of active sites and intermediates. The electron paramagnetic resonance (EPR) technique is at present widely used to explore many of these principal aspects of heterogeneous catalysis and surface chemistry. The extreme sensitivity compared to the usual spectroscopic methods is perhaps its most acknowledged advantage and makes EPR best suited to investigate and characterize low-abundance active sites and intermediates appearing during catalytic reaction. Additional information can be drawn from the theoretical analysis of the experimental spin Hamiltonian parameters within the ligand field and from angular overlap or Newman's superposition models as well as by more sophisticated quantum chemical calculations. The purpose of this paper is to show how catalysis benefits fro...
真实催化过程机理研究的基本目标是将反应过程分解为单个步骤;确定它们的顺序;测定活性位点和中间体的化学计量、结构和电子态。电子顺磁共振(EPR)技术目前被广泛用于探索多相催化和表面化学的许多主要方面。与通常的光谱方法相比,极好的灵敏度可能是其最公认的优势,使EPR最适合于研究和表征催化反应中出现的低丰度活性位点和中间体。可以从配体场内实验自旋哈密顿参数的理论分析、角重叠或纽曼叠加模型以及更复杂的量子化学计算中获得额外的信息。本文的目的是展示催化如何受益于…
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引用次数: 56
Heteropoly Acids and Related Compounds as Catalysts for Fine Chemical Synthesis 杂多酸及其相关化合物在精细化工合成中的催化作用
IF 10.9 2区 化学 Q1 CHEMISTRY, PHYSICAL Pub Date : 1995-05-01 DOI: 10.1080/01614949508007097
I. Kozhevnikov
Abstract Catalysis by heteropoly acids (HPAs) and related compounds is a field of growing importance, attracting increasing attention worldwide, in which many new and exciting developments are taking place in both research and technology [1–111, HPAs are polyoxometalates incorporating anions (heteropolyanions) having metal-oxygen octahedra as the basic structural units [ll-141. Among a wide variety of HPAs those belonging to the so-called Keggin series are the most importance for catalysis. They include heteropolyanions (HPANs)
杂多酸及其相关化合物的催化作用是一个日益重要的领域,在世界范围内受到越来越多的关注,在研究和技术上都取得了许多新的令人兴奋的进展[1-111],杂多酸是一种以金属氧八面体为基本结构单元的阴离子(杂多阴离子)的多金属氧酸盐[1 -141]。在各种各样的hpa中,属于所谓的Keggin系列的hpa对催化作用最重要。包括异多阴离子(hpan)
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引用次数: 571
Bubble column reactors and Fischer-Tropsch synthesis 气泡塔反应器与费托合成
IF 10.9 2区 化学 Q1 CHEMISTRY, PHYSICAL Pub Date : 1995-05-01 DOI: 10.1080/01614949508007096
S. Saxena
Abstract Three-phase slurry bubble column reactors have been used extensively in a number of chemical, petrochemical, and biochemical process engineering applications. For the success of these operations and their large scale industrial exploitation, it is essential that their transport and chemical characteristics be adequately understood on a mechanistic basis so that appropriate design criteria and optimum operating conditions can be established. It is the purpose of this review to present such available knowledge in relation to chemical catalytic operations. The mass transfer characteristics, catalytic activity, and mixing patterns of different phases necessitate a detailed understanding of the hydrodynamic behavior and catalyst dispersion in slurry bubble column reactors. The current status of these aspects is presented, discussed, and assessed in this review. Chemical and biochemical reactions are exothermic in nature and hence efficient heat removal devices must be installed in the reactor to prese...
三相浆态泡塔反应器在化工、石化、生化工艺工程中得到了广泛的应用。为了这些作业的成功及其大规模的工业开发,必须在机械的基础上充分了解其运输和化学特性,以便制定适当的设计标准和最佳的作业条件。这篇综述的目的是介绍这些与化学催化操作有关的现有知识。浆液泡塔反应器的传质特性、催化活性和不同相的混合模式需要对浆液泡塔反应器的流体动力学行为和催化剂分散有详细的了解。本文对这些方面的现状进行了介绍、讨论和评估。化学和生物化学反应本质上是放热的,因此必须在反应器中安装有效的散热装置来加热。
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引用次数: 52
Two Catalytic Technologies of Much Influence on Progress in Chemical Process Development in Japan 两种催化技术对日本化工工艺发展的影响很大
IF 10.9 2区 化学 Q1 CHEMISTRY, PHYSICAL Pub Date : 1995-02-01 DOI: 10.1080/01614949508007093
N. Nojiri, Y. Sakai, Yoshihisa Watanabe
Abstract A tremendous number of new catalytic chemical processes have been established and commercialized in Japan in recent years [l, 21. Table 1 shows typical Japanese-made technologies and processes from 1957, about which time the petrochemical industry started in Japan. In those days almost all processes adopted were either fully licensed from foreign companies in Western Europe and the U.S. or completed in Japan as a practical technology using basic and original ones discovered by the foreign companies. In 18 years, from 1957 to 1974, when the Japanese petrochemical industry matured and rapidly magnified its scale, 22 new technologies and processes were accomplished in Japan; however, some of them are not intrinsically Japanese for the reason already mentioned—they derived from foreign companies—and some others were only the first in Japan but not the first in the world. The next 17 years (1975–1992), which included two oil embargoes and were regarded as the time the industry entered the age of a low...
摘要近年来,日本建立了大量新的催化化学工艺并实现了商业化[1,21]。表1显示了1957年以来典型的日本制造技术和工艺,大约在这个时候,日本的石化工业开始了。在当时,几乎所有的工艺都是在西欧和美国完全获得外国公司的许可,或者是在日本利用外国公司发现的基础和原创技术作为实用技术完成的。从1957年到1974年的18年间,日本石化工业日趋成熟,规模迅速扩大,完成了22项新技术和新工艺;但是,由于前面提到的原因,它们中的一些并非本质上是日本的——它们来自外国公司——还有一些只是日本的第一个,而不是世界上的第一个。接下来的17年(1975-1992),包括两次石油禁运,被认为是该行业进入低谷时代的时候。
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引用次数: 27
The Use of Clays for the Hydrotreatment of Heavy Crude Oils 粘土在重质原油加氢处理中的应用
IF 10.9 2区 化学 Q1 CHEMISTRY, PHYSICAL Pub Date : 1995-02-01 DOI: 10.1080/01614949508007091
F. Marcos
Abstract The increasing supply of heavy crude oils is a matter of serious concern for the petroleum industry. In order to satisfy the changing pattern of product demand, significant investments in refining conversion processes will be necessary to profitably utilize these heavy crude oils. Although the most efficient and economical solution to this problem will depend to a large extent on individual country and company situations, the most promising technologies will likely involve the conversion of vacuum bottom residual oils, asphalt from deasphalting processes, and superheavy crude oils into useful light and middle distillate products.
重质原油供应的不断增加是石油工业严重关注的问题。为了满足不断变化的产品需求模式,需要在炼油转化过程中进行大量投资,以利用这些重质原油获利。虽然解决这一问题的最有效和最经济的办法在很大程度上取决于个别国家和公司的情况,但最有前途的技术可能是将真空底渣油、脱沥青过程中的沥青和超重原油转化为有用的轻质和中等馏分油产品。
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引用次数: 24
Oxidant Activation Over Structural Defects of Oxide Catalysts in Oxidative Methane Coupling 氧化甲烷偶联中氧化催化剂结构缺陷上的氧化活化
IF 10.9 2区 化学 Q1 CHEMISTRY, PHYSICAL Pub Date : 1995-02-01 DOI: 10.1080/01614949508007092
E. Voskresenskaya, V. G. Roguleva, A. Anshits
Abstract Different aspects concerning the process of direct methane conversion to oxygen-containing products developed during more than half a century have been considered in previous reviews [1–3]. In particular, Gesser et al. [13 paid most attention to the homogeneous stages in methane conversion, while Foster [2] and Pitchai and Klier [3] examined the effect of different catalysts on methanol and formaldehyde formation. At present the main product of the homogeneous methane oxidation process with oxygen is shown to be methanol formed according to a chain-branching mechanism. In the presence of homogeneous initiators [4] (benzene, 2,2,4- trimethylpentane, etc.) or heterogeneous catalysts [2,3,5,6], formaldehyde is formed together with CH30H. However, the yield of the desirable products is low and does not exceed 8–10%. Charged atomic oxygen forms are considered to take part in the process of catalytic methane oxidation.
半个多世纪以来,关于甲烷直接转化为含氧产品的不同方面已经在之前的综述中得到了阐述[1-3]。其中,Gesser等人[13]主要关注甲烷转化的均相阶段,而Foster[2]和Pitchai和Klier[3]研究了不同催化剂对甲醇和甲醛形成的影响。目前的研究表明,甲烷与氧均相氧化过程的主要产物是根据链分支机理形成的甲醇。在均相引发剂[4](苯、2,2,4-三甲基戊烷等)或非均相催化剂[2,3,5,6]存在下,甲醛与CH30H一起生成。然而,理想产品的收率很低,不超过8-10%。带电原子氧形式被认为参与催化甲烷氧化过程。
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引用次数: 103
The Catalytic Hydrogenolysis of Esters to Alcohols 酯类催化氢解制醇
IF 10.9 2区 化学 Q1 CHEMISTRY, PHYSICAL Pub Date : 1994-11-01 DOI: 10.1080/01614949408013931
T. Turek, D. Trimm, N. W. Cant
Abstract The hydrogenolysis of esters to alcohols is a reaction between esters and hydrogen which selectively splits a C-0 bond adjacent to a carbonyl group (1). A well-known large-scale industrial process based on this reaction the production of fatty alcohols from natural fatty acid esters-has been operated commercially for more than 50 years. Several processes which include the hydrogenolysis of an ester have been proposed for the manufacture of basic chemicals such as methanol and ethanol. Furthermore, there has been continuous interest over the past two decades in replacing the existing, energy-intensive processes for the production of ethylene glycol and 1,4-butanedioI by more cost-effective routes involving ester hydrogenolysis. While particular aspects of the literature on hydrogenolysis of esters have been reviewed already [1–3], the objective of the present work is to give a more general summary with special emphasis on the present or possible industrial applications of ester hydrogenolysis.
酯氢解制醇是酯和氢选择性分裂羰基附近的C-0键的反应(1)。基于该反应的一个众所周知的大规模工业过程——从天然脂肪酸酯中生产脂肪醇——已经在商业上运行了50多年。已经提出了几种方法,其中包括酯的氢解,用于制造基本化学品,如甲醇和乙醇。此外,在过去的二十年里,人们一直对用更具成本效益的酯氢解方法取代现有的生产乙二醇和1,4-丁二醇的能源密集型工艺感兴趣。虽然已经对酯类氢解的特定方面的文献进行了综述[1-3],但本工作的目的是对酯类氢解目前或可能的工业应用进行更全面的总结。
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引用次数: 191
期刊
Catalysis Reviews-Science and Engineering
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