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Trends in catalysis research PDF

195 Pages·2006·26.173 MB·English
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CONTENTS .. Preface .tll Chapter I Application of Plasma-Catalyst Hybrid Processes for the Control ofNOx and Volatile Organic Compounds I Hyun-Ha Kim. Atsuslti Ogata and Shigem Futamura Chapter 2 Hydrotalcites as Potential Catalysts for Hydroxylation of Phenol S Kannan Chapter 3 Cluster Model Approach in Catalysis Research A nihal Sien·aa/ra Chapter 4 Recent Inquiries into the Mechanisms of Mctai-Salen Catalyzed Asymmetric Oxidations ill Konstantin P. Bn,liakov and Evgenii P. Talsi Chapter 5 Utilization of Methane in the Catalytic Methylation of Aromatics and Coal Liquefaction over Zeolite Catalysts .Moses 0. Adehajo and Rm' L. Frost Chapter 6 Transient Reaction Analysis of an Automotive Catalyst on a Millisecond Time Scale Yoshiyuki Sakamoto. Tomoyoshi Motohiro, Kohei Okumura, Yoshimi Kizaki and Hirofiuni Shinjoh Index ill TRENDS IN CATALYSIS RESEARCH on• T h1• Ill M 11enal hron1cmy prawem autorskun PREFACE The chemical or biological process whereby the presence of an external compound, a catalyst, serves as an agent to cause a chemical reaction to occur or to improve reaction performance without altering the external compound. CataJysis is a very irnponant process from an industrial point of view since the production of most industrially imponant chemicals involve catalysis. Research into catalysis is a major field in applied science, and involves many fields of chemistry and physics. The new book brings together leading research in this vibrant field. Nonthemlal plasma (NTP) is gathering anentions as a powerful tool to induce various chemical reactions at atmospheric pressure and room temperature. The application fields of NTP processing include air pollution control, sterilization, surface modification, optical application. instrumental analysis, water treatment, ozone generation, fuel refom1ing and so fonh. Despite the long history of electrical corona discharge, its application to air pollution is relatively a new field. Chapter I describes the historical development and up-to-date evaluation of the NTP technology for the removal of NOx and volatile organic compounds (VOCs). Especially, this chapter focused on the culling-edge technology of hybrid NTP process, which combines NTP with various types of catalysts to improve energy efficiency and the reaction selectivity. Historical landmark in the development of NTP technology and current state-of-an technology of plasma-catalyst hybrid processes for the removal of NOx and VOCs arc discussed. Hydrotalcites are two dimensional layered materials. are receiving increased auention in recent years for their diverse applications like catalysts, supports, ion-exchangers, additives and precursors for multi-component catalysts. StructuraJiy. these materials can be perceived 2 by starting with brucite (Mg(OHh) structure wherein, a partial substitution of Mg by a ' 3 trivalent metal ion, say Al occurs and the resulting excess positive charge of the sheets are +, compensated by anions, which occupy the interlayer positions along with water molecules. The genera.! formula of these materials can be represented as [M(IT) .,M(Ill)x(OH)2] [A •· 1 llln].mHzO where M(H), M(JII) and A arc bivaJcnt metal ion, trivalent metaJ ion and interlayer anion and 'x' can usually have values around 0.2-0.4. The wide maneuverability of these layered materials by incorporating a gamut of varied metal ions and incorporation of any anions irrespective of their size and charge gives enonnous scope for tailoring these materials for specific applications. 1n chapter 2, an overall view of these materials including their synthesis and characterization and subsequently how these materia.ls are exploited for 'vtatenal chron1ony prawefll autorskun Lawrence I'. Bevy VIII selective hydroxylation of phenol, one of the industrially important reactions, to dihydroxybenzenes wiU be given. This chapter encompasses background of these materials, synthesis of specific materials, characteri.zation of them and their catalytic behavior. An attempt also will be made wherever possible for Slructure-activity relations. A travel wherein the catalytic behavior will be journeyed through different classes of hydrotalcites namely binary and ternary hydrotalcites with specific metal ions (bivalent, trivalent and tetravalent metal ions) in brucite-like sheets and analyz·ing 1he merits and demerits of them to derive broader conclusions. In this journey, influence of synthesis methodology wiiJ also be traversed to bring out its importance. A future scope of utilizing these materials for such cataly1ic seleclive oxida1ion reactions will be summarized. Chapter 3 presents a brief guide on the applica1ion of the cluster model approach to the invcsligation in the catalytical area. First, it describes the underlying theory, followed by the discussion of some recent examples. Since the clus1er model approach is founded on the existence of local phenomena, section 2 presents an introdu.ction on this important concept. In order 10 describe local phenomena, different calcula1ion strategies may be employed. Section 3 briefly describes the most common among these slratcgics. Finally, section 4 presents some examples on hydrodcsulphurizalion (HDS), supported/exchanged zeolite catalysts and other intcres1ing catalytic systems. This chapter does no intend to be an exhaustive review of the field of the cluster model approach. It is a introductory vison about the use of ab initio calculations, in the area of the cluster model approaches to model catalytic phenomena, and includes successes as well as failures and/or drawbacks of these methods. Since 1990s, metal-salen catalyzed asymmetric oxidations became very popular, so that Ill . the Jacobsen's Mn (salen)CI complex was named Fluka Reagent of the year 1994. The 111 Katsuki-Jacobsen Mn (salen)CI catalyzed cpoxidation of unfunctionalized olefms probably attracted the greatest attention among the chiral metal-salen catalytic systems. Any information on the intermediates could be of practical value for deeper understanding of the catalytic action of the system as well as could contribute to fundamental knowledge on oxidation reactions. In chapter 4, the authors present recent mechanistic studies of 111 [Mn (salen)CI] catalyzed oxidations of unfunctionalized olefins. It was shown that different intermediates operate in these systems depending on the terntinal oxidant used: manganese(lll) acylperoxo complex [Mn111(salen){00C0Aryl)] with m-chloroperoxybenzoic 2 acid (m-CPBA) and d low-spin oxomanganese(V) complex [Mn vO(salen)L] with iodosobcnzcnc (PhlO). Also, an anti ferromagnetically coupled binuclear manganese J.I·OXO 1 1 cr (IV) species of the type [(salen)LMn vOMnv(salen)L ') (L, L'= or PhlO) acting as a reservoir of the active species were detected. These results are compared with those obtained for [Crm(salcn)CI] catalyzed asymmetric oxidations of olefins by PhiO. The active intermediate of these systems was detected and identified as [CrvO(salen)L] (where L= Cl- or a solvent molecule). A reservoir of the active species in this system was also found to exist as 111 a mixed-valence binuclear species [L(salen)Cr 0Crv(salen)L') (L, L'= Cr or solvent molecules). The high-valence Cr complexes are in equilibrium and their ratio can be affected by addition of donor ligands (DMSO, DMF, H 0). The third class of systems to be discussed 2 here appeared in the last years, reflecting the growing need in simple and non-toxic systems 111 for suliide oxidation. Chinll [Fe (salen)CI] complexes were synthesized and used as catalysts for asymmetric oxidation of several alkylar:yl sulfides with PhJO. Surprisingly, the reactive intermediate in this system was found different from those detected in Mn-salen and Cr-salen Mate11al chroniony prawem autorsk1m . Pre lace IX based catalytic systems. Namely, the intermediate was shown to be an iodosylbenzene iron(lll)(salcn) complex similar to iodosylbenzene-iron(lll) porphyrin intermediates recently discussed in the literature. The data obtained are analyzed to understand some catalytic properties of these systems. The present world reserves of natural gas that contain mainly methane are still underutilized due to high cost of transportation. Considerable interest is therefore presently shown in the conversion of methane to transportable liquids and feedstocks in addition to its previous sole use for heating purposes by combustion. One possible new route for the utilization of methane de.rived from natural gas or other sources for conversion to more valuable higher hydrocarbons is the methylation of aromatic hydrocarbons. Chapter 5 provides a general overview of the work that has been done so far on the use of methane for catalytic methylation of model aromatic compounds and for direct liquefaction of coal for the production of liquid hydrocarbons. The chapter is especially focused on the use of both acidic and basic zeolites in acid-catalyzed and base-catalyzed methylation reactions. respectively. The base-catalyzed methylation reaction covered in this discussion is mainly the oxidative methylation of toluene to produce ethylbenzenc and styrene. This reaction has been found to occur over basic sites incorporated into zeolites by chemical modification or by changing the electronegative charge of the zeolite framework. There are two key points to develop an excellent purification system for automotive exhaust gas. The first one is to analyze the transient reactions of the catalyst_ because the components of automotive exhaust gas are not stable during the engine operation and an aggrcssi\le- usage of the transient reactions is considered to be one of the items to overcome strict regulations of automotive exhaust gas. The second is to design the catalyst synthesized by e.ach of nano materials. Chapter 6 studies an automotive catalyst from the above points, lhe have developed a new apparatus: time-resolved time-of-flight mass spectrometry with author~ molecular-pulse-probes for analysis of dynamic processes in surface catalytic reactions on a millisecond scale (TMPRAS; TM+). The method using TM+ enable us analyze a transient reaction of a catalyst under the high-pressure condition. which is simulated actual automotive exhaust gas on a millisecond time scale. It is possible for TM+ to measure catalysis reactions both of an actual usage catalyst and of a model catalyst. This method can bridge the gap between surface science and an actual catalyst, what can be called pressure gap and material gap. Firstly, TM+ is described from the viewpoints of the vacuum system and signal processing. Secondly, some examples arc shown as follows; CO oxidation on a platinum lilm. an oxygen storage reaction on a slurry-coated catalyst. oxygen isotopic exchange reaction on a Pt/ A 10 pellet sample and NO decomposition on a precious metal electrode. 1 3 'vtatenal chron1ony prawefll autorskun In: 'J rends ln Catalysts Research lSHN 1-59454-659-2 Editor: Lawrence P. Bevy, pp. 1-50 © 2006 Nova Science Publishers, Inc. Chapter 1 APPLICATION OF PLASMA-CATALYST HYBRID PROCESSES FOR THE CONTROL OF NOX AND VOLATILE ORGANIC COMPOUNDS Hyun-Ha Kim', Atsushi Ogata and Shigeru Futamura National Institute of Advanced Industrial Science and Technology (AIST) AIST Tsukuba West, 16-1 Onogawa, Tsukuba, lbaraki 305-8569, Japan ABSTRACT Nonthennal plasma (NTP) is gathering attentions as a powerful tool to induce various chemical reactions at atmospheric pressure and room temperature. The application fields of NTP processing include air pollution control. sterilization, surface modification, optical application, instrumental analysis, water treatment, ozone generation, fuel reforming and so forth. Despite the long history of electrical corona discharge, its application to air pollution is relatively new field. This chapter describes the historical development and up-to-date evaluation of the NTP technology for the removal of NOx and volatile organic compounds (VOCs). Especially, this chapter focused on the cutting edge technology of hybrid NTP process, which combines NTP with various types of catalysts to improve energy efficiency and the reaction selectivity. Historical landmark in the development of NTP technology and currcm state-of-an technology of plasma catalyst hybrid processes for the removal of NO.r and VOCs are discussed. Keywords: nonthermal plasma (NTP); catalyst; dielectric-barrier discharge; plasma-driven catalysis; pulsed corona discharge; air pollution; VOCs; NOx I. INTRODUCTION . . There are a number of problems facing mankind today such as ever-mcreasmg population, global warming, rapid urbanization/industrialization many developing 111 • E-mail: [email protected] Tel: +81-29-861-8061 Maknal chromony prawel" autorskrm 2 Hyun-Ha Kim, AtSushi Ogata and Shigeru Futamura countries, ozone layer depletion in the stratosphere, climate changes and desertification etc. In more recent rimes, concern about the atmospheric pollution has widened to include damages to buildings and materials, forestS, agricultural products and even the stratosphere. Especially recent pollution problems are not confined to regional ones any more because of the long distance transportation over the border. The need for bener quality is also emphasized for the indoor air since most people spend more than 90% of times indoor environment. The public's concern about the qualiry of environment keeps increasing every year. The emission regulations for the hazardous chemical compounds all the more stringent in many b~ome countries. There are two major approaches for the pollution prevention. One is the source reduction and the other one is end-of-pipe treauncnt. Although the source reduction is an environmental friendly solution for the control of pollutant emission. this approach alone cannot meet the regulaLion in most cases. It is therefore necessary to develop cost-efficient end-of-pipe treatment with high performance. Among the various air pollution control techniques, two important technologies discussed in this chapter are nonthermal plasma (NTP) and catalyst. Catalyst technology has been used in many industrial fields such as oil chemistry, pollution control, chemical synthesis, etc. Environmental application of catalytic technology has been started in the 1970s mostly for the cleaning of exhaust gas from cars. The catalyst technology used in the environmental protection field is also referred to as environmental catalytic process. Three-way catalyst (TWC), for exan1ple Pt-Rh-Ce0 , is one of representative environmental catalysts. The 2 progress of industry requires further enhancement of catalytic perfonnance. One example is the need for new catalyst capable of controlling NO.r emission from lean-bum engine. The application of NTP to environmental problems and to green chemistry is emerging fields that offer unique opportunities for advancement. The history of NTP to the environmental protection has more than I 00 years experience, mostly for the ozone generation in the water treatment facilities. Early studies on the NTP application for air pollution control started in 1970s, and gathered a considerable attention in the 1980s. Through the extensive research and development (R&D) effortS by many research groups in many countries, significant progress has been made during the last two decades. There also have been some review articles and books both on the fundamental, historical development and on the engineering of asp~tS NTP [ 1-8]. The purpose of this chapter is to provide the historical development and the recent R&D activities of the atmospheric-pressure nonthermal plasmas as an end-of-pipe treatment technology for the abatement of hazardous air pollutants. The major gas-phase air pollutants dealing with in this chapter include NOx, volatile organic compounds (VOCs), and particulate mauers (PMs) from diesel engine. Especially, this chapter deals with the combined system of NTP and catalyst, which takes advantage of a synergy of both technologies. The rype of the hybrid systems varies quite wide range depending on the configuration, types of catalyst and plasmas. The classification of combination, basic structure, the working principle of the each system, historical development of NTP, current achievement and future prospects will be presented. Malena! chroniony prawer- autorskun Application of Plasma-Catalyst Hybnd Processes for the Control of NOx . . . 3 2. ENVIRONMENTAL PROBLEMS RELATED TO NOX AND VOCS 2.1. Photochemical Smog Two well-known air poiJutants of NOx and VOCs are highly correlated each other in terms of photochemical smog. As one can see from the LA smog accident, this photochemical smog mostly occurs in urban areas. Three key factors in the formation of photochemical smog arc NOx, YOCs and the presence of suo light (mostly UV). Photochemical reactions between NOx-VOCs produce peroxyacyl nitrates (PANs), ozone, aldehydes and so on. which arc highly irritating chemicals. PANs arc now recognized to be ubiquitous in polluted urban atmosphere [9]. Ozone was found to be a major component of photochemical smog. YOCs arc emiued mostly from the industrial activity such as the use of solvent, petroleum industry, combustion etc. Most of YOCs arc known to as carcinogen or suspected carcinogen. Definition of YOCs differs from countries. For example, U.S.A clean air act defines YOCs as "a chemical compounds that can be a precursor of photochemical smog". EU defmes YOCs based on its vapor pressure (larger than 0.0 I kPa at 293.15K). However, the main purpose of YOCs emission regulations is to reduce photochemical smog by controlling the emission of VOCs. The technical term of "photochemical smog" was coined by the early works of Haagen-Smit in 1950s to find the reason of eye irritation complaint in Los Angeles area [I OJ. They found that the maio eye irritating chemical was ozone. Later on studies revealed the presence ofN0 and peroxyacetyl nitrate (PAN) together with ozone. 2 Anthropogenic emission sources of NOx are mostly related to the combustion processes such as industrial boiler. car engine. coal-oil fired power plant etc. Jn the flue gases from combustion process including engine, NOx is mostly emitted as NO(> 95%). Car engines arc the main source of NOx in urban area. which is highly related to the photochemical smog problem. The overall mechanism of photochemical smog formation together with their line in the atmosphere is illustrated in Figure I. Generally speaking, photochemical smog is a result of consecutive chain reactions involving atoms and free radicals. Chain initiation step in the photochemical smog is the photolysis of molecules (N0 0 aldehydes etc.), resulting in the 2, 3, formation of free radicals. NOx is initially emitted into the atmosphere as NO, and then slowly converted to N0 via R I. In daytime the produced undergoes photolysis, R2. to 2 N~ form NO and ground state atomic oxygen, oeP) . The photolysis ofN02 has a quantum yield of unity at wavelengths below 370 nm. (R I) N02 + hv (!.< 420om)-+ 2NO + oeP) (R2) (R3) (R4) 'vtatenal chron1ony prawefll autorskun 4 Hyun-Ha KJm, Atsushi Ogata and Sh1geru Futamura I -'o~ / I ' Photochemical oxidants RCO RCHO OH .-· RC(0)0 2 I RO NO RC(O)O RO, R t----. - OH / VOCs VOCs NO Acid rain 00 00 00 co 00 00 Figure I. Photochemical smog fom1ation in the atmosphere (R: alkyl radical, RO: alkoxy radicaL RCO: acyl radical. R0 2: Pcroxyalkyl radical. RCOO~: Acylperoxyl radical) The atomic oxygen recombines with oxygen molecule to form ozone. In lhe absence of VOCs, produced ozone reacts with NO and a steady-state is achieved in which the ozone concentration is given as follows. ( I ) This successive reactions of R2- R3 called as a shon-term NOx-cycle, and there is no significant 0 3 build-up. When lhe VOCs are present in the atmosphere, however. various radicals of hydrocarbons are produced. The OH radical-hydrocarbon reaction plays dominant role in most cases, and ozone and N0 radical for olefins chemistry. Especially. oxidative 3 decomposition of VOCs produce some peroxy radicals of peroxyalkyl radical (R0 2), acylperoxy (RC(0)0 radical and hydorperoxyl radical (H0 which are the chain carriers i.n ) ), 2 2 lhe conversion of NO to N0 This process involving peroxy radicals provides new palhway • 2 for the conversion of NO to NOz not involving OJ and resulting in the accumulation of ozone. (RS) NO + RO, -+ N0 + R0,,. (R6) 2 1 These NO oxidation processes by peroxy radicals play very imponant role in the NOx removal using the NTPs. Formation of PAN is also one of chain termination reaction between peroxyacetyl radical (RC(O)Oz) radical and NOz. Maknal chromony prawe!" autorsk1r1

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