Active Sites in Heterogeneous Catalytic Reaction on Metal and Metal Oxide: Theory and Practice
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Steam Reforming of Lower Alkanes and the Water-Gas Shift Reaction
INVESTIGATION OF ACTIVE SITES AND REACTION NETWORKS IN CATALYTIC HYDROGEN PRODUCTION: STEAM REFORMING OF LOWER ALKANES AND THE WATER-GAS SHIFT REACTION DISSERTATION Presented in Partial Fulfillment of the Requirements for the Degree Doctor of Philosophy in the Graduate School of The Ohio State University By Sittichai Natesakhawat, M.S. * * * * * The Ohio State University 2005 Dissertation Committee: Approved by Professor Umit S. Ozkan, Adviser Professor Jeffrey J. Chalmers Professor David L. Tomasko _________________________ Professor Heather Davis Adviser Graduate Program in Chemical Engineering ABSTRACT Steam reforming (SR) of hydrocarbons and water-gas shift (WGS) are of importance in hydrogen generation technologies due to recent attention focusing on fuel cells. Current research efforts have focused on catalyst development to improve activity, selectivity, and stability under a realistic range of operating conditions. Although coke formation is a major concern for Ni-based catalysts when used for hydrocarbon steam reforming, their low cost and long-proven performance warrants further investigation. Moreover, hydrogen and fuel cell technologies will greatly benefit from innovative high- temperature shift (HTS) catalyst formulations that can overcome some serious drawbacks (i.e., low activity at low temperatures, sintering of magnetite (Fe3O4), a pyrophoric nature, and the harmful effects of Cr6+ on human health). In this Ph.D. study, lanthanide-promoted Ni/Al2O3 catalysts and Fe-based catalysts promoted with first row transition metals were synthesized by a modified sol-gel technique and a coprecipitation method, respectively. The effect of synthesis variables on the catalyst properties (i.e., BET surface area, reducibility, crystallite size, crystal structure, oxidation states, adsorption/desorption behavior, and surface intermediates during the reaction) and, in turn, on the catalytic performance in SR of lower alkanes and ii the WGS reaction has been investigated. -
Opportunities for Catalysis in the 21St Century
Opportunities for Catalysis in The 21st Century A Report from the Basic Energy Sciences Advisory Committee BASIC ENERGY SCIENCES ADVISORY COMMITTEE SUBPANEL WORKSHOP REPORT Opportunities for Catalysis in the 21st Century May 14-16, 2002 Workshop Chair Professor J. M. White University of Texas Writing Group Chair Professor John Bercaw California Institute of Technology This page is intentionally left blank. Contents Executive Summary........................................................................................... v A Grand Challenge....................................................................................................... v The Present Opportunity .............................................................................................. v The Importance of Catalysis Science to DOE.............................................................. vi A Recommendation for Increased Federal Investment in Catalysis Research............. vi I. Introduction................................................................................................ 1 A. Background, Structure, and Organization of the Workshop .................................. 1 B. Recent Advances in Experimental and Theoretical Methods ................................ 1 C. The Grand Challenge ............................................................................................. 2 D. Enabling Approaches for Progress in Catalysis ..................................................... 3 E. Consensus Observations and Recommendations.................................................. -
Process Intensification in the Synthesis of Organic Esters : Kinetics
PROCESS INTENSIFICATION IN THE SYNTHESIS OF ORGANIC ESTERS: KINETICS, SIMULATIONS AND PILOT PLANT EXPERIMENTS By Venkata Krishna Sai Pappu A DISSERTATION Submitted to Michigan State University in partial fulfillment of the requirements for the degree of DOCTOR OF PHILOSOPHY Chemical Engineering 2012 ABSTRACT PROCESS INTENSIFICATION IN THE SYNTHESIS OF ORGANIC ESTERS: KINETICS, SIMULATIONS AND PILOT PLANT EXPERIMENTS By Venkata Krishna Sai Pappu Organic esters are commercially important bulk chemicals used in a gamut of industrial applications. Traditional routes for the synthesis of esters are energy intensive, involving repeated steps of reaction typically followed by distillation, signifying the need for process intensification (PI). This study focuses on the evaluation of PI concepts such as reactive distillation (RD) and distillation with external side reactors in the production of organic acid ester via esterification or transesterification reactions catalyzed by solid acid catalysts. Integration of reaction and separation in one column using RD is a classic example of PI in chemical process development. Indirect hydration of cyclohexene to produce cyclohexanol via esterification with acetic acid was chosen to demonstrate the benefits of applying PI principles in RD. In this work, chemical equilibrium and reaction kinetics were measured using batch reactors for Amberlyst 70 catalyzed esterification of acetic acid with cyclohexene to give cyclohexyl acetate. A kinetic model that can be used in modeling reactive distillation processes was developed. The kinetic equations are written in terms of activities, with activity coefficients calculated using the NRTL model. Heat of reaction obtained from experiments is compared to predicted heat which is calculated using standard thermodynamic data. The effect of cyclohexene dimerization and initial water concentration on the activity of heterogeneous catalyst is also discussed. -
Interstellar Formamide (NH2CHO), a Key Prebiotic Precursor
Interstellar formamide (NH2CHO), a key prebiotic precursor Ana López-Sepulcre,∗,y,z Nadia Balucani,{ Cecilia Ceccarelli,y Claudio Codella,x,y François Dulieu,k and Patrice Theulé? yUniv. Grenoble Alpes, IPAG, F-38000 Grenoble, France zInstitut de Radioastronomie Millimétrique (IRAM), 300 rue de la piscine, F-38406 Saint-Martin d’Hères, France {Dipartimento di Chimica, Biologia e Biotecnologie, Università degli Studi di Perugia, I-06123 Perugia, Italy xINAF, Osservatorio Astrofisico di Arcetri, Largo E. Fermi 5, I-50125, Firenze, Italy kUniversité de Cergy-Pontoise, Observatoire de Paris, PSL University, Sorbonne Université, CNRS, LERMA, F-95000, Cergy-Pontoise, France ?Aix-Marseille Université, PIIM UMR-CNRS 7345, 13397 Marseille, France E-mail: [email protected] Abstract Formamide (NH2CHO) has been identified as a potential precursor of a wide variety arXiv:1909.11770v1 [astro-ph.SR] 25 Sep 2019 of organic compounds essential to life, and many biochemical studies propose it likely played a crucial role in the context of the origin of life on our planet. The detection of formamide in comets, which are believed to have –at least partially– inherited their current chemical composition during the birth of the Solar System, raises the question whether a non-negligible amount of formamide may have been exogenously delivered onto a very young Earth about four billion years ago. A crucial part of the effort to 1 answer this question involves searching for formamide in regions where stars and planets are forming today in our Galaxy, as this can shed light on its formation, survival, and chemical re-processing along the different evolutionary phases leading to a star and planetary system like our own. -
Chemical Process Modeling in Modelica
Chemical Process Modeling in Modelica Ali Baharev Arnold Neumaier Fakultät für Mathematik, Universität Wien Nordbergstraße 15, A-1090 Wien, Austria Abstract model creation involves only high-level operations on a GUI; low-level coding is not required. This is the Chemical process models are highly structured. Infor- desired way of input. Not surprisingly, this is also mation on how the hierarchical components are con- how it is implemented in commercial chemical process nected helps to solve the model efficiently. Our ulti- simulators such as Aspen PlusR , Aspen HYSYSR or mate goal is to develop structure-driven optimization CHEMCAD R . methods for solving nonlinear programming problems Nonlinear system of equations are generally solved (NLP). The structural information retrieved from the using optimization techniques. AMPL (FOURER et al. JModelica environment will play an important role in [12]) is the de facto standard for model representation the development of our novel optimization methods. and exchange in the optimization community. Many Foundations of a Modelica library for general-purpose solvers for solving nonlinear programming (NLP) chemical process modeling have been built. Multi- problems are interfaced with the AMPL environment. ple steady-states in ideal two-product distillation were We are aiming to create a ‘Modelica to AMPL’ con- computed as a proof of concept. The Modelica source verter. One could use the Modelica toolchain to create code is available at the project homepage. The issues the models conveniently on a GUI. After exporting the encountered during modeling may be valuable to the Modelica model in AMPL format, the already existing Modelica language designers. software environments (solvers with AMPL interface, Keywords: separation, distillation column, tearing AMPL scripts) can be used. -
Surface Reactions and Chemical Bonding in Heterogeneous Catalysis
Surface reactions and chemical bonding in heterogeneous catalysis Henrik Öberg Doctoral Thesis in Chemical Physics at Stockholm University 2014 Thesis for the Degree of Doctor of Philosophy in Chemical Physics Department of Physics Stockholm University Stockholm 2014 c Henrik Oberg¨ ISBN 978-91-7447-893-8 Abstract This thesis summarizes studies which focus on addressing, using both theoretical and experimental methods, fundamental questions about surface phenomena, such as chemical reactions and bonding, related to processes in heterogeneous catalysis. The main focus is on the theoretical approach and this aspect of the results. The included articles are collected into three categories of which the first contains detailed studies of model systems in heterogeneous catalysis. For example, the trimerization of acetylene adsorbed on Cu(110) is measured using vibrational spectroscopy and modeled within the framework of Density Functional Theory (DFT) and quantitative agreement of the reaction barriers is obtained. In the second category, aspects of fuel cell catalysis are discussed. O2 dissociation is rate-limiting for the reduction of oxygen (ORR) under certain conditions and we find that adsorbate-adsorbate interactions are decisive when modeling this reaction step. Oxidation of Pt(111) (Pt is the electrocatalyst), which may alter the overall activity of the catalyst, is found to start via a PtO-like surface oxide while formation of a-PtO2 trilayers precedes bulk oxidation. When considering alternative catalyst materials for the ORR, their stability needs to be investigated in detail under realistic conditions. The Pt/Cu(111) skin alloy offers a promising candidate but segregation of Cu atoms to the surface is induced by O adsorption. -
Taking Reactive Distillation to the Next Level of Process Intensification, Chemical Engineering Transactions, 69, 553-558 DOI: 10.3303/CET1869093 554
553 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 69, 2018 The Italian Association of Chemical Engineering Online at www.aidic.it/cet Guest Editors: Elisabetta Brunazzi, Eva Sorensen Copyright © 2018, AIDIC Servizi S.r.l. ISBN 978-88-95608-66-2; ISSN 2283-9216 DOI: 10.3303/CET1869093 Taking Reactive Distillation to the Next Level of Process Intensification Anton A. Kissa,b,*, Megan Jobsona a The University of Manchester, School of Chemical Engineering and Analytical Science, Centre for Process Integration, Sackville Street, The Mill, Manchester M13 9PL, United Kingdom b University of Twente, Sustainable Process Technology, PO Box 217, 7500 AE Enschede, The Netherlands [email protected] Reactive distillation (RD) is an efficient process intensification technique that integrates catalytic chemical reaction and distillation in a single apparatus. The process is also known as catalytic distillation when a solid catalyst is used. RD technology has many key advantages such as reduced capital investment and significant energy savings, as it can surpass equilibrium limitations, simplify complex processes, increase product selectivity and improve the separation efficiency. But RD is also constrained by thermodynamic requirements (related to volatility differences and heat of reaction), overlapping of the reaction and distillation operating conditions, and the availability of catalysts that are active, selective and with sufficient longevity. This paper is the first to provide insights into novel reactive distillation technologies that combine RD principles with other intensified distillation technologies – e.g. dividing-wall columns, cyclic distillation, HiGee distillation, and heat integrated distillation column – potentially leading to new processes and applications. 1. Introduction Reactive distillation (RD) is one of the best success stories of process intensification technology – developed since the early 1920s – that made a strong positive impact in the chemical process industry (CPI). -
Systematic Approach for Chemical Reactivity
SYSTEMATIC APPROACH FOR CHEMICAL REACTIVITY EVALUATION A Dissertation by ABDULREHMAN AHMED ALDEEB Submitted to the Office of Graduate Studies of Texas A&M University in partial fulfillment of the requirements for the degree of DOCTOR OF PHILOSOPHY December 2003 Major Subject: Chemical Engineering SYSTEMATIC APPROACH FOR CHEMICAL REACTIVITY EVALUATION A Dissertation by ABDULREHMAN AHMED ALDEEB Submitted to the Office of Graduate Studies of Texas A&M University in partial fulfillment of the requirements for the degree of DOCTOR OF PHILOSOPHY Approved as to style and content by: ____________________________ ____________________________ M. Sam Mannan Kenneth R. Hall (Chair of Committee) (Member) ____________________________ ____________________________ Mark T. Holtzapple Jerald A. Caton (Member) (Member) ____________________________ Kenneth R. Hall (Head of Department) December 2003 Major Subject: Chemical Engineering iii ABSTRACT Systematic Approach for Chemical Reactivity Evaluation. (December 2003) Abdulrehman Ahmed Aldeeb, B.S., Jordan University of Science & Technology; M.S., The University of Texas at Arlington Chair of Advisory Committee: Dr. M. Sam Mannan Under certain conditions, reactive chemicals may proceed into uncontrolled chemical reaction pathways with rapid and significant increases in temperature, pressure, and/or gas evolution. Reactive chemicals have been involved in many industrial incidents, and have harmed people, property, and the environment. Evaluation of reactive chemical hazards is critical to design and operate safer chemical plant processes. Much effort is needed for experimental techniques, mainly calorimetric analysis, to measure thermal reactivity of chemical systems. Studying all the various reaction pathways experimentally however is very expensive and time consuming. Therefore, it is essential to employ simplified screening tools and other methods to reduce the number of experiments and to identify the most energetic pathways. -
CHEMICAL REACTION ENGINEERING* Current Status and Future Directions
[eJij9iviews and opinions CHEMICAL REACTION ENGINEERING* Current Status and Future Directions M. P. DUDUKOVIC and petrochemical industry provided a fertile ground Washington University for further development of reaction engineering con St. Louis, MO 63130 cepts. The final cornerstone of this new discipline was laid in 1957 by the First Symposium on Chemical HEMICAL REACTIONS have been used by man Reaction Engineering [3] which brought together and C kind since time immemorial to produce useful synthesized the European point of view. The Amer products such as wine, metals, etc. Nevertheless, the ican and European schools of thought were not identi unifying principles that today we call chemical reac cal, but in time they converged into the subject matter tion engineering were not developed until relatively a that we know today as chemical reaction engineering, short time ago. During the decade of the 1940's (not or CRE. The above chronology led to the establish even half a century ago!) a transition was made from ment of CRE as an accepted discipline over the span descriptive industrial chemistry to the conceptual un of a decade and a half. This does not imply that all the ification of reaction processes and reactor types. The principles important in CRE were discovered then. pioneering work in this area of industrial practice was The foundation for CRE had already been established done by Denbigh [1] in England. Then in 1947, by the early work of Frank-Kamenteski, Damkohler, Hougen and Watson [2] published the first textbook Zeldovitch, etc., but at that time they represented in the U.S. -
Surface Models in Heterogeneous Catalysis the Synthesis of Ammonia and the Conversion of Carbon Monoxide
JOURNAL OF CATALYSIS 8, 29-35 (1967) Surface Models in Heterogeneous Catalysis The Synthesis of Ammonia and the Conversion of Carbon Monoxide G. PARRAVANO From the Deparzment qf Chemical and Metallurgical Engineering, University qf Michigan Ann Arbor, Machigan Received November 16, 1966, revised January 16, 1967 The establishment of chemical equilibria between gas and solid catalysts during the synthesis of NH3 and the conversion of CO is considered. Suitable solid-gas equilibrium reactions are discussed. With the correct choice of the rate-controlling step, the equilib- rium surface models are able to reproduce the experimental expressions for the rates of reaction. These models represent a drastic departure from the concept of a fixed, hetero- geneous surface that has been extensively used in the past for the interpretation of the experimental results on the above reactions. The two approaches, however, complement each other and the validity of each one may well be justified under different experimental conditions. Thus, a model may be considered the extension of the other by modification of some of the parameters of the system. Over the past several years many investi- view and it is certainly invalid for relatively gations have been carried out on the catalytic long periods of catalyst operation. It is, synthesis of NH3 and on the conversion of therefore, of interest to consider other CO. The studies have generally been directed possibilities more physically justifiable. toward the understanding of the nature, In this direction it seems particularly properties, and operation of the catalytic important to consider the possibility that surface through the analysis of experimental equilibration reactions between surface and results of reaction rates. -
Chapter 6 – the Structure and Reactivity of Molecules the Structure of Molecules This Is the Golden Age of Instrumentation
Chapter 6 – The Structure and Reactivity of Molecules The Structure of Molecules This is the golden age of instrumentation. Many of the techniques you used in organic lab were used a hundred years ago as the sole method of structure determination. Remember the nucleus has been known for just over 100 years! Beginning in the 1920's and 30's through today, we have seen the invention and the development of many analytical techniques used in structure determination. Infrared, NMR, UV-visible (electronic), and ESR spectroscopies, electrochemistry, X-ray crystallography are the major ones. Sixty years ago, an X-ray crystal structure could be an entire Ph.D. dissertation. Today an undergraduate can frequently solve the same structure in a single afternoon. We will talk about some of these methods later in the chapter. Valence Shell Electron Pair Repulsion (VSEPR) Theory While determining molecular structure is increasingly simple, a simple method of predicting structure is still invaluable. The method of choice is VSEPR theory. You saw this in CHM 211 so we'll only briefly review it. This method is a little different from the book’s and can be found in my general chemistry notes. Movable images of the different shapes can be found at http://science.marshall.edu/castella/chm211/vsepr.html (You will need Java® to view this page. Also you will have to use the Java® control panel to add this site to the secure list.). 1) Draw the Lewis structure of the molecule. 2) Determine the base shape of the molecule by adding the number of atoms bound to the central atom to the number of lone pairs on the central atom. -
Interpreting the Periodic Table – Teacher Page
Name: _____________________ Period: ____ Interpreting the Periodic Table – Teacher Page TEKS 8.5 Matter and energy. The student knows that matter is composed of atoms and has chemical and physical properties. The student is expected to: (C) interpret the arrangement of the Periodic Table, including groups and periods, to explain how properties are used to classify elements; Pre-Teach This is an activity designed to help students demonstrate an understanding of the arrangement of the periodic table. Students should be familiar with how the periodic table is arranged by atomic number, mass, energy levels, groups, periods, reactivity, valence electrons, reactivity etc. through other forms of presentation before completing this activity. A good activity to help construct this information for students would be the Mr. X activity. Differentiation Having students work together on this activity can be beneficial in some instances, but can also hinder student’s recall of the information. This is intended to be a summative assessment for this particular TEK before moving on to another concept. It is recommended that the assignment be modified so that the patterns could be easier to identify by reducing the number of letters on the “hypothetical periodic table” and strategically placing them on the table so they are closer together. Name: _____________________ Period: ____ Interpreting the Periodic Table Examine the hypothetical periodic table shown below. Use this periodic table to answer the questions that follow. B A D E C G F I H 1. Which pair(s) of elements has the same number of valence electrons? _____________________________________________________________ 2. How many valence electrons do they have? _____________________________________________________________ 3.