Designing Electric Field Assisted Catalytic Reactors for Hydrogen

Total Page:16

File Type:pdf, Size:1020Kb

Designing Electric Field Assisted Catalytic Reactors for Hydrogen DESIGNING ELECTRIC FIELD ASSISTED CATALYTIC REACTORS FOR HYDROGEN PRODUCTION APPLICATIONS By JAKE T. GRAY A dissertation submitted in partial fulfillment of the requirements for the degree of DOCTOR OF PHILOSOPHY WASHINGTON STATE UNIVERSITY The Gene and Linda Voiland School of Chemical Engineering and Bioengineering DECEMBER 2019 © Copyright by JAKE T. GRAY, 2019 All Rights Reserved © Copyright by JAKE T. GRAY, 2019 All Rights Reserved To the Faculty of Washington State University: The members of the Committee appointed to examine the dissertation of JAKE T. GRAY find it satisfactory and recommend that it be accepted. Su Ha, Ph.D., Chair Norbert Kruse, Ph.D. Jean-Sabin McEwen, Ph.D. M. Grant Norton, Ph.D. ii ACKNOWLEDGMENT This dissertation would not have been possible without the assistance of a great many people—far too numerous to name, and many of whom I do not know. Let the rudimentary list that follows suffice, and accept my sincerest apologies for anyone inadvertently overlooked. I first gratefully acknowledge my funding sources, without whom this research would only have been an idea. Most of the work presented in this dissertation had its beginnings in my project as an undergraduate, which was financed in part by the DeVlieg Foundation and many of the supplies and equipment used throughout this dissertation were obtained through their generosity. The National Science Foundation Graduate Research Fellowship Program (NSF-GRFP Award #1347973) contributed to most of the rest of this work by directly supporting me as a researcher. Without this aid, I would not have been able to focus on research. Additional funding from the Korea Institute of Energy Research and from the U.S. Office of Naval Research helped to purchase more supplies and equipment as the research progressed and allowed the project to expand through collaboration with the Navy Undersea Research Program. The intellectual input of my committee drove this research forward: I thank Drs. Su Ha, Norbert Kruse, Jean-Sabin McEwen, and Grant Norton for their academic assistance, advice, and general support. I’d like to extend additional gratitude to Drs. Ha and Norton for their assistance in preparing my NSF-GRFP and Graduate Research Internship Program (GRIP) application packages. I gratefully acknowledge the involvement of numerous collaborators over the years: Dr. Fanglin Che for her detailed and insightful density functional theory support which was the progenitor of much of my work, and supplemented much of the rest; Kriti Agarwal for her iii assistance with the electrical engineering aspects of this research and COMSOL modeling work; Dr. John Izzo for his support and guidance while working at the Naval Underseas Warfare Center which helped to expand the project in new directions; and to the undergraduate students who worked closely with me to adapt new materials for this application: Matt Sundheim and Derek Burnett. Without our lab and office facilities and equipment and the people responsible for holding it all together, none of this research would have been possible. Although I am immensely grateful to the entirety of the WSU faculty and staff for their role in maintaining our facilities, I would like to recognize certain people specifically: Jim Pogue, Jennifer Starks, and Nicole Leavitt for always putting up with my complicated schemes, ordering my equipment and supplies, and recovering my travel expenses; Jo Ann McCabe for helping navigate the twisted labyrinth that is university finances; Burton “Billy” Schmuck for looking out for our safety and the safety of the community; Kate Konen for her patient help with all things technological (even if it was usually just a button we forgot to press); Samantha Bailey for taking care of the crucial behind-the-scenes bureaucratic headaches of graduate school; and to Valerie Lynch-Holm and Daniel Mullendore at the Francesci Microscopy and Imaging Center for training, advice, and keeping the microscopes in excellent condition despite the hordes of inconsiderate graduate students always fiddling with them. To my group members, past and present, I thank you for companionship both inside and outside the lab. Thanks for making graduate school slightly more tolerable: Xiaoxue “Christy” Hou, Shuozhen Hu, Tsai Garcia-Perez, Bita Khorasani, Parissa Ziaei, Qusay Bkour, Kaytee Villafranca, Xianghui “John” Zhang, Kai Zhao, Oscar Marin-Flores, Martinus “Martin” Dewa, iv Wei-Jyun “Will” Wang, Yilin Liu, and Mohamed “Mo” Elharati. I wish you all success and happiness wherever your paths may lead. To my friends outside the lab, thanks for helping keep me grounded and limiting the amount of time I spend thinking about research. I especially thank Justin Jurgerson for being an entertaining conversationalist, formidable board game adversary, and delightful dinner guest. For my family I am eternally grateful. You have supported me since childhood and I wouldn’t be half the man I am today without you. My mother, Corrina Gray; brother Aric Gray (and his wonderful wife, Jackie Gray); sister Caitlin Gray; and all of my grandparents: Sam and Debbie Duncan and Kent and Susan Gray. Although they are no longer here to appreciate it, I also acknowledge the family I lost during my graduate journey: my great-grandmother Edith Curtis; my grandmother Carolyn Pray; and my father, Loren Travis Gray. Despite my best efforts to drown myself in my work, you have always reminded me of what is most important in life. Finally, I thank my partner-in-crime, Julian Reyes. Your smile always brightens my day whether we’re getting lost in the mountains or getting fat together on the couch. v DESIGNING ELECTRIC FIELD ASSISTED CATALYTIC REACTORS FOR HYDROGEN PRODUCTION APPLICATIONS Abstract by Jake T. Gray, Ph.D. Washington State University December 2019 Chair: Su Ha Fundamental studies on the effects of strong electric fields (on the order of 1-10 V/nm) have been conducted in various forms for nearly a century. These investigations have revealed a surprising amount about the natural world: the presence of strong intrinsic electric fields is, in part, responsible for the high catalytic activity of many natural systems. Examples include catalysts ranging from enzymes for biochemical processes to zeolites in industrial-scale petroleum refining to frustrated Lewis acid-base pairs in specialized synthetic chemistry. With Nature as our inspiration, attempts at artificially recreating these highly reactive conditions have been ongoing (albeit sporadically) since at least the 1970s. Until recently, these experiments have been necessarily conducted in high-vacuum systems to avoid the dielectric breakdown associated with long-range high-intensity fields. A handful of attempts at high-pressure, high-throughput applications of this phenomenon have been attempted—but aside from a few promising observations, little progress has been made. vi Herein are presented recent contributions to this body of work focusing on the development of (i) new high-pressure, high-throughput, and high-field reactors for hydrogen-producing reactions and (ii) tools for future reaction engineers seeking to incorporate applied electric fields into their designs. To this end, Chapters 1 and 2 supply comprehensive foundational knowledge including the fundamental physics of electric field assisted catalysis as well as previous attempts at reactor or test apparatus design. Chapter 3 explores the mechanism for the hydrogen producing reaction of formic acid decomposition. This well-characterized reaction is then applied in Chapter 4 as a reactive probe to directly measure the applied field strength at catalyst active sites. A technique is also presented for visualizing the field structures generated across the catalyst. Chapters 5 and 6 delve deeper into more traditional hydrogen producing reactions via hydrocarbon steam reforming: methane in Chapter 5 and gasoline, diesel, and jet fuel surrogates in Chapter 6. Two reactor designs are investigated in detail throughout this dissertation: the integrated circuit reactor in Chapters 4 and 5 and the coaxial capacitor reactor in Chapter 6. Suggested next steps for future researchers are provided in Chapter 7. vii TABLE OF CONTENTS Page ACKNOWLEDGEMENT ............................................................................................................. iii ABSTRACT ................................................................................................................................... vi LIST OF TABLES ......................................................................................................................... xi LIST OF FIGURES ...................................................................................................................... xii PREFACE ........................................................................................................................................1 CHAPTER 1: INTRODUCTION ....................................................................................................3 Section 1.1. Transport .............................................................................................................3 Section 1.2. Molecular Orientation .........................................................................................7 Section 1.3. Electronic Structure ..........................................................................................10 Section 1.4. Kinetic and Thermodynamic Changes ..............................................................16 Section 1.5. Intrinsic
Recommended publications
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • Water Splitting by Heterogeneous Catalysis
    !"#$ #"%"" &' () * ( +# ,% - . ( (.( ( . %/ .0! 1 ( % 2 3 . 4 . 5 % . . % . . . . . . 3 % !# 3 ( 3 ( 3 ( 3 %/. . - % . (. 6 7 % ( 2!0! . (/ (3 . 7 % ( ( 3 % . 3 ( %/ . 8 9 3 8 % ( :;0 9 . <= 3 9 . % ( . ( 3 > % !"#$ ?@@ %% @ A B ?? ? ? #;C#C# ,8D$CD#$$D$":D! ,8D$CD#$$D$";"C ! " # $ (#" D# WATER SPLITTING BY HETEROGENEOUS CATALYSIS Henrik Svengren Water splitting by heterogeneous catalysis Henrik Svengren ©Henrik Svengren, Stockholm University 2017 ISBN print 978-91-7797-039-2 ISBN PDF 978-91-7797-040-8 Printed in Sweden by Universitetsservice US-AB, Stockholm 2017 Distributed by the Department of Materials and Environmental Chemistry To my beloved family Cover image + Heterogeneous catalysis of water oxidation according to 2H2O ĺ O2 + 4H on CoSbO4/CoSb2O6, investigated in Paper II. The figure is composed of SEM- and TEM images, structural drawings, reactant- and product molecules. i Examination Faculty opponent Docent Tomas Edvinsson Solid State Physics Department of Engineering Sciences Uppsala University,
    [Show full text]
  • Catalytic Oxidation of NO to NO2 for Nitric Acid Production Over a Pt
    1 Catalytic oxidation of NO to NO2 for nitric acid production over a Pt/Al2O3 catalyst Ata ul Rauf Salmana, Bjørn Christian Engerb, Xavier Auvraya c, Rune Lødengb, Mohan Menond, David Wallerd, Magnus Rønninga* a Department of Chemical Engineering, Norwegian University of Science and Technology (NTNU), Sem Sælands vei 4, NO-7491 Trondheim, Norway. b SINTEF Industry, Kinetic and Catalysis group, P.O. Box 4760 Torgarden, NO-7465 Trondheim, Norway. c Current address: Competence Centre for Catalysis, Chemical Engineering, Chalmers University of Technology, S-412 96 Gothenburg, Sweden d YARA Technology Center, Herøya Forskningspark, Bygg 92, Hydrovegen 67, NO-3936 Porsgrunn, Norway. * Corresponding author. Tel.: +47 73594121. E-mail address: [email protected] (M. Rønning). 2 Abstract The oxidation of nitric oxide (NO) to nitrogen dioxide (NO2) is a key step both in NOx abatement technologies as well as in the Ostwald process for nitric acid production. A 1 wt.% Pt/Al2O3 catalyst was used to study oxidation of nitric oxide at two different concentrations of NO; 400 ppm NO (representative of engine exhaust treatment) and 10% NO (nitric acid plant). The catalyst was characterised using N2 adsorption and CO chemisorption. The effect of temperature and feed concentration on catalytic activity was investigated. For a feed comprising of 10% NO and 6% O2, Pt/Al2O3 exhibits significant catalytic activity above o 300 C. Addition of 15% H2O in the feed had an insignificant effect on activity of the catalyst. We report for the first time the kinetics for oxidation of NO to NO2 under nitric acid plant conditions. An apparent activation energy of 33 kJ/mol was observed.
    [Show full text]
  • PDF (Chapter 5
    ~---=---5 __ Heterogeneous Catalysis 5.1 I Introduction Catalysis is a term coined by Baron J. J. Berzelius in 1835 to describe the property of substances that facilitate chemical reactions without being consumed in them. A broad definition of catalysis also allows for materials that slow the rate of a reac­ tion. Whereas catalysts can greatly affect the rate of a reaction, the equilibrium com­ position of reactants and products is still determined solely by thermodynamics. Heterogeneous catalysts are distinguished from homogeneous catalysts by the dif­ ferent phases present during reaction. Homogeneous catalysts are present in the same phase as reactants and products, usually liquid, while heterogeneous catalysts are present in a different phase, usually solid. The main advantage of using a hetero­ geneous catalyst is the relative ease of catalyst separation from the product stream that aids in the creation of continuous chemical processes. Additionally, heteroge­ neous catalysts are typically more tolerant ofextreme operating conditions than their homogeneous analogues. A heterogeneous catalytic reaction involves adsorption of reactants from a fluid phase onto a solid surface, surface reaction of adsorbed species, and desorption of products into the fluid phase. Clearly, the presence of a catalyst provides an alter­ native sequence of elementary steps to accomplish the desired chemical reaction from that in its absence. If the energy barriers of the catalytic path are much lower than the barrier(s) of the noncatalytic path, significant enhancements in the reaction rate can be realized by use of a catalyst. This concept has already been introduced in the previous chapter with regard to the CI catalyzed decomposition of ozone (Figure 4.1.2) and enzyme-catalyzed conversion of substrate (Figure 4.2.4).
    [Show full text]
  • Heterogeneous Catalysis on Metal Oxides
    catalysts Review Heterogeneous Catalysis on Metal Oxides Jacques C. Védrine ID Laboratoire de Réactivité de Surface, Université P. & M. Curie, Sorbonne Université, UMR-CNRS 7197, 4 Place Jussieu, F-75252 Paris, France; [email protected]; Tel.: +33-1-442-75560 Received: 8 October 2017; Accepted: 27 October 2017; Published: 10 November 2017 Abstract: This review article contains a reminder of the fundamentals of heterogeneous catalysis and a description of the main domains of heterogeneous catalysis and main families of metal oxide catalysts, which cover acid-base reactions, selective partial oxidation reactions, total oxidation reactions, depollution, biomass conversion, green chemistry and photocatalysis. Metal oxide catalysts are essential components in most refining and petrochemical processes. These catalysts are also critical to improving environmental quality. This paper attempts to review the major current industrial applications of supported and unsupported metal oxide catalysts. Viewpoints for understanding the catalysts’ action are given, while applications and several case studies from academia and industry are given. Emphases are on catalyst description from synthesis to reaction conditions, on main industrial applications in the different domains and on views for the future, mainly regulated by environmental issues. Following a review of the major types of metal oxide catalysts and the processes that use these catalysts, this paper considers current and prospective major applications, where recent advances in the science
    [Show full text]
  • Heterogeneous Catalytic Hydrogenation
    •Platinum Metals Rev., 2012, 56, (4), 236–241• Heterogeneous Catalytic Hydrogenation Platinum group metals as hydrogenation catalysts in a two-day course http://dx.doi.org/10.1595/147106712X654187 http://www.platinummetalsreview.com/ Reviewed by Fabrizio Nerozzi Introduction Johnson Matthey, Catalysis and Chiral Technologies, Heterogeneous catalytic hydrogenations are important Orchard Road, Royston, Hertfordshire SG8 5HE, UK reactions that fi nd wide industrial application in Email: [email protected] the production of pharmaceuticals, agrochemicals, fi ne chemicals, fl avours, fragrances and dietary supplements. The reactions are generally highly selective and easy to work up, the catalyst can often be recovered and recycled, and the processes are atom effi cient. It is therefore no surprise that somewhere between 10–20% of the reactions used to produce chemicals today are catalytic hydrogenations. Despite the importance of the technique, and mainly because of its multidisciplinary nature, development chemists and engineers have a hard time fi nding training on this highly specialised subject. Scientifi c Update has fi lled this gap with a training course run for the fi rst time on the 16th and 17th of April 2012, in Brussels, Belgium (1). Attended by 35 scientists from 10 European countries and the USA, representing 27 chemical companies and research institutions, the course was an extensive scientifi c overview of heterogeneous catalytic hydrogenation, but also touched on engineering, safety and economic topics. The tutor was Felix Roessler, a catalysis expert who during his long career has worked at Roche and DSM, was honoured twice with the Sandmeyer Award granted by the Swiss Chemical Society (2), has authored 18 publications or monographs and holds 4 patents.
    [Show full text]
  • Design of Molecular Water Oxidation Catalysts Stabilized by Ultrathin Inorganic Overlayers—Is Active Site Protection Necessary?
    inorganics Article Design of Molecular Water Oxidation Catalysts Stabilized by Ultrathin Inorganic Overlayers—Is Active Site Protection Necessary? Laurent Sévery 1 , Sebastian Siol 2 and S. David Tilley 1,* 1 Department of Chemistry, University of Zurich, Winterthurerstrasse 190, 8057 Zurich, Switzerland; [email protected] 2 EMPA, Uberlandstrasse 129, 8600 Dubendorf, Switzerland; [email protected] * Correspondence: [email protected]; Tel.: +41-44-635-46-75 Received: 4 September 2018; Accepted: 27 September 2018; Published: 29 September 2018 Abstract: Anchored molecular catalysts provide a good step towards bridging the gap between homogeneous and heterogeneous catalysis. However, applications in an aqueous environment pose a serious challenge to anchoring groups in terms of stability. Ultrathin overlayers embedding these catalysts on the surface using atomic layer deposition (ALD) are an elegant solution to tackle the anchoring group instability. The propensity of ALD precursors to react with water leads to the question whether molecules containing aqua ligands, such as most water oxidation complexes, can be protected without side reactions and deactivation during the deposition process. We synthesized two iridium and two ruthenium-based water oxidation catalysts, which contained an aqua ligand (Ir–OH2 and Ru–OH2) or a chloride (Ir–Cl and Ru–Cl) that served as a protecting group for the former. Using a ligand exchange reaction on the anchored and partially embedded Ru–Cl, the optimal overlayer thickness was determined to be 1.6 nm. An electrochemical test of the protected catalysts on meso-ITO showed different behaviors for the Ru and the Ir catalysts. The former showed no onset difference between protected and non-protected versions, but limited stability.
    [Show full text]
  • Heterogeneous Catalyst Deactivation and Regeneration: a Review
    Catalysts 2015, 5, 145-269; doi:10.3390/catal5010145 OPEN ACCESS catalysts ISSN 2073-4344 www.mdpi.com/journal/catalysts Review Heterogeneous Catalyst Deactivation and Regeneration: A Review Morris D. Argyle and Calvin H. Bartholomew * Chemical Engineering Department, Brigham Young University, Provo, UT 84602, USA; E-Mail: [email protected] * Author to whom correspondence should be addressed; E-Mail: [email protected]; Tel: +1-801-422-4162, Fax: +1-801-422-0151. Academic Editor: Keith Hohn Received: 30 December 2013 / Accepted: 12 September 2014 / Published: 26 February 2015 Abstract: Deactivation of heterogeneous catalysts is a ubiquitous problem that causes loss of catalytic rate with time. This review on deactivation and regeneration of heterogeneous catalysts classifies deactivation by type (chemical, thermal, and mechanical) and by mechanism (poisoning, fouling, thermal degradation, vapor formation, vapor-solid and solid-solid reactions, and attrition/crushing). The key features and considerations for each of these deactivation types is reviewed in detail with reference to the latest literature reports in these areas. Two case studies on the deactivation mechanisms of catalysts used for cobalt Fischer-Tropsch and selective catalytic reduction are considered to provide additional depth in the topics of sintering, coking, poisoning, and fouling. Regeneration considerations and options are also briefly discussed for each deactivation mechanism. Keywords: heterogeneous catalysis; deactivation; regeneration 1. Introduction Catalyst deactivation, the loss over time of catalytic activity and/or selectivity, is a problem of great and continuing concern in the practice of industrial catalytic processes. Costs to industry for catalyst replacement and process shutdown total billions of dollars per year. Time scales for catalyst deactivation vary considerably; for example, in the case of cracking catalysts, catalyst mortality may be on the order of seconds, while in ammonia synthesis the iron catalyst may last for 5–10 years.
    [Show full text]
  • Molecular Enhancement of Heterogeneous CO2 Reduction
    PERSPECTIVE https://doi.org/10.1038/s41563-020-0610-2 Molecular enhancement of heterogeneous CO2 reduction Dae-Hyun Nam 1,7, Phil De Luna 1,2,3,7, Alonso Rosas-Hernández 4,5, Arnaud Thevenon 4,5, Fengwang Li 1, Theodor Agapie4,5, Jonas C. Peters4,5, Osama Shekhah 6, Mohamed Eddaoudi 6 and Edward H. Sargent 1 ✉ The electrocatalytic carbon dioxide reduction reaction (CO2RR) addresses the need for storage of renewable energy in valuable carbon-based fuels and feedstocks, yet challenges remain in the improvement of electrosynthesis pathways for highly selective hydrocarbon production. To improve catalysis further, it is of increasing interest to lever synergies between heterogeneous and homogeneous approaches. Organic molecules or metal complexes adjacent to heterogeneous active sites provide additional bind- ing interactions that may tune the stability of intermediates, improving catalytic performance by increasing Faradaic efficiency (product selectivity), as well as decreasing overpotential. We offer a forward-looking perspective on molecularly enhanced het- erogeneous catalysis for CO2RR. We discuss four categories of molecularly enhanced strategies: molecular-additive-modified heterogeneous catalysts, immobilized organometallic complex catalysts, reticular catalysts and metal-free polymer catalysts. We introduce present-day challenges in molecular strategies and describe a vision for CO2RR electrocatalysis towards multi-carbon products. These strategies provide potential avenues to address the challenges of catalyst activity, selectivity and stability in the further development of CO2RR. he electrochemical carbon dioxide (CO2) reduction reac- loenzymes, which are able to mediate challenging multi-electron/ tion (CO2RR) to fuels and chemical feedstocks, powered by proton reductive transformations at remarkably fast rates with very renewable electricity, offers a pathway to long-term seasonal little applied bias8.
    [Show full text]
  • Theoretical Studies in Heterogeneous Catalysis: Towards a Rational Design of Novel Catalysts for Hydrodesulfurization and Hydrogen Production
    BNL-81930-2009-BC Theoretical Studies in Heterogenous Catalysis: Towards a Rational Design of Novel Catalysts for Hydrodesulfurization and Hydrogen Production José A. Rodriguez and Ping Liu To be published in “New Developments in QuantumChemistry” October 2008 Chemistry Department Brookhaven National Laboratory P.O. Box 5000 Upton, NY 11973-5000 www.bnl.gov Notice: This manuscript has been authored by employees of Brookhaven Science Associates, LLC under Contract No. DE-AC02-98CH10886 with the U.S. Department of Energy. The publisher by accepting the manuscript for publication acknowledges that the United States Government retains a non-exclusive, paid-up, irrevocable, world-wide license to publish or reproduce the published form of this manuscript, or allow others to do so, for United States Government purposes. This preprint is intended for publication in a journal or proceedings. Since changes may be made before publication, it may not be cited or reproduced without the author’s permission. DISCLAIMER This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, nor any of their contractors, subcontractors, or their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or any third party’s use or the results of such use of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government or any agency thereof or its contractors or subcontractors.
    [Show full text]
  • Frontiers at the Interface of Homogeneous and Heterogeneous Catalysis
    FRONTIERS AT THE INTERFACE OF HOMOGENEOUS AND HETEROGENEOUS CATALYSIS Meeting of the Catalysis Science Program Chemical Sciences, Geosciences and Biosciences Division Office of Basic Energy Sciences U.S. Department of Energy Westin Annapolis Annapolis, Maryland June 30 – July 2, 2013 This document was produced under contract number DE-AC05-060R23100 between the U.S. Department of Energy and Oak Ridge Associated Universities. FOREWORD The 2013 Catalysis Science Program Meeting is sponsored by the Division of Chemical Sciences, Geosciences and Biosciences, Office of Basic Energy Sciences (BES), U.S. Department of Energy. It is being held on June 30 through July 2, 2013, at the Westin Annapolis Hotel, Annapolis, Maryland. The purposes of this meeting are to discuss the recent advances in the chemical, physical, and biological bases of catalysis science, to foster exchange of ideas and cooperation among participants, and to discuss the new challenges and opportunities recently emerging in energy technologies. Catalysis activities within BES emphasize fundamental research aimed at initially understanding and finally controlling the chemical conversion of natural and artificial feedstocks. The long-term goal of this research is to discover fundamental principles and produce ever more insightful approaches to predict structure-reactivity behavior. Such knowledge, integrated with advances in chemical and materials synthesis, in situ and operando analytical instrumentation, and chemical kinetics and quantum chemistry methods, will allow the control of chemical reactions along desired pathways. Ultimately, this new knowledge should impact the efficiency of conversion of natural resources into fuels, chemicals, materials, or other forms of energy, while minimizing the impact to the environment. This year’s meeting is focused on three topical areas: (i) the interface of homogeneous and heterogeneous catalysis, (ii) catalysis for biomass or solar energy conversion, and (iii) molecular catalysis, with an emphasis on organic synthesis.
    [Show full text]