Elucidating CO2 Chemisorption in Diamine-Appended Metal–Organic Frameworks Alexander C
Total Page:16
File Type:pdf, Size:1020Kb
Load more
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. -
Insight Into Adsorption Thermodynamics
16 Insight Into Adsorption Thermodynamics Dr. Papita Saha and Shamik Chowdhury Biotechnology Department, National Institute of Technology-Durgapur, Mahatma Gandhi Avenue, Durgapur (WB)-713209 India 1. Introduction Saving the environment to save the Earth and to make the future of mankind safe is the need of the hour. Over the past several decades, the exponential population and social civilization change, affluent lifestyles and resources use, and continuing progress of the industrial and technologies has been accompanied by a sharp modernization and metropolitan growth. The world is reaching new horizons but the cost which we are paying or we will pay in near future is surely going to be high. Among the consequences of this rapid growth is environmental disorder with a big pollution problem. Rapid industrialization, unplanned urbanization and unskilled utilization of natural water resources have led to the destruction of water quality in many parts of the world. In many developing countries, groundwater provides drinking water for more than one-half of the nation's population, and is the sole source of drinking water for many rural communities and some large cities. However, due to industrial, agricultural and domestic activities, a variety of chemicals can pass through the soil and potentially contaminate natural water resources and reservoirs. In recent years, the surge of industrial activities has led to tremendous increase in the use of heavy metals, synthetic dyes and other toxic chemicals, and inevitably resulted in an increased flux of these substances in the aquatic environment. Environmental contamination by toxic heavy metals and synthetic dyes is becoming a serious dilemma now days due to their negative ecotoxicological effects and bioaccumulation in wildlife. -
4. Industrial Processes and Product
4. Industrial Processes and Product Use The Industrial Processes and Product Use (IPPU) chapter includes greenhouse gas emissions occurring from industrial processes and from the use of greenhouse gases in products. The industrial processes and product use categories included in this chapter are presented in Figure 4-1. Greenhouse gas emissions from industrial processes can occur in two different ways. First, they may be generated and emitted as the byproducts of various non-energy- related industrial activities. Second, they may be emitted due to their use in manufacturing processes or by end- consumers. In the case of byproduct emissions, the emissions are generated by an industrial process itself, and are not directly a result of energy consumed during the process. For example, raw materials can be chemically or physically transformed from one state to another. This transformation can result in the release of greenhouse gases such as carbon dioxide (CO2), methane (CH4), nitrous oxide (N2O), and fluorinated greenhouse gases (e.g., HFC-23). The greenhouse gas byproduct generating processes included in this chapter include iron and steel production and metallurgical coke production, cement production, lime production, other process uses of carbonates (e.g., flux stone, flue gas desulfurization, and glass manufacturing), ammonia production and urea consumption, petrochemical production, aluminum production, HCFC-22 production, soda ash production and use, titanium dioxide production, ferroalloy production, glass production, zinc production, phosphoric acid production, lead production, silicon carbide production and consumption, nitric acid production, adipic acid production, and caprolactam production. Greenhouse gases that are used in manufacturing processes or by end-consumers include man-made compounds such as hydrofluorocarbons (HFCs), perfluorocarbons (PFCs), sulfur hexafluoride (SF6), and nitrogen trifluoride (NF3). -
High Pressure Hydrogen Sorption Isotherms on Microporous Fluorinated Metal Organic Frameworks (FMOF) and BPL Carbon Using High‐Pressure TGA (TGA‐HP)
High Pressure Hydrogen Sorption Isotherms on Microporous Fluorinated Metal Organic Frameworks (FMOF) and BPL Carbon Using High‐Pressure TGA (TGA‐HP) Qian Mather and A. F. Venero TA Instruments‐Waters LLC, 159 Lukens Drive, New Castle, DE 19720, USA Prof. Mohammad Omary, University of North Texas, Denton, TX, USA ABSTRACT This paper discusses the use of high‐pressure TGA (TGA‐HP) to investigate the hydrogen storage capacity of a novel fluorinated metal organic framework (FMOF). INTRODUCTION Hydrogen is attractive as the clean energy source of the future and as a potential replacement for fossil fuels due to the absence of harmful exhaust emissions and compatibility with fuel cells. The challenge for adopting hydrogen as a fuel source is the need for practical, portable storage systems.1 Potential hydrogen storage technologies include containers of compressed or liquefied H2, carbon nanotubes, metal hydrides and metal organic frameworks (MOFs), which store hydrogen via physisorption or chemisorption. The Department of Energy (DOE) has set aggressive targets for hydrogen storage capacity at near‐ambient temperatures and pressures. At present, none of the currently‐available candidate storage materials possess the combination of high hydrogen densities, low desorption temperatures, fast kinetics, and low‐cost needed for automotive applications that meet the DOE criteria. Recently, new microporous metal‐ organic frameworks (MOFs) were found to be promising candidates for hydrogen storage. Porous MOFs are constructed through the assembly of metal‐containing clusters with multidentate organic ligands via coordination bonds into a three‐dimensional structure with well‐defined pore size and morphology. Because of their high surface area, controlled pore size and functionality, high gas sorption capacities are observed. -
Chemisorption Poster
Chemisorption Presented by Micromeritics Instrument Corporation Blue spheres: Red spheres: Red and Green: surface molecules gas molecules molecules react only with hemisorption: Chemical 1.) 2.) 3.) each other to form a new adsorption is an interaction Green spheres: molecular species muchC stronger than physical ad- active sites sorption. In fact, the interaction is an actual chemical bond where electrons are shared between the gas and the solid surface. While physical adsorption takes place on all surfaces if temperature and pressure conditions are favorable, chemisorption only occurs on cer- tain surfaces and only if these sur- faces are clean. Chemisorption, unlike physisorption, ceases when the adsorbate can no longer make direct contact with the surface; it is therefore a single layer process. Most medicinal, chemical, and petroleum-derived items in Chemisorption Physisorption Many molecules must be activated before they will react ac- common usage are dependent at some stage in their manu- cording to present theories. Activation energy is a measure Near or above dew point Temperature Range: Unlimited facture on a heterogeneous catalytic process. High octane of gas of the energy which must be supplied to them to bring about gasoline, plastics, fertilizers, and herbicides would either be reaction. In some cases the activation energy requirement is prohibitively expensive or unobtainable without them. Like- Enthalpy of Typically Typically such that reaction will proceed only at a measurable rate above (5 - 80 kJ/mol) wise, pollution control would be almost nonexistent were it Adsorption: (80 - 800 kJ/mol) a certain temperature. In others, reaction proceeds rapidly at not for catalysts. Nature of the low temperature, hydrogen on platinum being an example of a Irreversible Reversable adsorption: chemisorption reaction where the activation energy approach- Physical and Chemical Limited to one es zero. -
Control No. 1-5-54-01174(1F)
I 1: L I Y ,e- .- l THE DEVELOPMENT OF STRUCTURAL ADHESIVE I I SYSTEMS SUITABLE FOR USE WITH LIQUID OXYGEN ~ il Jerome Hollander, Floyd D. Trischler, and Edward S. Harrison ANNUAL SUMMARY REPORT I11 1 July 1965 to 30 June 1966 July 1966 , Prepared under Contract No. NAS 8-11068 Control No. 1-5-54-01174(1F) WHITTA-KER COR-PORATION Narmco Research & Development Division San Diego, California 92123 N e k (ACCESSION NUMBER) I (THRU) ea > - (PAGES) i (CODE) 2 (NASA CR OR TUX OR AD NUMBER) (CATEGORY) Propulsion and Vehicle Engineering Division 1'I! National Aeronautic s and Space Administration George C. Marshall Space Flight Center Huntsville, Alabama FOREWORD This report was prepared by Whittaker Corporation, Narmco Research 6 Development Division, under Contract No. NAS 8-11068, Control KO. 1-5-54- 01174(1F), entitled "The Development of Structural Adhesive Systems Suitable for Use with Liquid Oxygen," for the George C. Marshall Space Flight Center of the National Aeronautics and Space Administration. The work was adminis- tered under the direction of the Propulsion and Vehicle Engineering Division, Engineering Materials Branch, with Dr. W. E. Hill acting as project officer. The research work was conducted in Narmco's laboratory by Dr. Jerome Hollander and Mr. Floyd D. Trischler, Senior Research Chemists, Mr. Edward S. Harrison, Research Chemist and Mr. Robert M. DeBorde, Research Technician. Also con- tributing to the research were Mr. Richard T. Rafter, Mr. Phillip N. Crabtree, Mrs . Beatrix Y. Sanders, and Mr. Jerry L. Kerkmeyer , Research Chemists. Dr. Jerome Hollander served as program manager. This report covers the period 1 July 1965 to 30 June 1966. -
Method for Preparing Polymeric Foams and Chemical Compositions Used Therefor
Europaisches Patentamt 19 European Patent Office Office europeen des brevets © Publication number : 0 498 628 A1 EUROPEAN PATENT APPLICATION (2j) Application number : 92300954.2 © int. ci.5 : C08G 18/10, C08J 9/00, // C08L75/04 (22) Date of filing : 04.02.92 (§) Priority : 04.02.91 GB 9102362 Inventor : Postema, Aaldrik Roelf Frieswijk 113 NL-1852 VG Heiloo (NL) @ Date of publication of application Inventor : Stanssens, Drik 12.08.92 Bulletin 92/33 Pastoorslindestraat 75, Bus 1 B-3620 Lanaken (BE) Inventor : Randall, David @ Designated Contracting States : Nachtegalenlaan 7 DE ES FR GB IT NL SE B-3078Everberg (BE) Inventor : De Vos, Rik Valleelaan 40a © Applicant : IMPERIAL CHEMICAL B-3110 Rotselaar (BE) INDUSTRIES PLC Imperial Chemical House, Millbank London SW1P 3JF (GB) (74) Representative : Leherte, Georges Maurice Lucien Marie et al Group Patents Services Dept., P.O. Box 6, (72) Inventor : Gillis, Herbert Russell Shire Park, Bessemer Road Unit 4, 8230 Crestview Drive Welwyn Garden City, Hertfordshire AL7 1HD Sterling Heights, Michigan 48077 (US) (GB) © Method for preparing polymeric foams and chemical compositions used therefor. © A method for the preparation of rigid foams by reacting an organic polyisocyanate with an isocyanate-reactive material in the presence of a blowing promoter characterised in that the iso- cyanate-reactive material comprises at least one isocyanate-reactive cyclic carbonate or isocyanate- reactive cyclic urea, the reaction being performed in the presence of an inert insoluble organic liquid which is present as the disperse phase of an emulsion or a microemulsion, and in the presence of a metal salt catalyst. 00 CM CO 00 o> LU Jouve, 18, rue Saint-Denis, 75001 PARIS EP 0 498 628 A1 This invention relates to polymeric foams and more especially to rigid polyurethane foams derived from organic polyisocyanates and to methods for their preparation. -
Chemistry of Acetylene on Platinum (111) and (100) Surfaces (Chemisorption/Ultra-High Vacuum/Metal Surface Chemistry/Hydrocarbon Reactions) E
Proc. Nati Acad. Sci. USA Vol. 78, No. 11, pp. 6571-6575, November 1981 Chemistry Chemistry of acetylene on platinum (111) and (100) surfaces (chemisorption/ultra-high vacuum/metal surface chemistry/hydrocarbon reactions) E. L. MUETTERTIESt, M.-C. TSAit, AND S. R. KELEMENt tMaterials and Molecular Research Division, Lawrence Berkeley Laboratory, Berkeley, California 94720; and Department of Chemistry, University of California, Berkeley, California 94720; and tCorporate Research Science Laboratories, Exxon Research and Engineering Company, P.O. Box 45, Linden, New Jersey 07036 Contributed by Earl L. Muetterties, July 24, 1981 ABSTRACT An ultra-high vacuum experimental study of face generated showed the 5 x 20 low energy electron diffiac- acetylene chemisorption on Pt(111) and Pt(100) and ofthe reaction tion pattern. The 5 X 20 surface converted to the 1 X 1 structure of hydrogen with the acetylene adsorbate has established distin- with exposure to acetylene (5). The 1 x 1 surface is stabilized guishing features ofcarbon-hydrogen bond breaking and making by the presence of acetylene and is present during the hydro- processes as a function ofpressure, temperature, and surfacecrys- genation and dehydrogenation processes discussed in this tallography. The rates for both processes are substantially higher article. on the Pt(100) surface. Net acetylene-hydrogen processes, in the temperature range of20°C to -13rC, are distinctly different on the two surfaces: on Pt(100) the net reaction is hydrogen exchange RESULTS ('H. H exchange) and on Pt(III) the only detectable reaction is hydrogenation. Stereochemical differences in the acetylene ad- Acetylene is the simplest unsaturated hydrocarbon. Its geo- sorbate structure are considered to be a contributing factor to the metric structure, electronic structure, and organic chemistry differences in acetylene chemistry on these two surfaces. -
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). -
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 -
Perfluorotributylamine Safety Data Sheet 3132206 According to Federal Register / Vol
Perfluorotributylamine Safety Data Sheet 3132206 according to Federal Register / Vol. 77, No. 58 / Monday, March 26, 2012 / Rules and Regulations Date of issue: 08/04/2015 Version: 1.0 SECTION 1: Identification 1.1. Identification Product form : Substance Substance name : Perfluorotributylamine CAS No : 311-89-7 Product code : 3132-2-06 Formula : C12F27N Synonyms : Perfluorotributylamine; HEPTACOSA; Tris(perfluorobut-1-yl)amine; Heptacosafluorotributylamine Other means of identification : MFCD00000436 1.2. Relevant identified uses of the substance or mixture and uses advised against Use of the substance/mixture : Laboratory chemicals Manufacture of substances Scientific research and development 1.3. Details of the supplier of the safety data sheet SynQuest Laboratories, Inc. P.O. Box 309 Alachua, FL 32615 - United States of America T (386) 462-0788 - F (386) 462-7097 [email protected] - www.synquestlabs.com 1.4. Emergency telephone number Emergency number : (844) 523-4086 (3E Company - Account 10069) SECTION 2: Hazard(s) identification 2.1. Classification of the substance or mixture Classification (GHS-US) Skin Irrit. 2 H315 - Causes skin irritation Eye Irrit. 2A H319 - Causes serious eye irritation STOT SE 3 H335 - May cause respiratory irritation Full text of H-phrases: see section 16 2.2. Label elements GHS-US labeling Hazard pictograms (GHS-US) : GHS07 Signal word (GHS-US) : Warning Hazard statements (GHS-US) : H315 - Causes skin irritation H319 - Causes serious eye irritation H335 - May cause respiratory irritation Precautionary statements (GHS-US) : P261 - Avoid breathing fumes, mist, spray, vapors P264 - Wash skin thoroughly after handling P271 - Use only outdoors or in a well-ventilated area P280 - Wear protective gloves/protective clothing/eye protection/face protection P302+P352 - If on skin: Wash with plenty of soap and water P304+P340 - If inhaled: Remove person to fresh air and keep comfortable for breathing P305+P351+P338 - If in eyes: Rinse cautiously with water for several minutes. -
Gold Catalysts Containing Interstitial Carbon Atoms Boost Hydrogenation Activity
ARTICLE https://doi.org/10.1038/s41467-020-18322-x OPEN Gold catalysts containing interstitial carbon atoms boost hydrogenation activity Yafei Sun1,6, Yueqiang Cao 2,6, Lili Wang1,6, Xiaotong Mu1, Qingfei Zhao1, Rui Si3, Xiaojuan Zhu1, ✉ Shangjun Chen1, Bingsen Zhang 4, De Chen5 & Ying Wan 1 Supported gold nanoparticles are emerging catalysts for heterogeneous catalytic reactions, including selective hydrogenation. The traditionally used supports such as silica do not favor 1234567890():,; the heterolytic dissociation of hydrogen on the surface of gold, thus limiting its hydrogenation activity. Here we use gold catalyst particles partially embedded in the pore walls of meso- porous carbon with carbon atoms occupying interstitial sites in the gold lattice. This catalyst allows improved electron transfer from carbon to gold and, when used for the chemoselective hydrogenation of 3-nitrostyrene, gives a three times higher turn-over frequency (TOF) than that for the well-established Au/TiO2 system. The d electron gain of Au is linearly related to the activation entropy and TOF. The catalyst is stable, and can be recycled ten times with negligible loss of both reaction rate and overall conversion. This strategy paves the way for optimizing noble metal catalysts to give an enhanced hydrogenation catalytic performance. 1 Key Laboratory of Resource Chemistry of Ministry of Education, Shanghai Key Laboratory of Rare Earth Functional Materials, and Department of Chemistry, Shanghai Normal University, 200234 Shanghai, China. 2 State Key Laboratory of Chemical Engineering, East China University of Science and Technology, 200237 Shanghai, China. 3 Shanghai Synchrotron Radiation Facility, Shanghai Institute of Applied Physics, Chinese Academy of Sciences, 201204 Shanghai, China.