Theories of Reaction Rates
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Rate Constants and Kinetic Isotope Effects for Methoxy Radical Reacting with NO2 and O2 Jiajue Chai, Hongyi Hu, Theodore
Rate Constants and Kinetic Isotope Effects for Methoxy Radical Reacting with NO2 and O2 Jiajue Chai, Hongyi Hu, Theodore. S. Dibble* Department of Chemistry, College of Environmental Science and Forestry, State University of New York, Syracuse, New York 13210, United States Geoffrey. S. Tyndall,* and John. J. Orlando Atmospheric Chemistry Division, National Center for Atmospheric Research, Boulder, Colorado 80307, United States Abstract Relative rate studies were carried out to determine the temperature dependent rate constant ratio k1/k2a: CH3O• + O2 → HCHO + HO2• (R1) CH3O• + NO2 (+M) → CH3ONO2 (+ M) (R2a) over the temperature range 250-333 K in an environmental chamber at 700 Torr using FTIR detection. Absolute rate constants k2 were determined using laser flash photolysis/laser induced fluorescence under the same conditions. The analogous experiments were carried out for the reactions of perdeuterated methoxy radical (CD3O•). Absolute rate constants k2 were in excellent agreement with the recommendations of the JPL Data Evaluation panel. The combined data (i.e., 3 -1 k1/k2 and k2) allow determination of k1 as cm s , corresponding to 1.4 × 10-15 cm3 s-1 at 298 K. The rate constant at 298 K is in excellent agreement with previous work, but the observed temperature dependence is less than previously reported. The deuterium isotope effect, kH/kD, can be expressed in Arrhenius form as The deuterium isotope effect does not appear to be greatly influenced by tunneling, which is consistent with previous theoretical work by Hu and Dibble (Hu, H.; Dibble, T. S., J. Phys. Chem. A 2013, 117, 14230–14242). Keywords: methylnitrite, formaldehyde, methylnitrate, alkoxy radicals, kinetic isotope effect * [email protected], [email protected] 1 I. -
Chapter 9. Atomic Transport Properties
NEA/NSC/R(2015)5 Chapter 9. Atomic transport properties M. Freyss CEA, DEN, DEC, Centre de Cadarache, France Abstract As presented in the first chapter of this book, atomic transport properties govern a large panel of nuclear fuel properties, from its microstructure after fabrication to its behaviour under irradiation: grain growth, oxidation, fission product release, gas bubble nucleation. The modelling of the atomic transport properties is therefore the key to understanding and predicting the material behaviour under irradiation or in storage conditions. In particular, it is noteworthy that many modelling techniques within the so-called multi-scale modelling scheme of materials make use of atomic transport data as input parameters: activation energies of diffusion, diffusion coefficients, diffusion mechanisms, all of which are then required to be known accurately. Modelling approaches that are readily used or which could be used to determine atomic transport properties of nuclear materials are reviewed here. They comprise, on the one hand, static atomistic calculations, in which the migration mechanism is fixed and the corresponding migration energy barrier is calculated, and, on the other hand, molecular dynamics calculations and kinetic Monte-Carlo simulations, for which the time evolution of the system is explicitly calculated. Introduction In nuclear materials, atomic transport properties can be a combination of radiation effects (atom collisions) and thermal effects (lattice vibrations), this latter being possibly enhanced by vacancies created by radiation damage in the crystal lattice (radiation enhanced-diffusion). Thermal diffusion usually occurs at high temperature (typically above 1 000 K in nuclear ceramics), which makes the transport processes difficult to model at lower temperatures because of the low probability to see the diffusion event occur in a reasonable simulation time. -
SF Chemical Kinetics. Microscopic Theories of Chemical Reaction Kinetics
SF Chemical Kinetics. Lecture 5. Microscopic theory of chemical reaction kinetics. Microscopic theories of chemical reaction kinetics. • A basic aim is to calculate the rate constant for a chemical reaction from first principles using fundamental physics. • Any microscopic level theory of chemical reaction kinetics must result in the derivation of an expression for the rate constant that is consistent with the empirical Arrhenius equation. • A microscopic model should furthermore provide a reasonable interpretation of the pre-exponential factor A and the activation energy EA in the Arrhenius equation. • We will examine two microscopic models for chemical reactions : – The collision theory. – The activated complex theory. • The main emphasis will be on gas phase bimolecular reactions since reactions in the gas phase are the most simple reaction types. 1 References for Microscopic Theory of Reaction Rates. • Effect of temperature on reaction rate. – Burrows et al Chemistry3, Section 8. 7, pp. 383-389. • Collision Theory/ Activated Complex Theory. – Burrows et al Chemistry3, Section 8.8, pp.390-395. – Atkins, de Paula, Physical Chemistry 9th edition, Chapter 22, Reaction Dynamics. Section. 22.1, pp.832-838. – Atkins, de Paula, Physical Chemistry 9th edition, Chapter 22, Section.22.4-22.5, pp. 843-850. Collision theory of bimolecular gas phase reactions. • We focus attention on gas phase reactions and assume that chemical reactivity is due to collisions between molecules. • The theoretical approach is based on the kinetic theory of gases. • Molecules are assumed to be hard structureless spheres. Hence the model neglects the discrete chemical structure of an individual molecule. This assumption is unrealistic. • We also assume that no interaction between molecules until contact. -
Eyring Equation
Search Buy/Sell Used Reactors Glass microreactors Hydrogenation Reactor Buy Or Sell Used Reactors Here. Save Time Microreactors made of glass and lab High performance reactor technology Safe And Money Through IPPE! systems for chemical synthesis scale-up. Worldwide supply www.IPPE.com www.mikroglas.com www.biazzi.com Reactors & Calorimeters Induction Heating Reacting Flow Simulation Steam Calculator For Process R&D Laboratories Check Out Induction Heating Software & Mechanisms for Excel steam table add-in for water Automated & Manual Solutions From A Trusted Source. Chemical, Combustion & Materials and steam properties www.helgroup.com myewoss.biz Processes www.chemgoodies.com www.reactiondesign.com Eyring Equation Peter Keusch, University of Regensburg German version "If the Lord Almighty had consulted me before embarking upon the Creation, I should have recommended something simpler." Alphonso X, the Wise of Spain (1223-1284) "Everything should be made as simple as possible, but not simpler." Albert Einstein Both the Arrhenius and the Eyring equation describe the temperature dependence of reaction rate. Strictly speaking, the Arrhenius equation can be applied only to the kinetics of gas reactions. The Eyring equation is also used in the study of solution reactions and mixed phase reactions - all places where the simple collision model is not very helpful. The Arrhenius equation is founded on the empirical observation that rates of reactions increase with temperature. The Eyring equation is a theoretical construct, based on transition state model. The bimolecular reaction is considered by 'transition state theory'. According to the transition state model, the reactants are getting over into an unsteady intermediate state on the reaction pathway. -
Department of Chemistry
07 Sept 2020 2020–2021 Module Outlines MSc Chemistry MSc Chemistry with Medicinal Chemistry Please note: This handbook contains outlines for the modules comprise the lecture courses for all the MSc Chemistry and Chemistry with Medicinal Chemistry courses. The outline is also posted on Moodle for each lecture module. If there are any updates to these published outlines, this will be posted on the Level 4 Moodle, showing the date, to indicate that there has been an update. PGT CLASS HEAD: Dr Stephen Sproules, Room A5-14 Phone (direct):0141-330-3719 email: [email protected] LEVEL 4 CLASS HEAD: Dr Linnea Soler, Room A4-36 Phone (direct):0141-330-5345 email: [email protected] COURSE SECRETARY: Mrs Susan Lumgair, Room A4-30 (Teaching Office) Phone: 0141-330-3243 email: [email protected] TEACHING ADMINISTRATOR: Ms Angela Woolton, Room A4-27 (near Teaching Office) Phone: 0141-330-7704 email: [email protected] Module Topics for Lecture Courses The Course Information Table below shows, for each of the courses (e.g. Organic, Inorganic, etc), the lecture modules and associated lecturer. Chemistry with Medicinal Chemistry students take modules marked # in place of modules marked ¶. Organic Organic Course Modules Lecturer Chem (o) o1 Pericyclic Reactions Dr Sutherland o2 Heterocyclic Systems Dr Boyer o3 Advanced Organic Synthesis Dr Prunet o4 Polymer Chemistry Dr Schmidt o5m Asymmetric Synthesis Prof Clark o6m Organic Materials Dr Draper Inorganic Inorganic Course Modules Lecturer Chem (i) i1 Metals in Medicine -
Estimation of Viscosity Arrhenius Pre-Exponential Factor and Activation Energy of Some Organic Liquids E
ISSN 2350-1030 International Journal of Recent Research in Physics and Chemical Sciences (IJRRPCS) Vol. 5, Issue 1, pp: (18-26), Month: April 2018 – September 2018, Available at: www.paperpublications.org ESTIMATION OF VISCOSITY ARRHENIUS PRE-EXPONENTIAL FACTOR AND ACTIVATION ENERGY OF SOME ORGANIC LIQUIDS E. IKE1 and S. C. EZIKE2 1,2Department of Physics, Modibbo Adama University of Technology, P. M. B. 2076, Yola, Adamawa State, Nigeria. Corresponding Author‟s E-mail: [email protected] Abstract: Information concerning fluid’s physico-chemical behaviors is of utmost importance in the design, running and optimization of industrial processes, in this regard, the idea of fluid viscosity quickly comes to mind. Models have been proposed in literatures to describe the viscosity of liquids and fluids in general. The Arrhenius type equations have been proposed for pure solvents; correlating the pre-exponential factor A and activation energy Ea. In this paper, we aim at extending these Arrhenius parameters to simple organic liquids such as water, ethanol and Diethyl ether. Hence, statistical method and analysis are applied using viscosity data set from the literature of some organic liquids. The Arrhenius type equation simplifies the estimation of viscous properties and the calculations thereafter. Keywords: Viscosity, organic liquids, Arrhenius parameters, correlation, statistics. 1. INTRODUCTION All fluids are compressible and when flowing are capable of sustaining shearing stress on account of friction between the adjacent layers. Viscosity (η) is the inherent property of all fluids and may be referred to as the internal friction offered by a fluid to the flow. For water in a beaker, when stirred and left to itself, the motion subsides after sometime, which can happen only in the presence of resisting force acting on the fluid. -
Tables of Rate Constants for Gas Phase Chemical Reactions of Sulfur Compounds (1971-1979)
NBSIR 80-2118 Tables of Rate Constants for Gas Phase Chemical Reactions of Sulfur Compounds (1971-1979) Francis Westley Chemical Kinetics Division Center for Thermodynamics and Molecular Science National Measurement Laboratory National Bureau of Standards U.S. Department of Commerce Washington. D.C. 20234 July 1980 Interim Report Prepared for Morgantown Energy Technology Center Department of Energy Morgantown, West Virginia 26505 Fice of Standard Reference Data itional Bureau of Standards ashington, D.C. 20234 c, 2 Jl 1 m * rational bureau 07 STANDARDS LIBRARY NBSIR 80-2118 wov 2 4 1980 TABLES OF RATE CONSTANTS FOR GAS f)Oi Clcc -Ore PHASE CHEMICAL REACTIONS OF SULFUR COMPOUNDS (1971-1979) 1 5 (o lo-z im Francis Westley Chemical Kinetics Division Center for Thermodynamics and Molecular Science National Measurement Laboratory National Bureau of Standards U.S. Department of Commerce Washington, D.C. 20234 July 1980 Interim Report Prepared for Morgantown Energy Technology Center Department of Energy Morgantown, West Virginia 26505 and Office of Standard Reference Data National Bureau of Standards Washington, D.C. 20234 U.S. DEPARTMENT OF COMMERCE, Philip M. Klutznick, Secretary Luther H. Hodges, Jr., Deputy Secretary Jordan J. Baruch, Assistant Secretary for Productivity, Technology, and Innovation NATIONAL BUREAU OF STANDARDS. Ernest Ambler, Director . i:i : a 1* V'.OTf in. te- ?') t aa.‘ .1 J Table of Contents Abstract 1 Introduction 2 Guidelines for the User 4 Table of Arrhenius Parameters for Chemical Reactions of Sulfur Compounds 12 Reactions of: S(Sulfur atom) 12 $2(Sulfur dimer) 20 S0(Sulfur monoxide) 21 S02(Sulfur dioxide 23 S0 (Sulfur trioxide) 28 3 S20(Sul fur oxide^O) ) 29 SH (Mercapto free radical) 29 H2S (Hydroqen sulfide 31 CS (Carbon monosulfide free radical) 32 CS2 (Carbon disulfide) 33 COS (Carbon oxide sulfide) 35 CH^S* ( Methyl thio free radical) 36 CH^SH (Methanethiol ) 36 cy-CF^CF^S (Thiirane) 37 CH^SCF^* (Methyl, (methyl thio)-, free radical) ... -
Classical and Modern Methods in Reaction Rate Theory
J. Phys. Chem. 1988, 92, 3711-3725 3711 loss associated with the transition between states is offset by a For the Re( MQ+)-based complexes an additional complication gain in energy in the intramolecular vibrations (eq 3). to intramolecular electron transfer exists arising from a "flattening" On the other hand, if (AGe,,2 + A0,2) > (AG,,l + A,,,) (Figure of the relative orientations of the two rings of the MQ+ ligand 4B) and nuclear tunneling effects in the librational modes are when it accepts an However, the analysis presented unimportant, intramolecular electron transfer can not occur in here does provide a general explanation for the role of free energy a frozen environment. The situation is the same as in Figure 3A. change in environments where dipole motions are restricted. For Even direct Re(1) - MQ' excitation (process a in Figure 4B) a directed, intramolecular electron transfer such as reaction 1, must either lead to the ground state by emission or to the Re- the change in electronic distribution between states will, in general, (11)-bpy'--based MLCT state by reverse electron transfer: lead to a difference between Ao,l and A0,2. This difference creates a solvent dipole barrier to intramolecular electron transfer. It [ (bpy)Re"(CO) 3( MQ')] 2+* -+ (bpy'-)Re"( CO) 3(MQ')] 2'* follows from eq 4 that if light-induced electron transfer is to occur (5) in a frozen environment, the difference in solvent reorganizational The inversion in the sense of the electron transfer in the frozen energy, A& = bS2- A,,, must be compensated for by a favorable environment is induced energetically by the greater solvent re- free energy change, A(AG) = - AGes,l,as organizational energy for the lower excited state, A0,2 > Ao,l - Aces,~- AGes.2 > Ao-2 - &,I (AGes,2 - AGes,l)* or In a macroscopic sample, a distribution of solvent dipole en- vironments exists around the assembly of ground states. -
(A) Reaction Rates (I) Following the Course of a Reaction Reactions Can Be Followed by Measuring Changes in Concentration, Mass and Volume of Reactants Or Products
(a) Reaction rates (i) Following the course of a reaction Reactions can be followed by measuring changes in concentration, mass and volume of reactants or products. g Measuring a change in mass Measuring a change in volume Volume of gas produced of gas Volume Mass of beaker and contents of beaker Mass Time Time The rate is highest at the start of the reaction because the concentration of reactants is highest at this point. The steepness (gradient) of the plotted line indicates the rate of the reaction. We can also measure changes in product concentration using a pH meter for reactions involving acids or alkalis, or by taking small samples and analysing them by titration or spectrophotometry. Concentration reactant Time Calculating the average rate The average rate of a reaction, or stage in a reaction, can be calculated from initial and final quantities and the time interval. change in measured factor Average rate = change in time Units of rate The unit of rate is simply the unit in which the quantity of substance is measured divided by the unit of time used. Using the accepted notation, ‘divided by’ is represented by unit-1. For example, a change in volume measured in cm3 over a time measured in minutes would give a rate with the units cm3min-1. 0.05-0.00 Rate = 50-0 1 - 0.05 = 50 = 0.001moll-1s-1 Concentration moll Concentration 0.075-0.05 Rate = 100-50 0.025 = 50 = 0.0005moll-1s-1 The rate of a reaction, or stage in a reaction, is proportional to the reciprocal of the time taken. -
Kinetics 651
Chapter 12 | Kinetics 651 Chapter 12 Kinetics Figure 12.1 An agama lizard basks in the sun. As its body warms, the chemical reactions of its metabolism speed up. Chapter Outline 12.1 Chemical Reaction Rates 12.2 Factors Affecting Reaction Rates 12.3 Rate Laws 12.4 Integrated Rate Laws 12.5 Collision Theory 12.6 Reaction Mechanisms 12.7 Catalysis Introduction The lizard in the photograph is not simply enjoying the sunshine or working on its tan. The heat from the sun’s rays is critical to the lizard’s survival. A warm lizard can move faster than a cold one because the chemical reactions that allow its muscles to move occur more rapidly at higher temperatures. In the absence of warmth, the lizard is an easy meal for predators. From baking a cake to determining the useful lifespan of a bridge, rates of chemical reactions play important roles in our understanding of processes that involve chemical changes. When planning to run a chemical reaction, we should ask at least two questions. The first is: “Will the reaction produce the desired products in useful quantities?” The second question is: “How rapidly will the reaction occur?” A reaction that takes 50 years to produce a product is about as useful as one that never gives a product at all. A third question is often asked when investigating reactions in greater detail: “What specific molecular-level processes take place as the reaction occurs?” Knowing the answer to this question is of practical importance when the yield or rate of a reaction needs to be controlled. -
Spring 2013 Lecture 13-14
CHM333 LECTURE 13 – 14: 2/13 – 15/13 SPRING 2013 Professor Christine Hrycyna INTRODUCTION TO ENZYMES • Enzymes are usually proteins (some RNA) • In general, names end with suffix “ase” • Enzymes are catalysts – increase the rate of a reaction – not consumed by the reaction – act repeatedly to increase the rate of reactions – Enzymes are often very “specific” – promote only 1 particular reaction – Reactants also called “substrates” of enzyme catalyst rate enhancement non-enzymatic (Pd) 102-104 fold enzymatic up to 1020 fold • How much is 1020 fold? catalyst time for reaction yes 1 second no 3 x 1012 years • 3 x 1012 years is 500 times the age of the earth! Carbonic Anhydrase Tissues ! + CO2 +H2O HCO3− +H "Lungs and Kidney 107 rate enhancement Facilitates the transfer of carbon dioxide from tissues to blood and from blood to alveolar air Many enzyme names end in –ase 89 CHM333 LECTURE 13 – 14: 2/13 – 15/13 SPRING 2013 Professor Christine Hrycyna Why Enzymes? • Accelerate and control the rates of vitally important biochemical reactions • Greater reaction specificity • Milder reaction conditions • Capacity for regulation • Enzymes are the agents of metabolic function. • Metabolites have many potential pathways • Enzymes make the desired one most favorable • Enzymes are necessary for life to exist – otherwise reactions would occur too slowly for a metabolizing organis • Enzymes DO NOT change the equilibrium constant of a reaction (accelerates the rates of the forward and reverse reactions equally) • Enzymes DO NOT alter the standard free energy change, (ΔG°) of a reaction 1. ΔG° = amount of energy consumed or liberated in the reaction 2. -
Eyring Activation Energy Analysis of Acetic Anhydride Hydrolysis in Acetonitrile Cosolvent Systems Nathan Mitchell East Tennessee State University
East Tennessee State University Digital Commons @ East Tennessee State University Electronic Theses and Dissertations Student Works 5-2018 Eyring Activation Energy Analysis of Acetic Anhydride Hydrolysis in Acetonitrile Cosolvent Systems Nathan Mitchell East Tennessee State University Follow this and additional works at: https://dc.etsu.edu/etd Part of the Analytical Chemistry Commons Recommended Citation Mitchell, Nathan, "Eyring Activation Energy Analysis of Acetic Anhydride Hydrolysis in Acetonitrile Cosolvent Systems" (2018). Electronic Theses and Dissertations. Paper 3430. https://dc.etsu.edu/etd/3430 This Thesis - Open Access is brought to you for free and open access by the Student Works at Digital Commons @ East Tennessee State University. It has been accepted for inclusion in Electronic Theses and Dissertations by an authorized administrator of Digital Commons @ East Tennessee State University. For more information, please contact [email protected]. Eyring Activation Energy Analysis of Acetic Anhydride Hydrolysis in Acetonitrile Cosolvent Systems ________________________ A thesis presented to the faculty of the Department of Chemistry East Tennessee State University In partial fulfillment of the requirements for the degree Master of Science in Chemistry ______________________ by Nathan Mitchell May 2018 _____________________ Dr. Dane Scott, Chair Dr. Greg Bishop Dr. Marina Roginskaya Keywords: Thermodynamic Analysis, Hydrolysis, Linear Solvent Energy Relationships, Cosolvent Systems, Acetonitrile ABSTRACT Eyring Activation Energy Analysis of Acetic Anhydride Hydrolysis in Acetonitrile Cosolvent Systems by Nathan Mitchell Acetic anhydride hydrolysis in water is considered a standard reaction for investigating activation energy parameters using cosolvents. Hydrolysis in water/acetonitrile cosolvent is monitored by measuring pH vs. time at temperatures from 15.0 to 40.0 °C and mole fraction of water from 1 to 0.750.