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Thermodynamics Physical  Observe relative stability of states  differences  Static comparisons of states Lecture 4 Kinetics Introduction to  Observe changes of state over  Several different topics  Empirical description of the rate of reaction  Determination of experimental parameters  Microscopic theories

Rates Reaction velocity A is described by an The rates of appearance of products and equation of the type disappearance of reactants are related by 1 of the reaction H()  O () gas H O ( ) 2222 Define the reaction velocity, v, in terms of Rates: “normalized” rates of appearance of products and disappearance of reactants  Rate of change of [H2O]: d[H2O]/dt  Rate of change of [H ]: d[H ]/dt 1 di[] 2 2 v   Rate of change of [O ]: d[O ]/dt 2 2 i dt Rates related by the overall equation Example of the production of water:  1 oxygen disappears for every 2 dH[]dO []dHO [ ] hydrogen in the above reaction v 222 2  dt dt dt

Rate laws Order

Describe of how reaction velocity depends on In many situations, one may write the functional parameters such as , form of the reaction velocity approximately as vkABC [][][]abc , , etc. a, b, c are the orders of reaction under the vfABTP ([react ],[ prod ], , ) conditions examined May be simple or complex Many reaction velocities are more complicated functions than the simple one above Gives insight into the manner in which the  Example: Production of HBr over a wide range reaction occurs 12/ [][]HBr22  Reactions do not necessarily occur in the manner vk HBr []HBr indicated by the overall reaction equation 1 k' []Br2 Orders are often determined over a limited range  Initial order of reaction Differential method of Determining initial order determining order

Calculate approximate derivatives as ratios of Measure initial velocity as a function of the differences for specific concentrations amount of reactants in the Plot approximate derivatives versus Example: OCl- + I-  OI- + Cl- [OCl- ] [I-] [OH-] Initial velocity ln(v)  k  nln(C) 0.0017 0.0017 1.00 1.75  10-4 0.0034 0.0017 1.00 3.50  10-4 0.0017 0.0034 1.00 3.50  10-4 0.0017 0.0017 0.50 3.50  10-4 Concentrations are in mol dm-3. Rate is mol dm-3 sec-1.

By comparison, one finds the initial rate Example: Decomposition of di-tert-butyl peroxide equation  Line slope = 1.04    1 vinitial k[OCl ][I ][OH ]  Order with respect to DTBP is close to 1 under these conditions (and probably is 1)

Integrated rate laws - first order in a reactant First-order rate law

For simple chemical reactions, integrate the Example: rate laws to determine decomposition of di- how the reactant dA[] v  kA[] tert-butyl peroxide dt 1 concentration changes slope  -k with time 1

First-order rate law [At ( )] [ A (0 )] exp( kt1 ) Rate constant for

 Exponential in time this reaction is

 Linear form is the ln [At ( )] ln  [ A (0 )]  kt1 determined to be logarithm -1 k1 = 0.0193 min from the slope of the line

Reactant or ? First-order Product

What if one can only Example: First-order Rely on conservation of matter measure a product reaction [B(t)]  [A(0)]  [A(t)] concentration with A  B  [A(0)]  [A(0)]ekt time? Then Sometimes one can kt d[B] d[A]  [A(0)] (1  e ) derive an equation   for the product dt dt Rearrange to find the linear form concentration with Can solve for the [A(0)]  [B(t)] time concentration of B ln( )   kt exactly [A(0)] Integrated rate law – second order in reactant (Case I) Second-order rate law Second-order rate 1 dA[] 2 Example: law may be v  kA[] 2 dt 2 integrated  Collision-induced decomposition of Linear plot of 11 diacetylene, DA 2 kt2 1/[A(t)] versus t [At ( )] [ A (0 )]  Hou and Palmer, Often see reported 1965 rate constant for 1 Linear plot of [DA]-1 kt disappearance of A [()]A 0 eff versus t  k = 2 k 7 eff 2 keff = 6.79 x10  Exercise caution in cm3/mol-sec assessing reported rate constants

Integrated rate laws for other Second-order rate law reactant orders (Case II)

A + B Products Integration gives a Previously considered general form for all  Homomolecular v  k [A][B] orders (except 1) reaction ( A + A) 2 d[A] d[B] v     The power of the 1  If other species dt dt [A(t)]  [A]  x [B(t)]  [B]  x function of affected reaction, 0 0 concentration linear they were held dx 1  k [A]  x [B]  x 1 constant dt 2 0 0 in time is related to 0  [A(t)]  [A]  order of reaction for Consider second-order ln   ln 0   [B]  [A] k t  [B(t)]  [B]  0 0 2 the conditions under heteromolecular    0  which the system is  Second order overall . Does not for observed  First order in each [A]0 = [B]0 reactant

Determining kinetic Half life parameters

Can describe time First order Two conceptual steps dependence in several  Find parameter proportional to concentration different ways ln 2  Find appropriate function of time to allow  Rate constant, k t1/ 2  evaluation of time course  Half life, t , time for one 1/2 k Parameter often measured Parameter needed half of reactant to

Gas P, total pressure Pi, of disappear Second order reactant  Other that describe Total optical absorption Absorption of a single the amount left 1 component Total conductance Conductance of a single t1/2  component k [A(0)] Total Volume change of a eff single component Concentration of a single component Summary Chemical change quantified by the mathematics of chemical kinetics Rate constant and order characterize a reaction Determining rates and velocities  Differential method  Integrated-rate-law method Results often limited to a particular time scale or situation  Initial reaction  With some materials in excess