Lecture Recap, CHEM 162 9/22-9/23 Hº compares product stability to reactant stability. Hº compares product bond strengths to reactant bond strengths. At constant temperature (T = 0), a chemical system that absorbs or releases energy, gains or loses chemical potential energy, respectively. Source of chemical potential energy: electrostatic attraction of bonding electrons to mutual nuclei. Temperature is a measure of the average kinetic energy of a system of particles. Rate of Rxn typically increases with: Increasing concentration Increasing temperature A Catalyst Decreasing complexity of particle geometry Atomic Theory necessarily predicts a Collision Theory of Kinetics: Increasing concentration Increasing temperature A Catalyst Decreasing complexity of particle geometry Increasing Frequency of Collisions Increasing Energy of Collisions Increasing Frequency of Collisions Majority of productive collisions are less dependent on trajectory 9/24-9/26 A mechanism is one or more elementary steps indicating how collisions between reactants and intermediates lead to product formation. Any mechanism whose elementary steps do not sum to the overall balanced equation can be eliminated. Multiple mechanisms can and should be proposed for a chemical reaction. Experiment is used to eliminate some or all. Mechanisms can not be proved. For the balanced equation, aA + bB cC + dD: rate of reaction = 1 a A t 1 b B t 1 c C t 1 d D t = 1/a * the rate of disappearance of A = 1/b * the rate of disappearance of B = 1/c * the rate of formation of C = 1/d * the rate of formation of D Method of Initial Rates More typically the concentration of a reactant, rather than that of a product, is monitored over time. The tangent line slope at t = 0 in a concentration vs. time curve yields the instantaneous initial rate. An equilibrium condition is typically not allowed to occur. Experimental Rate Law and Order of Reactant Concentration Using the method of initial rates, a reactant’s concentration is varied, all other things being equal, to see how the initial rate is affected. If no rate change is observed when concentration is changed then the reaction is zeroth (0th) order in the reactant concentration. If the rate is directly proportional to the concentration the reaction is first (1st) order in the reactant concentration. If the rate is directly proportional to the square of the concentration the reaction is second (2nd) order in the reactant concentration. Once all reactant concentration orders are experimentally determined an experimental rate law can be written: rate = k[A]x[B]y for the reaction A + B products, where k is the average rate constant calculated from all trials, i.e. k = rate/[A]x[B]y. A rate law simply shows how rate varies with concentration. From collision theory it is known that rate concentration, from experiment, rate (concentration)x, where x = 0, 1, 2. 9/29-10/1 Method of Integrated Rate Laws Two equivalent expressions of rate can be manipulated to derive a differential equation that can be integrated over concentration and time ranges. A Rate = = k[ A] x t A = kt [ A] x [ A] = x [ A ]0 [ A] [ A ]t t kt t0 The integration yields linear equations whose slope k. These equations allow one to find the concentration of a reactant at any time. 0th [ A]t kt [ A]0 1st ln[ A]t kt ln[ A]0 2nd 1 1 kt [ A]t [ A]0 Both the initial rate and integrated rate methods produce a rate law. The latter can generate additional information, i.e. concentration at any time. Half-life Half-life is the time for ½ of the starting material to disappear. It can be calculated for each order by solving the integrated rate law for time when [A]t = [A]0/2 0th t½ = [ A]0 2k 1st t½ = ln 2 k 2nd t½ = 1 k [ A]0 half-life is constant Methods for Determining Reactant Concentration Order Graphical: Plot [A] vs. time. A linear plot with negative slope suggests 0th order. A curved plot is either 1st or 2nd order. Plot ln[A] vs. time. A linear plot with negative slope suggests 1st order. Plot 1/[A] vs. time if needed a linear plot with positive slope suggests 2nd order. Experimental data could suggest all orders are possible. In this case the “best line” wins, i.e. the linear plot with R2 closest to 1. 100 2 R = 0.9874 -4.2 Raw Data Linear (Raw Data) -4.3 -4.4 Raw Data -4.5 Linear (Raw Data) -4.6 -4.8 50 time (min) 100 2 R = 0.9996 120 100 80 Raw Data 60 Linear (Raw Data) 40 20 -4.7 0 y = 0.8756x + 59.146 140 y = -0.0101x - 4.1131 50 1/[C 4H6], M-1 -4 -4.1 0 2 R = 0.9551 ln[C4H6] [C 4H6] (M) y = -0.0001x + 0.0161 0.018 0.016 0.014 0.012 0.01 0.008 0.006 0.004 0.002 0 Kinetic Profile for the Dimerization of 1,3-butadiene Kinetic Profile for the Dimerization of 1,3-butadiene Kinetic Profile for the Dimerization of 1,3-butadiene 0 0 -4.9 time (min) 50 100 time (min) Half-Life: This method allows for a quick assessment of order by inspecting the concentration and time data. Compare successive half-lives. Each successive half-life will be ½ that of the previous one, the same as the previous one, and double the previous one for 0th, 1st, and 2nd order, respectively. Often times perfect half way points are not available so use this method with care. Constant k: Calculate three values of k using an integrated rate law. Typically it’s best to pick data from the beginning, middle, and end of a kinetic run. A particular order is supported if the k values are the same within experimental error (significant figures)