United States Environmental Protection Agency Environmental Research Laboratory Athens GA 30613 Research and Development EPA-600/S3-82-049 Sept. 1982 Project Summary Analysis of Mathematical Models for Pollutant Transport and Dissipation W. F. Ames Four realistic nonlinear models of pollutant transport with turbulent diffusion and reaction in rivers were studied. Exact solutions for all the kinetics models (no transport, no diffusion — the so-called stirred tank reactor) are described. An algorithm for calculating the rate constantsf rom the exact solutions is given. Exact solutions for all systems are also provided when transport terms are included with the kinetics (plug flow model). The inclusion of turbulent diffusion prevents exact solution, but the methods of perturbation and the maximum (minimum) principle provide approximate solutions and bounds on the traveling wave solution. The steady state is also analyzed by the bounding technique. These bounds, which may be used independently, demonstrate how the various param- eters affect the solutions. This Project Summary was developed by EPA's Environmental Research Laboratory. Athens. GA, to announce key findings of the research project that is fully documented in a separate report of the same title (see Project Report ordering information at back). Introduction Mathematical models of pollutant reaction, diffusion and transport in rivers and streams are nonlinear partial differential equations, primarily because of the nonlinear kinetics of the bio- chemical reactions. In previous studies, exact solutions have been given for, at most, simplified and/or linearized problems. These solutions, usually, are not good approximations for the true situation. For the nonlinear problems, numerical solutions are usually obtained. Although often useful, numerical solu- tions are not easily employable in analyzing the adequacy of a model and evaluating parameters. Numerical solutions, without error analysis, must be viewed with caution and even suspicion — doubly so for nonlinear problems that may develop singularities, bifurcations, etc. In this study, four realistic models of pollutant transport, turbulent diffusion and reaction are employed. In the absence of turbulent diffusion and transport, the kinetic equations are solved exactly in all four cases. When transport is added, the equations are also solved in all four cases. For the full system, exact solutions do not seem possible. For travelling wave problems, however, models I and II can be exactly solved for the active carbon and the bacteria and approximately for the pollutant. For all travelling wave cases and all steady state cases, upper and lower bounds involving all parameters of the problem are constructed using the maximum (minimum) principle. These bounds are simple negative exponentials and may be used independently — that is, they are not coupled together as are the equations. This is the most useful and interesting result to come out of this work. ------- Procedure With C,, i =1,2,3 as the concentra- tions of pesticide, bacteria and organic carbon; D,, i = 1,2,3 as the respective diffusion coefficients; k,, i = 1,2,3 as the appropriate rate constants; v as the mean stream velocity; T asthe time; and x as the distance along the river, the model equations are: dr dx. 9x2 9C2 + y 9C2 - dr dx 3x2 9r ax- i+k3f3(Ci, c2,c3) dx2 Model I: fi = CiC2, f2 = fa = Model II: fi ^ CiC2C3, fa = fa = C2C3 Model III: fi = C,C2, K + C3 Model IV: fi = CiC2 C3, The analysis had four stages. 1. Stirred tank reactor - Kinetics only. With D, = 0, and V = 0, the kinetic equations are solved exactly using the methods of ordinary differential equations. An algorithm is described for the evaluation of rate constants, which are employed in subsequent analyses. Solutions are displayed for several models. 2. Plug flow reactor - Kinetics and transport. With D, = 0, the transport equations with kinetics are solved exactly using the method of charac- teristics of hyperbolic first order equations. The resulting solutions have a number of arbitrary functions that depend upon initial and/or boundary conditions. 3. The Full System. In this case all physical processes, kinetics, trans- port and turbulent diffusion are included. These parabolic equations admit the important ca.se of travelling wave solutions. In cases I and II, exact solutions are obtainable for the bacteria and active carbon but only a perturbation solution is possible for the pollutant. For all cases uncoupled analytic upper and lower bounds are obtained by means of maximum (minimum) principle. These bounds contain the parameters of the problem and may be used independently. 4. The Steady State. Solutions of the steady state are not obtainable analytically. The maximum (mini- mum) principle is used to derive upper and lower bounds. These bounds contain the parameters of the problems and are uncoupled. In this problem the exact values of parameters, such as rate constants, turbulent diffusion constants, etc. are not known exactly but do lie on an interval- i.e. ,/}33. Interval analysis is employed to obtain information about the solutions in such cases. Summary and Conclusions (1) For four stirred-tank-type kinetic models, dimensional analysis has been applied, dimensionless ki- netic groups obtained, and analytic solutions developed and analyzed. In the case of Model II (third order kinetics for Ci, second order for C2 and C3), the dimensionless equa- tions are also parameter-free. This is an interesting and some- what unusual situation. From an examination of these exact solu- tions, the following limiting results (as t—<») are obtained. Model Number Ci C2 C3 I II III IV 0 •K) 0 0 0 0 0 From the exact solutions for the oft-used Model I, it is shown how these equations can be used to obtain rate constant ratios and the individual rate constants. (2) When transport effects (constant velocity) are included, the resulting first order hyperbolic partial differential equations must be dimensionally analyzed in a man- ner different from the kinetic models. (3) When turbulent dispersion effects are included, the equations be- come coupled reaction-diffusion equations that are parabolic. Dimensional analysis reveals the importance of the reciprocal of a Peclet number (Npe) for mass transport and reaction rate ratios. None of the model equations possess classical similar solutions, but they all possess travelling wave solutions. For Models I and II, a partial exact solution is constructed that can be used to generate a perturbation solution for the pollutant. Both show the subtle way the problem param- eters enter. In particular, the pollutant decays according to the exponential of the negative of the square root of the term NpeE and by a complicated function of A = k3/ ki for Model I (E is a constant of integration). On the other hand, the active carbon decays accord- Ing to the exponential of the negative of the square root of NPe Eks/k,. (4) The complicated functions expe- rienced in the perturbation analy- ses suggested that upper and lower bounds be constructed in terms of simple functions (nega- tive exponentials). This has been done for all travelling wave solutions and for the steady state. Those bounds may be used in- dependently. Moreover, the bounds show how the various parameters affect the solutions. This is the most useful and interesting result to come out of this work. (5) Because none of the parameters are known exactly, interval analy- sis has been used to give deferred interval bounds in which the upper bound lies. Some of the results are verified by computer calculations. ------- W. F. Ames is with Georgia Institute of Technology, Atlanta. GA 30332. James W. Falco is the EPA Project Officer (see below). The complete report, entitled "Analysis of Mathematical Models for Pollutant Transport and Dissipation," (Order No. PB 82-256 900; Cost: $10.50, subject to change) will be available only from: National Technical Information Service 5285 Port Royal Road Springfield, V'A 22161 Telephone: 703-487-4650 The EPA Project Officer can be contacted at: Environmental Research Laboratory U.S. Environmental Protection Agency College Station Road Athens, GA 30613 I U£.GOVERNMENTPRINTimOFFICE: 1«M-559-017/0826 ------- United States Environmental Protection Agency Center for Environmental Research Information Cincinnati OH 45268 Postage and Fees Paid Environmental Protection Agency EPA 335 Official Business Penalty for Private Use $300 ------- |