Continuously stirred tank reactor with periodic behavior

This example illustrates a continuously stirred tank reactor (CSTR) with steady inputs but periodic interior state.

A stoichiometric hydrogen/oxygen mixture is introduced and reacts to produce water. But since water has a large efficiency as a third body in the chain termination reaction

\[\mathrm{ H + O_2 + M \rightleftharpoons HO_2 + M }\]

as soon as a significant amount of water is produced the reaction stops. After enough time has passed that the water is exhausted from the reactor, the mixture explodes again and the process repeats. This explanation can be verified by decreasing the rate for reaction 7 in file h2o2.yaml and re-running the example.

Acknowledgments: The idea for this example and an estimate of the conditions needed to see the oscillations came from Bob Kee, Colorado School of Mines.

Tags: Matlab combustion reactor network well-stirred reactor plotting

function periodic_cstr
    clear all
    close all

    tic
    help periodic_cstr

    % create the gas mixture
    gas = Solution('h2o2.yaml', 'ohmech');

    % pressure = 60 Torr, T = 770 K
    p = 60.0 * 133.3;
    t = 770.0;

    gas.TPX = {300, p, 'H2:2, O2:1'};

    % create an upstream reservoir that will supply the reactor.  The
    % temperature, pressure, and composition of the upstream reservoir are
    % set to those of the 'gas' object at the time the reservoir is
    % created.
    upstream = Reservoir(gas);

    % Now set the gas to the initial temperature of the reactor, and create
    % the reactor object.
    gas.TP = {t, p};
    cstr = IdealGasReactor(gas);

    % Set its volume to 10 cm^3. In this problem, the reactor volume is
    % fixed, so the initial volume is the volume at all later times.
    cstr.V = 10.0 * 1.0e-6;

    % We need to have heat loss to see the oscillations. Create a
    % reservoir to represent the environment, and initialize its
    % temperature to the reactor temperature.
    env = Reservoir(gas);

    % Create a heat-conducting wall between the reactor and the
    % environment. Set its area, and its overall heat transfer
    % coefficient. Larger U causes the reactor to be closer to isothermal.
    % If U is too small, the gas ignites, and the temperature spikes and
    % stays high.
    w = Wall(cstr, env);
    w.area = 1.0;
    w.heatTransferCoeff = 0.02;

    % Connect the upstream reservoir to the reactor with a mass flow
    % controller (constant mdot). Set the mass flow rate to 1.25 sccm.
    sccm = 1.25;
    vdot = sccm * 1.0e-6/60.0 * ((OneAtm / gas.P) * (gas.T / 273.15)); % m^3/s
    mdot = gas.D * vdot; % kg/s
    mfc = MassFlowController(upstream, cstr);
    mfc.massFlowRate = mdot;

    % now create a downstream reservoir to exhaust into.
    downstream = Reservoir(gas);

    % connect the reactor to the downstream reservoir with a valve, and
    % set the coefficient sufficiently large to keep the reactor pressure
    % close to the downstream pressure of 60 Torr.
    v = Valve(cstr, downstream);
    v.valveCoeff = 1.0e-9;

    % create the network
    network = ReactorNet({cstr});

    % now integrate in time
    tme = 0.0;
    dt = 0.1;

    n = 0;

    while tme < 300.0
        n = n + 1;
        tme = tme + dt;
        network.advance(tme);
        tm(n) = tme;
        y(1, n) = cstr.massFraction('H2');
        y(2, n) = cstr.massFraction('O2');
        y(3, n) = cstr.massFraction('H2O');
    end

    clf
    figure(1)
    plot(tm, y)
    legend('H2', 'O2', 'H2O')
    title('Mass Fractions')

    toc
end