function periodic_cstr
    %%  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
    %
    % .. math::
    %
    %     \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.
    %
    % Requires: cantera >= 3.2.0
    %
    % .. tags:: Matlab, combustion, reactor network, well-stirred reactor, plotting

    tic
    help periodic_cstr

    %%
    % Create the gas mixture
    gas = ct.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 = ct.zeroD.Reservoir(gas);
    %%
    % Now set the gas to the initial temperature of the reactor, and create
    % the reactor object.
    gas.TP = {t, p};
    cstr = ct.zeroD.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 = ct.zeroD.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 = ct.zeroD.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 * ((ct.OneAtm / gas.P) * (gas.T / 273.15)); % m^3/s
    mdot = gas.massDensity * vdot; % kg/s
    mfc = ct.zeroD.MassFlowController(upstream, cstr);
    mfc.massFlowRate = mdot;
    %%
    % Now create a downstream reservoir to exhaust into.
    downstream = ct.zeroD.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 = ct.zeroD.Valve(cstr, downstream);
    v.valveCoeff = 1.0e-9;
    %%
    % Create the network
    network = ct.zeroD.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

    for i = 2:length(tm)
        if abs(y(3, i-1) - y(3, i)) > (y(3, i-1) * 5)
            disp(tm(i))
        end
    end
    %%
    % Plot results
    clf
    figure(1)
    plot(tm, y)
    legend('H2', 'O2', 'H2O')
    title('Mass Fractions')
    ylabel('Mass Fractions')
    xlabel('Time (s)')

    toc
end
