view +rv/+time/RungekuttaInteriorRv.m @ 1142:cff49fba3cc8 rv-interpolation

Closing branch
author Vidar Stiernström <vidar.stiernstrom@it.uu.se>
date Mon, 05 Aug 2019 10:49:21 +0200
parents 2ef20d00b386
children 010bb2677230
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classdef RungekuttaInteriorRv < time.Timestepper
    properties
        F       % RHS of the ODE
        k       % Time step
        t       % Time point
        v       % Solution vector
        n       % Time level
        coeffs  % The coefficents used for the RK time integration
        RV      % Residual Viscosity
        DvDt    % Function for computing the time deriative used for the RV evaluation

        % Convenience properties. Only for plotting
        viscosity % Total viscosity
        residualViscosity % Residual viscosity
        firstOrderViscosity % first order viscosity
        dvdt % Evaluated time derivative in residual
        Df % Evaluated flux in residual
    end

    methods
        function obj = RungekuttaInteriorRv(F, k, t0, v0, RV, DvDt, order)
            obj.F = F;
            obj.k = k;
            obj.t = t0;
            obj.v = v0;
            obj.n = 0;
            % Extract the coefficients for the specified order
            % used for the RK updates from the Butcher tableua.
            [s,a,b,c] = time.rk.butcherTableau(order);
            obj.coeffs = struct('s',s,'a',a,'b',b,'c',c);
            obj.RV = RV;
            obj.DvDt = DvDt;
            obj.dvdt = obj.DvDt(obj.v);
            [obj.viscosity,  obj.Df, obj.firstOrderViscosity, obj.residualViscosity] = obj.RV.evaluate(obj.v,obj.dvdt);
        end

        function [v, t] = getV(obj)
            v = obj.v;
            t = obj.t;
        end

        function state = getState(obj)
            state = struct('v', obj.v, 'dvdt', obj.dvdt, 'Df', obj.Df, 'viscosity', obj.viscosity, 'residualViscosity', obj.residualViscosity, 'firstOrderViscosity', obj.firstOrderViscosity, 't', obj.t);
        end

        function obj = step(obj)
            obj.v = rv.time.rungekuttaRV(obj.v, obj.t, obj.k, obj.F, obj.RV, obj.DvDt, obj.coeffs);
            obj.t = obj.t + obj.k;
            obj.n = obj.n + 1;
            obj.dvdt = obj.DvDt(obj.v);
            [obj.viscosity,  obj.Df, obj.firstOrderViscosity, obj.residualViscosity] = obj.RV.evaluate(obj.v,obj.dvdt);
        end
    end
end