예제 #1
0
def saturated_hydrostatic_balance(state,
                                  theta_e,
                                  mr_t,
                                  exner0=None,
                                  top=False,
                                  exner_boundary=Constant(1.0),
                                  max_outer_solve_count=40,
                                  max_theta_solve_count=5,
                                  max_inner_solve_count=3):
    """
    Given a wet equivalent potential temperature, theta_e, and the total moisture
    content, mr_t, compute a hydrostatically balance virtual potential temperature,
    dry density and water vapour profile.

    The general strategy is to split up the solving into two steps:
    1) finding rho to balance the theta profile
    2) finding theta_v and r_v to get back theta_e and saturation
    We iteratively solve these steps until we (hopefully)
    converge to a solution.

    :arg state: The :class:`State` object.
    :arg theta_e: The initial wet equivalent potential temperature profile.
    :arg mr_t: The total water pseudo-mixing ratio profile.
    :arg exner0: Optional function to put exner pressure into.
    :arg top: If True, set a boundary condition at the top, otherwise
              it will be at the bottom.
    :arg exner_boundary: The value of exner on the specified boundary.
    :arg max_outer_solve_count: Max number of outer iterations for balance solver.
    :arg max_theta_solve_count: Max number of iterations for theta solver (middle part of solve).
    :arg max_inner_solve_count: Max number of iterations on the inner most
                                loop for the water vapour solver.
    """

    theta0 = state.fields('theta')
    rho0 = state.fields('rho')
    mr_v0 = state.fields('vapour_mixing_ratio')

    # Calculate hydrostatic exner pressure
    Vt = theta0.function_space()
    Vr = rho0.function_space()

    VDG = state.spaces("DG")
    if any(deg > 2 for deg in VDG.ufl_element().degree()):
        logger.warning(
            "default quadrature degree most likely not sufficient for this degree element"
        )

    theta0.interpolate(theta_e)
    mr_v0.interpolate(mr_t)

    v_deg = Vr.ufl_element().degree()[1]
    if v_deg == 0:
        boundary_method = Boundary_Method.physics
    else:
        boundary_method = None
    rho_h = Function(Vr)
    Vt_broken = FunctionSpace(state.mesh, BrokenElement(Vt.ufl_element()))
    rho_averaged = Function(Vt)
    rho_recoverer = Recoverer(rho0,
                              rho_averaged,
                              VDG=Vt_broken,
                              boundary_method=boundary_method)
    w_h = Function(Vt)
    theta_h = Function(Vt)
    theta_e_test = Function(Vt)
    delta = 0.8

    # expressions for finding theta0 and mr_v0 from theta_e and mr_t
    exner = thermodynamics.exner_pressure(state.parameters, rho_averaged,
                                          theta0)
    p = thermodynamics.p(state.parameters, exner)
    T = thermodynamics.T(state.parameters, theta0, exner, mr_v0)
    r_v_expr = thermodynamics.r_sat(state.parameters, T, p)
    theta_e_expr = thermodynamics.theta_e(state.parameters, T, p, mr_v0, mr_t)

    for i in range(max_outer_solve_count):
        # solve for rho with theta_vd and w_v guesses
        compressible_hydrostatic_balance(state,
                                         theta0,
                                         rho_h,
                                         top=top,
                                         exner_boundary=exner_boundary,
                                         mr_t=mr_t,
                                         solve_for_rho=True)

        # damp solution
        rho0.assign(rho0 * (1 - delta) + delta * rho_h)

        theta_e_test.assign(theta_e_expr)
        if errornorm(theta_e_test, theta_e) < 1e-8:
            break

        # calculate averaged rho
        rho_recoverer.project()

        # now solve for r_v
        for j in range(max_theta_solve_count):
            theta_h.interpolate(theta_e / theta_e_expr * theta0)
            theta0.assign(theta0 * (1 - delta) + delta * theta_h)

            # break when close enough
            if errornorm(theta_e_test, theta_e) < 1e-6:
                break
            for k in range(max_inner_solve_count):
                w_h.interpolate(r_v_expr)
                mr_v0.assign(mr_v0 * (1 - delta) + delta * w_h)

                # break when close enough
                theta_e_test.assign(theta_e_expr)
                if errornorm(theta_e_test, theta_e) < 1e-6:
                    break

        if i == max_outer_solve_count:
            raise RuntimeError(
                'Hydrostatic balance solve has not converged within %i' % i,
                'iterations')

    if exner0 is not None:
        exner = thermodynamics.exner(state.parameters, rho0, theta0)
        exner0.interpolate(exner)

    # do one extra solve for rho
    compressible_hydrostatic_balance(state,
                                     theta0,
                                     rho0,
                                     top=top,
                                     exner_boundary=exner_boundary,
                                     mr_t=mr_t,
                                     solve_for_rho=True)
예제 #2
0
파일: physics.py 프로젝트: jtessier10/gusto
    def __init__(self, state, iterations=1):
        super().__init__(state)

        self.iterations = iterations
        # obtain our fields
        self.theta = state.fields('theta')
        self.water_v = state.fields('water_v')
        self.water_c = state.fields('water_c')
        rho = state.fields('rho')
        try:
            rain = state.fields('rain')
            water_l = self.water_c + rain
        except NotImplementedError:
            water_l = self.water_c

        # declare function space
        Vt = self.theta.function_space()

        # make rho variables
        # we recover rho into theta space
        if state.vertical_degree == 0 and state.horizontal_degree == 0:
            boundary_method = Boundary_Method.physics
        else:
            boundary_method = None
        Vt_broken = FunctionSpace(state.mesh, BrokenElement(Vt.ufl_element()))
        rho_averaged = Function(Vt)
        self.rho_recoverer = Recoverer(rho,
                                       rho_averaged,
                                       VDG=Vt_broken,
                                       boundary_method=boundary_method)

        # define some parameters as attributes
        dt = state.timestepping.dt
        R_d = state.parameters.R_d
        cp = state.parameters.cp
        cv = state.parameters.cv
        c_pv = state.parameters.c_pv
        c_pl = state.parameters.c_pl
        c_vv = state.parameters.c_vv
        R_v = state.parameters.R_v

        # make useful fields
        Pi = thermodynamics.pi(state.parameters, rho_averaged, self.theta)
        T = thermodynamics.T(state.parameters,
                             self.theta,
                             Pi,
                             r_v=self.water_v)
        p = thermodynamics.p(state.parameters, Pi)
        L_v = thermodynamics.Lv(state.parameters, T)
        R_m = R_d + R_v * self.water_v
        c_pml = cp + c_pv * self.water_v + c_pl * water_l
        c_vml = cv + c_vv * self.water_v + c_pl * water_l

        # use Teten's formula to calculate w_sat
        w_sat = thermodynamics.r_sat(state.parameters, T, p)

        # make appropriate condensation rate
        dot_r_cond = ((self.water_v - w_sat) / (dt * (1.0 +
                                                      ((L_v**2.0 * w_sat) /
                                                       (cp * R_v * T**2.0)))))

        # make cond_rate function, that needs to be the same for all updates in one time step
        cond_rate = Function(Vt)

        # adjust cond rate so negative concentrations don't occur
        self.lim_cond_rate = Interpolator(
            conditional(dot_r_cond < 0,
                        max_value(dot_r_cond, -self.water_c / dt),
                        min_value(dot_r_cond, self.water_v / dt)), cond_rate)

        # tell the prognostic fields what to update to
        self.water_v_new = Interpolator(self.water_v - dt * cond_rate, Vt)
        self.water_c_new = Interpolator(self.water_c + dt * cond_rate, Vt)
        self.theta_new = Interpolator(
            self.theta * (1.0 + dt * cond_rate *
                          (cv * L_v / (c_vml * cp * T) - R_v * cv * c_pml /
                           (R_m * cp * c_vml))), Vt)
예제 #3
0
# find perturbed water_v
w_v = Function(Vt)
phi = TestFunction(Vt)
rho_averaged = Function(Vt)
rho_recoverer = Recoverer(rho0,
                          rho_averaged,
                          VDG=FunctionSpace(mesh,
                                            BrokenElement(Vt.ufl_element())),
                          boundary_method=physics_boundary_method)
rho_recoverer.project()

exner = thermodynamics.exner_pressure(state.parameters, rho_averaged, theta0)
p = thermodynamics.p(state.parameters, exner)
T = thermodynamics.T(state.parameters, theta0, exner, r_v=w_v)
w_sat = thermodynamics.r_sat(state.parameters, T, p)

w_functional = (phi * w_v * dxp - phi * w_sat * dxp)
w_problem = NonlinearVariationalProblem(w_functional, w_v)
w_solver = NonlinearVariationalSolver(w_problem)
w_solver.solve()

water_v0.assign(w_v)
water_c0.assign(water_t - water_v0)

state.set_reference_profiles([('rho', rho_b), ('theta', theta_b),
                              ('vapour_mixing_ratio', water_vb)])

rho_opts = None
theta_opts = EmbeddedDGOptions()
u_transport = ImplicitMidpoint(state, "u")
예제 #4
0
파일: physics.py 프로젝트: jtessier10/gusto
    def __init__(self, state):
        super().__init__(state)

        # obtain our fields
        self.theta = state.fields('theta')
        self.water_v = state.fields('water_v')
        self.rain = state.fields('rain')
        rho = state.fields('rho')
        try:
            water_c = state.fields('water_c')
            water_l = self.rain + water_c
        except NotImplementedError:
            water_l = self.rain

        # declare function space
        Vt = self.theta.function_space()

        # make rho variables
        # we recover rho into theta space
        if state.vertical_degree == 0 and state.horizontal_degree == 0:
            boundary_method = Boundary_Method.physics
        else:
            boundary_method = None
        Vt_broken = FunctionSpace(state.mesh, BrokenElement(Vt.ufl_element()))
        rho_averaged = Function(Vt)
        self.rho_recoverer = Recoverer(rho,
                                       rho_averaged,
                                       VDG=Vt_broken,
                                       boundary_method=boundary_method)

        # define some parameters as attributes
        dt = state.timestepping.dt
        R_d = state.parameters.R_d
        cp = state.parameters.cp
        cv = state.parameters.cv
        c_pv = state.parameters.c_pv
        c_pl = state.parameters.c_pl
        c_vv = state.parameters.c_vv
        R_v = state.parameters.R_v

        # make useful fields
        Pi = thermodynamics.pi(state.parameters, rho_averaged, self.theta)
        T = thermodynamics.T(state.parameters,
                             self.theta,
                             Pi,
                             r_v=self.water_v)
        p = thermodynamics.p(state.parameters, Pi)
        L_v = thermodynamics.Lv(state.parameters, T)
        R_m = R_d + R_v * self.water_v
        c_pml = cp + c_pv * self.water_v + c_pl * water_l
        c_vml = cv + c_vv * self.water_v + c_pl * water_l

        # use Teten's formula to calculate w_sat
        w_sat = thermodynamics.r_sat(state.parameters, T, p)

        # expression for ventilation factor
        a = Constant(1.6)
        b = Constant(124.9)
        c = Constant(0.2046)
        C = a + b * (rho_averaged * self.rain)**c

        # make appropriate condensation rate
        f = Constant(5.4e5)
        g = Constant(2.55e6)
        h = Constant(0.525)
        dot_r_evap = (((1 - self.water_v / w_sat) * C *
                       (rho_averaged * self.rain)**h) /
                      (rho_averaged * (f + g / (p * w_sat))))

        # make evap_rate function, needs to be the same for all updates in one time step
        evap_rate = Function(Vt)

        # adjust evap rate so negative rain doesn't occur
        self.lim_evap_rate = Interpolator(
            conditional(
                dot_r_evap < 0, 0.0,
                conditional(self.rain < 0.0, 0.0,
                            min_value(dot_r_evap, self.rain / dt))), evap_rate)

        # tell the prognostic fields what to update to
        self.water_v_new = Interpolator(self.water_v + dt * evap_rate, Vt)
        self.rain_new = Interpolator(self.rain - dt * evap_rate, Vt)
        self.theta_new = Interpolator(
            self.theta * (1.0 - dt * evap_rate *
                          (cv * L_v / (c_vml * cp * T) - R_v * cv * c_pml /
                           (R_m * cp * c_vml))), Vt)
예제 #5
0
def moist_hydrostatic_balance(state, theta_e, water_t, pi_boundary=Constant(1.0)):
    """
    Given a wet equivalent potential temperature, theta_e, and the total moisture
    content, water_t, compute a hydrostatically balance virtual potential temperature,
    dry density and water vapour profile.
    :arg state: The :class:`State` object.
    :arg theta_e: The initial wet equivalent potential temperature profile.
    :arg water_t: The total water pseudo-mixing ratio profile.
    :arg pi_boundary: the value of pi on the lower boundary of the domain.
    """

    theta0 = state.fields('theta')
    rho0 = state.fields('rho')
    water_v0 = state.fields('water_v')

    # Calculate hydrostatic Pi
    Vt = theta0.function_space()
    Vr = rho0.function_space()
    Vv = state.fields('u').function_space()
    n = FacetNormal(state.mesh)
    g = state.parameters.g
    cp = state.parameters.cp
    R_d = state.parameters.R_d
    p_0 = state.parameters.p_0

    VDG = state.spaces("DG")
    if any(deg > 2 for deg in VDG.ufl_element().degree()):
        state.logger.warning("default quadrature degree most likely not sufficient for this degree element")
    quadrature_degree = (5, 5)

    params = {'ksp_type': 'preonly',
              'ksp_monitor_true_residual': True,
              'ksp_converged_reason': True,
              'snes_converged_reason': True,
              'ksp_max_it': 100,
              'mat_type': 'aij',
              'pc_type': 'lu',
              'pc_factor_mat_solver_type': 'mumps'}

    theta0.interpolate(theta_e)
    water_v0.interpolate(water_t)
    Pi = Function(Vr)
    epsilon = 0.9  # relaxation constant

    # set up mixed space
    Z = MixedFunctionSpace((Vt, Vt))
    z = Function(Z)

    gamma, phi = TestFunctions(Z)

    theta_v, w_v = z.split()

    # give first guesses for trial functions
    theta_v.assign(theta0)
    w_v.assign(water_v0)

    theta_v, w_v = split(z)

    # define variables
    T = thermodynamics.T(state.parameters, theta_v, Pi, r_v=w_v)
    p = thermodynamics.p(state.parameters, Pi)
    w_sat = thermodynamics.r_sat(state.parameters, T, p)

    dxp = dx(degree=(quadrature_degree))

    # set up weak form of theta_e and w_sat equations
    F = (-gamma * theta_e * dxp
         + gamma * thermodynamics.theta_e(state.parameters, T, p, w_v, water_t) * dxp
         - phi * w_v * dxp
         + phi * w_sat * dxp)

    problem = NonlinearVariationalProblem(F, z)
    solver = NonlinearVariationalSolver(problem, solver_parameters=params)

    theta_v, w_v = z.split()

    Pi_h = Function(Vr).interpolate((p / p_0) ** (R_d / cp))

    # solve for Pi with theta_v and w_v constant
    # then solve for theta_v and w_v with Pi constant
    for i in range(5):
        compressible_hydrostatic_balance(state, theta0, rho0, pi0=Pi_h, water_t=water_t)
        Pi.assign(Pi * (1 - epsilon) + epsilon * Pi_h)
        solver.solve()
        theta0.assign(theta0 * (1 - epsilon) + epsilon * theta_v)
        water_v0.assign(water_v0 * (1 - epsilon) + epsilon * w_v)

    # now begin on Newton solver, setup up new mixed space
    Z = MixedFunctionSpace((Vt, Vt, Vr, Vv))
    z = Function(Z)

    gamma, phi, psi, w = TestFunctions(Z)

    theta_v, w_v, pi, v = z.split()

    # use previous values as first guesses for newton solver
    theta_v.assign(theta0)
    w_v.assign(water_v0)
    pi.assign(Pi)

    theta_v, w_v, pi, v = split(z)

    # define variables
    T = thermodynamics.T(state.parameters, theta_v, pi, r_v=w_v)
    p = thermodynamics.p(state.parameters, pi)
    w_sat = thermodynamics.r_sat(state.parameters, T, p)

    F = (-gamma * theta_e * dxp
         + gamma * thermodynamics.theta_e(state.parameters, T, p, w_v, water_t) * dxp
         - phi * w_v * dxp
         + phi * w_sat * dxp
         + cp * inner(v, w) * dxp
         - cp * div(w * theta_v / (1.0 + water_t)) * pi * dxp
         + psi * div(theta_v * v / (1.0 + water_t)) * dxp
         + cp * inner(w, n) * pi_boundary * theta_v / (1.0 + water_t) * ds_b
         + g * inner(w, state.k) * dxp)

    bcs = [DirichletBC(Z.sub(3), 0.0, "top")]

    problem = NonlinearVariationalProblem(F, z, bcs=bcs)
    solver = NonlinearVariationalSolver(problem, solver_parameters=params)

    solver.solve()

    theta_v, w_v, pi, v = z.split()

    # assign final values
    theta0.assign(theta_v)
    water_v0.assign(w_v)

    # find rho
    compressible_hydrostatic_balance(state, theta0, rho0, water_t=water_t, solve_for_rho=True)