def __init__(self, name, T0, sub_comp=[], timer=Timer()):
"""Initalizes a thermal hydraulic super component.
:param name: The name of the supercomponent (i.e., "fuel" or "cool")
:type name: str.
:param T0: The initial temperature of the supercomponent
:type T0: float.
:param sub_comp: List of components that makes up the supercomponent.
The sub_components should be in order from the center to the outside
:type sub_comp: list of THComponent
:param timer: The timer instance for the sim
:type timer: Timer object
"""
THComponent.__init__(self, name=name,
mat=Material(),
vol=0.0*units.meter**3,
T0=T0,
alpha_temp=0*units.delta_k/units.kelvin,
timer=timer,
heatgen=False,
power_tot=0*units.watt,
sph=False,
ri=0*units.meter,
ro=0*units.meter)
self.sub_comp = sub_comp
self.T = units.Quantity(np.zeros(shape=(timer.timesteps(),),
dtype=float), 'kelvin')
self.T[0] = T0
self.conv = {}
self.add_conduction_in_mesh()
self.alpha_temp = 0.0*units.delta_k/units.kelvin
def test_wakao_model():
mat = Material(k=1 * units.watt / units.meter / units.kelvin,
cp=1 * units.joule / units.kg / units.kelvin,
mu=2 * units.pascal * units.second)
h_wakao = ConvectiveModel(mat=mat,
m_flow=1 * units.kg / units.g,
a_flow=1 * units.meter**2,
length_scale=1 * units.meter,
model='wakao')
assert_equal(h_wakao.mu, 2 * units.pascal * units.second)
rho = 100 * units.kg / units.meter**3
assert_equal(h_wakao.h(rho, 0 * units.pascal * units.second),
h_wakao.h(rho, 2 * units.pascal * units.second))
def initialize(self):
print("Initializing program...")
self.renderer = Renderer()
self.scene = Scene()
self.camera = Camera()
# pull camera towards viewer
self.camera.setPosition(0, 0, 7)
geometry = SphereGeometry(radius=3)
vsCode = """
in vec3 vertexPosition;
in vec3 vertexColor;
uniform mat4 modelMatrix;
uniform mat4 viewMatrix;
uniform mat4 projectionMatrix;
out vec3 color;
uniform float time;
void main()
{
float offset = 0.2 * sin(2.0 * vertexPosition.x + time);
vec3 pos = vertexPosition + vec3(0, offset, 0);
gl_Position = projectionMatrix * viewMatrix * modelMatrix * vec4(pos, 1);
color = vertexColor;
}
"""
fsCode = """
in vec3 color;
uniform float time;
out vec4 fragColor;
void main()
{
float r = abs(sin(time));
vec4 c = vec4(r, -0.5*r, -0.5*r, 0);
fragColor = vec4(color , 1) + c;
}
"""
material = Material(vsCode, fsCode)
material.addUniform("float", "time", 0)
material.locateUniforms()
self.time = 0
self.mesh = Mesh(geometry, material)
self.scene.add(self.mesh)
def test_conduction_slab():
mat = Material(k=1 * units.watt / units.meter / units.kelvin)
components = [
th_component.THComponent(mat=mat, T0=700 * units.kelvin),
th_component.THComponent(mat=mat, T0=700 * units.kelvin)
]
th = th_system.THSystem(0, components)
assert_equal(
th.conduction_slab(components[0], components[1], 0, 1 * units.meter,
1 * units.meter**2), 0)
components = [
th_component.THComponent(mat=mat, T0=800 * units.kelvin),
th_component.THComponent(mat=mat, T0=700 * units.kelvin)
]
th = th_system.THSystem(0, components)
assert (th.conduction_slab(components[0], components[1], 0,
1 * units.meter, 1 * units.meter**2) > 0)
def __init__(self,
h0=0 * units.watt / units.meter**2 / units.kelvin,
mat=Material(),
m_flow=None,
a_flow=None,
length_scale=None,
model="constant"):
"""
Initializes the DensityModel object.
:param h0: convective heat transfer coefficient when it's a constant
:type h0: double
:param mat: material of the fluid
:type mat: Material object
:param m_flow: mass flow rate
:type m_flow: double
:param a_flow: flow cross section surface area
:type a_flow: double
:param length_scale: heat transfer length scale
:type length_scale: double
:param model: The keyword for a model type, implemented types are
'constant' and 'wakao'
:type model: string
"""
self.h0 = h0
self.k = mat.k
self.cp = mat.cp
self.mu = mat.mu
self.m_flow = m_flow
self.a_flow = a_flow
self.length_scale = length_scale
self.implemented = {'constant': self.constant, 'wakao': self.wakao}
if model in self.implemented.keys():
self.model = model
else:
self.model = NotImplemented
msg = "Convective heat transfer model type "
msg += model
msg += " is not an implemented convective model. Options are:"
for m in self.implemented.keys():
msg += m
raise ValueError(msg)
def initialize(self):
print("Initializing program...")
self.renderer = Renderer()
self.scene = Scene()
self.camera = Camera()
# pull camera towards viewer
self.camera.setPosition(0, 0, 7)
geometry = SphereGeometry(radius=3)
vsCode = """
in vec3 vertexPosition;
out vec3 position;
uniform mat4 modelMatrix;
uniform mat4 viewMatrix;
uniform mat4 projectionMatrix;
void main()
{
vec4 pos = vec4(vertexPosition, 1);
gl_Position = projectionMatrix * viewMatrix * modelMatrix * pos;
position = vertexPosition;
}
"""
fsCode = """
in vec3 position;
out vec4 fragColor;
void main()
{
vec3 color = fract(position);
fragColor = vec4(color,1);
}
"""
material = Material(vsCode, fsCode)
material.locateUniforms()
self.mesh = Mesh(geometry, material)
self.scene.add(self.mesh)
from reactivity_insertion import RampReactivityInsertion
rho_ext = RampReactivityInsertion(timer=ti,
t_start=60.0 * units.seconds,
t_end=70.0 * units.seconds,
rho_init=0.0 * units.delta_k,
rho_rise=600.0 * units.pcm,
rho_final=600.0 * units.pcm)
# maximum number of internal steps that the ode solver will take
nsteps = 5000
k_mod = random.gauss(17, 17 * 0.05) * units.watt / (units.meter * units.kelvin)
cp_mod = random.gauss(1650.0, 1650.0 * 0.05) * \
units.joule / (units.kg * units.kelvin)
rho_mod = DensityModel(a=1740. * units.kg / (units.meter**3), model="constant")
Moderator = Material('mod', k_mod, cp_mod, dm=rho_mod)
k_fuel = random.uniform(15.0, 19.0) * units.watt / (units.meter * units.kelvin)
cp_fuel = random.gauss(
1818.0, 1818 * 0.05) * units.joule / units.kg / units.kelvin # [J/kg/K]
rho_fuel = DensityModel(a=2220.0 * units.kg / (units.meter**3),
model="constant")
Fuel = Material('fuel', k_fuel, cp_fuel, dm=rho_fuel)
k_shell = random.gauss(17, 17 * 0.05) * units.watt / \
(units.meter * units.kelvin)
cp_shell = random.gauss(
1650.0, 1650.0 * 0.05) * units.joule / (units.kg * units.kelvin)
rho_shell = DensityModel(a=1740. * units.kg / (units.meter**3),
model="constant")
Shell = Material('shell', k_shell, cp_shell, dm=rho_shell)
import th_component as th
from db import database
from utilities.ur import units
from timer import Timer
from materials.material import Material
import density_model
name = "testname"
vol = 20*units.meter**3
k = 10*units.watt/units.meter/units.kelvin
cp = 10*units.joule/units.kg/units.kelvin
dm = density_model.DensityModel(a=0*units.kg/units.meter**3,
b=100*units.kg/units.meter**3,
model='constant')
mat = Material(k=k, cp=cp, dm=dm)
kappa = 0
T0 = 700*units.kelvin
t0 = 0*units.seconds
tf = 10*units.seconds
tfeedback = 5*units.seconds
dt = 0.1*units.seconds
ti = Timer(t0=t0, tf=tf, dt=dt, t_feedback=tfeedback)
tester = th.THComponent(name=name, mat=mat, vol=vol, T0=T0, timer=ti)
tester_sph = th.THComponent(name=name, mat=mat, vol=vol, T0=T0, timer=ti,
sph=True, ri=0*units.meter, ro=1*units.meter)
def test_constructor():
# External Reactivity
from reactivity_insertion import StepReactivityInsertion
rho_ext = StepReactivityInsertion(timer=ti,
t_step=t_feedback + 10.0 * units.seconds,
rho_init=0.0 * units.delta_k,
rho_final=650.0 * 2 * units.pcm)
# maximum number of internal steps that the ode solver will take
nsteps = 5000
mu0 = 0 * units.pascal * units.second
k_mod = 17 * units.watt / (units.meter * units.kelvin)
cp_mod = 1650.0 * units.joule / (units.kg * units.kelvin)
rho_mod = DensityModel(a=1740. * units.kg / (units.meter**3), model="constant")
Moderator = Material('mod', k_mod, cp_mod, mu0, rho_mod)
k_fuel = 15 * units.watt / (units.meter * units.kelvin)
cp_fuel = 1818.0 * units.joule / units.kg / units.kelvin
rho_fuel = DensityModel(a=2220.0 * units.kg / (units.meter**3),
model="constant")
Fuel = Material('fuel', k_fuel, cp_fuel, mu0, rho_fuel)
k_shell = 17 * units.watt / (units.meter * units.kelvin)
cp_shell = 1650.0 * units.joule / (units.kg * units.kelvin)
rho_shell = DensityModel(a=1740. * units.kg / (units.meter**3),
model="constant")
Shell = Material('shell', k_shell, cp_shell, mu0, rho_shell)
k_cool = 1 * units.watt / (units.meter * units.kelvin)
cp_cool = 2415.78 * units.joule / (units.kg * units.kelvin)
def __init__(self, name=None,
mat=Material(),
vol=0.0*units.meter**3,
T0=0.0*units.kelvin,
alpha_temp=0*units.delta_k/units.kelvin,
timer=Timer(),
heatgen=False,
power_tot=0*units.watt,
sph=False,
ri=0*units.meter,
ro=0*units.meter):
"""Initalizes a thermal hydraulic component.
A thermal-hydraulic component will be treated as one "lump" in the
lumped capacitance model.
:param name: The name of the component (i.e., "fuel" or "cool")
:type name: str.
:param mat: The material of this component
:type mat: Material object
:param vol: The volume of the component
:type vol: float meter**3
:param T0: The initial temperature of the component
:type T0: float.
:param alpha_temp: temperature coefficient of reactivity
:type alpha_temp: float
:param timer: The timer instance for the sim
:type timer: Timer object
:param heatgen: is this component a heat generator (fuel)
:type heatgen: bool
:param power_tot: power generated in this component
:type power_tot: float
:param sph: is this component a spherical component, spherical
equations for heatgen, conduction are different,
post-processing is different too
:type sph: bool
:param ri: inner radius of the sph/annular component, ri=0 for sphere
:type ri: float
:param ro: outer radius of the sph/annular component,
ro=radius for sphere
:type ro: float
"""
self.name = name
self.vol = vol.to('meter**3')
self.mat = mat
self.k = mat.k
self.cp = mat.cp
self.dm = mat.dm
self.timer = timer
self.T = units.Quantity(np.zeros(shape=(timer.timesteps(),),
dtype=float), 'kelvin')
self.T[0] = T0
self.T0 = T0
self.alpha_temp = alpha_temp.to('delta_k/kelvin')
self.heatgen = heatgen
self.power_tot = power_tot
self.cond = {}
self.conv = {}
self.adv = {}
self.mass = {}
self.cust = {}
self.prev_t_idx = 0
self.convBC = {}
self.sph = sph
self.ri = ri.to('meter')
self.ro = ro.to('meter')
