def dens_floc(ConcAl, ConcClay, DIM_FRACTAL, DiamTarget, coag, material, Temp):
"""Calculate floc density as a function of size."""
WaterDensity = pc.density_water(Temp)
return ((dens_floc_init(ConcAl, ConcClay, coag, material)
- WaterDensity
)
* (material.Diameter / DiamTarget)**(3 - DIM_FRACTAL)
+ WaterDensity
).to(u.kg/u.m**3)
def vel_term_floc(ConcAl, ConcClay, coag, material, DIM_FRACTAL, DiamTarget,
Temp):
"""Calculate floc terminal velocity."""
WaterDensity = pc.density_water(Temp).magnitude
return (((pc.gravity.magnitude * material.Diameter**2) /
(18 * PHI_FLOC * pc.viscosity_kinematic(Temp).magnitude)) *
((dens_floc_init(ConcAl, ConcClay, coag, material).magnitude -
WaterDensity) / WaterDensity) *
(DiamTarget / material.Diameter)**(DIM_FRACTAL - 1))
def dens_pacl_solution(ConcAluminum, temp):
"""Return the density of the PACl solution.
From Stock Tank Mixing report Fall 2013:
https://confluence.cornell.edu/download/attachments/137953883/20131213_Research_Report.pdf
"""
return ((0.492 * ConcAluminum * PACl.MolecWeight /
(PACl.AluminumMPM * MOLEC_WEIGHT_ALUMINUM)) +
pc.density_water(temp).magnitude)
def diam_floc_vel_term(ConcAl, ConcClay, coag, material, DIM_FRACTAL, VelTerm,
Temp):
"""Calculate floc diamter as a function of terminal velocity."""
WaterDensity = pc.density_water(Temp).magnitude
return (material.Diameter * (
((18 * VelTerm * PHI_FLOC * pc.viscosity_kinematic(Temp).magnitude) /
(pc.gravity.magnitude * material.Diameter**2)) *
(WaterDensity /
(dens_floc_init(ConcAl, ConcClay, coag, material).magnitude -
WaterDensity)))**(1 / (DIM_FRACTAL - 1)))
def check_diffuser(
w_sed,
w_diffuser,
vel_up,
max_hl,
temp,
report_writer,
shear_floc_max=0.5 * u.Pa,
pi_plane_jet=0.0124,
):
"""Check that the diffuser's are designed appropriately by first checking
the velocity calculated from their geometry is less than the maximum allowed
due to shear. Then check that the head loss is less than the maximum allowable.
For more info on shear stress calculation and default values see
https://aguaclara.github.io/Textbook/Sedimentation/Sed_Design.html#jet-reverser-shear-stress
Args:
w_sed: width of the sed tank (u.m)
w_diffuser: width of a diffuser (u.m)
vel_up: design upflow velocity through the sed tank (u.m / u.s)
max_hl: maximum allowable head loss over a diffuser (u.m)
q_input: design flow rate (u.L / u.s)
report_writer: ReportWriter object to record validation results
shear_floc_max: maximum shear allowed without disrupting flocculation.
Defaults to 0.5 Pascals
pi_plane_jet: the amount of energy lost in the time that it takes for
the jet to travel it's width normalized by the total kinetic energy.
Defaults to 0.0124
Returns:
none
"""
rho = pc.density_water(temp)
nu = pc.viscosity_kinematic_water(temp)
vel_diffuser = vel_up * w_sed / w_diffuser
try:
vel_max_shear = (
(shear_floc_max / rho) ** (1 / 2)
* (vel_up * w_sed / (nu * pi_plane_jet)) ** (1 / 4)
).to(u.mm / u.s)
assert vel_diffuser < vel_max_shear
report_writer.write_message(
"The max diffuser velocity based on floc shear, {!s}, "
"is greater than the one calculated by this validation "
"code, {!s}.\n".format(vel_max_shear, vel_diffuser)
)
except AssertionError:
report_writer.write_message(
"INVALID: The max diffuser velocity based on floc shear, {!s}, "
"is less than the one calculated by this validation "
"code, {!s}.\n".format(vel_max_shear, vel_diffuser)
)
report_writer.set_result("Invalid: Check Validation Report")
try:
head_loss = (vel_diffuser ** 2 / (2 * u.g_0)).to(u.cm)
assert head_loss < max_hl
report_writer.write_message(
"The max head loss, {!s}, is greater than "
"the one calculated by this validation "
"code, {!s}.\n".format(max_hl, head_loss)
)
except AssertionError:
report_writer.write_message(
"INVALID: The max head loss, {!s}, "
"is less than the one calculated by this validation "
"code, {!s}.\n".format(max_hl, head_loss)
)
report_writer.set_result("Invalid: Check Validation Report")
return vel_diffuser