'''This code is for Direct Expansion in Heating Mode'''
from __future__ import division, absolute_import, print_function
from ACHP.Cycle import DXCycleClass
from ACHP.convert_units import F2K
#Instantiate the class
Cycle = DXCycleClass()
#--------------------------------------
# Cycle parameters
#--------------------------------------
Cycle.Verbosity = 0 #the idea here is to have different levels of debug output
Cycle.ImposedVariable = 'Subcooling' #or it could be 'Charge'
Cycle.DT_sc_target = 7.0
#Cycle.Charge_target = 3.3 #uncomment for use with imposed charge
Cycle.Mode = 'HP'
Cycle.Ref = 'R410A'
Cycle.Backend = 'TTSE&HEOS' #Backend for refrigerant properties calculation: 'HEOS','TTSE&HEOS','BICUBIC&HEOS','REFPROP','SRK','PR'
Cycle.Oil = 'POE32'
Cycle.shell_pressure = 'low-pressure'
Cycle.EvapSolver = 'Moving-Boundary' #choose the type of Evaporator solver scheme ('Moving-Boundary' or 'Finite-Element')
Cycle.EvapType = 'Fin-tube' #if EvapSolver = 'Moving-Boundary', choose the type of evaporator ('Fin-tube' or 'Micro-channel')
Cycle.CondSolver = 'Moving-Boundary' #choose the type of Condenser solver scheme ('Moving-Boundary' or 'Finite-Element')
Cycle.CondType = 'Fin-tube' #if CondSolver = 'Moving-Boundary', choose the type of condenser ('Fin-tube' or 'Micro-channel')
Cycle.Update()
#--------------------------------------
# Charge correction parameters (activate by setting Cycle.ImposedVariable to 'Charge' and Cycle.ChargeMethod to either 'One-point' or 'Two-point')
#--------------------------------------
Cycle.C = 0 #[kg]
Cycle.K = 0 #[kg]
def SampleDXHPSystem():
#########################################################################
###################### CYCLE INITIALIZATION ######################
#########################################################################
## Here we load parameters that are not a function of operating conditions
## They are primarily geometric parameters
Cycle = DXCycleClass()
#--------------------------------------
#--------------------------------------
# Cycle parameters
#--------------------------------------
#--------------------------------------
Cycle.Verbosity = 5 #the idea here is to have different levels of debug output
Cycle.ImposedVariable = 'Subcooling'
Cycle.DT_sc_target = 7.0
Cycle.Charge_target = 3.3
Cycle.Mode = 'HP'
Cycle.Ref = 'R410A'
Cycle.EvapSolver = 'Moving-Boundary' #choose the type of Evaporator solver scheme (for now only 'Moving-Boundary')
Cycle.EvapType = 'Fin-tube' #if EvapSolver = 'Moving-Boundary', choose the type of evaporator (for now only 'Fin-tube')
Cycle.CondSolver = 'Moving-Boundary' #choose the type of Condenser solver scheme (for now only 'Moving-Boundary')
Cycle.CondType = 'Fin-tube' #if CondSolver = 'Moving-Boundary', choose the type of condenser ('Fin-tube' or 'Micro-channel')
Cycle.Update()
#--------------------------------------
#--------------------------------------
# Compressor parameters
#--------------------------------------
#--------------------------------------
#A few 3 ton cooling capacity compressor maps
if Cycle.Ref == 'R410A':
M = [
217.3163128, 5.094492028, -0.593170311, 4.38E-02, -2.14E-02,
1.04E-02, 7.90E-05, -5.73E-05, 1.79E-04, -8.08E-05
] #compressor map coefficients
P = [
-561.3615705, -15.62601841, 46.92506685, -0.217949552, 0.435062616,
-0.442400826, 2.25E-04, 2.37E-03, -3.32E-03, 2.50E-03
]
params = {
'M': M,
'P': P,
'Ref': Cycle.Ref, #refrigerant
'fp':
0.0, #Fraction of electrical power lost as heat to ambient #shell heat loss
'Vdot_ratio':
1.0, #Displacement Scale factor #up- or downsize compressor (1=original)
'Verbosity':
0, # How verbose should the debugging statements be [0 to 10]
'DT_sh':
5. #Superheat at inlet to compressor [K]
}
Cycle.Compressor.Update(**params)
#--------------------------------------
#--------------------------------------
# Condenser parameters
# -> see GUI for illustration/units
#--------------------------------------
#--------------------------------------
Cycle.Condenser.Fins.Tubes.NTubes_per_bank = 32
Cycle.Condenser.Fins.Tubes.Nbank = 3
Cycle.Condenser.Fins.Tubes.Ncircuits = 6
Cycle.Condenser.Fins.Tubes.Ltube = 0.452
Cycle.Condenser.Fins.Tubes.OD = 0.009525
Cycle.Condenser.Fins.Tubes.ID = 0.0089154
Cycle.Condenser.Fins.Tubes.Pl = 0.0254
Cycle.Condenser.Fins.Tubes.Pt = 0.0219964
Cycle.Condenser.Fins.Tubes.kw = 237 #wall thermal conductivity (i.e pipe material)
Cycle.Condenser.Fins.Fins.FPI = 14.5
Cycle.Condenser.Fins.Fins.Pd = 0.001
Cycle.Condenser.Fins.Fins.xf = 0.001
Cycle.Condenser.Fins.Fins.t = 0.00011
Cycle.Condenser.Fins.Fins.k_fin = 237
Cycle.Condenser.Fins.Air.Vdot_ha = 0.5663
Cycle.Condenser.Fins.Air.Tmean = F2K(70)
Cycle.Condenser.Fins.Air.Tdb = F2K(70)
Cycle.Condenser.Fins.Air.p = 101325
Cycle.Condenser.Fins.Air.RH = 0.51
Cycle.Condenser.Fins.Air.RHmean = 0.51
Cycle.Condenser.Fins.Air.FanPower = 438
params = {
'Verbosity': 0,
'FinsType':
'WavyLouveredFins' #Choose fin Type: 'WavyLouveredFins' or 'HerringboneFins'or 'PlainFins'
}
Cycle.Condenser.Update(**params)
#--------------------------------------
#--------------------------------------
# Evaporator
# -> see Condenser and GUI for explanations
#--------------------------------------
#--------------------------------------
Cycle.Evaporator.Fins.Tubes.NTubes_per_bank = 41 #number of tubes per bank=row
Cycle.Evaporator.Fins.Tubes.Nbank = 1 #number of banks/rows
Cycle.Evaporator.Fins.Tubes.Ncircuits = 5
Cycle.Evaporator.Fins.Tubes.Ltube = 2.286
Cycle.Evaporator.Fins.Tubes.OD = 0.007
Cycle.Evaporator.Fins.Tubes.ID = 0.0063904
Cycle.Evaporator.Fins.Tubes.Pl = 0.0191 #distance between center of tubes in flow direction
Cycle.Evaporator.Fins.Tubes.Pt = 0.0222 #distance between center of tubes orthogonal to flow direction
Cycle.Evaporator.Fins.Fins.FPI = 25 #Number of fins per inch
Cycle.Evaporator.Fins.Fins.Pd = 0.001 #2* amplitude of wavy fin
Cycle.Evaporator.Fins.Fins.xf = 0.001 #1/2 period of fin
Cycle.Evaporator.Fins.Fins.t = 0.00011 #Thickness of fin material
Cycle.Evaporator.Fins.Fins.k_fin = 237 #Thermal conductivity of fin material
Cycle.Evaporator.Fins.Air.Vdot_ha = 1.7934 #rated volumetric flowrate
Cycle.Evaporator.Fins.Air.Tmean = F2K(47)
Cycle.Evaporator.Fins.Air.Tdb = F2K(47) #Dry Bulb Temperature
Cycle.Evaporator.Fins.Air.p = 101325 #Air pressure in Pa
Cycle.Evaporator.Fins.Air.RH = 0.51 #Relative Humidity
Cycle.Evaporator.Fins.Air.FanPower = 160
Cycle.Evaporator.Fins.Air.RHmean = 0.51
params = {
'Ref': Cycle.Ref,
'Verbosity': 0,
'DT_sh': 5,
'FinsType':
'WavyLouveredFins' #Choose fin Type: 'WavyLouveredFins' or 'HerringboneFins'or 'PlainFins'
}
Cycle.Evaporator.Update(**params)
params = {
'L': 7.6,
'k_tube': 0.19,
't_insul': 0.02,
'k_insul': 0.036,
'T_air': 297,
'Ref': Cycle.Ref,
'h_air': 6,
'LineSetOption': 'Off'
}
Cycle.LineSetSupply.Update(**params)
Cycle.LineSetReturn.Update(**params)
Cycle.LineSetSupply.OD = 0.01905
Cycle.LineSetSupply.ID = 0.017526
Cycle.LineSetReturn.OD = 0.009525
Cycle.LineSetReturn.ID = 0.007986
#Now solve
Cycle.PreconditionedSolve()
from ACHP.Cycle import DXCycleClass
#Instantiate the cycle class
Cycle=DXCycleClass()
#--------------------------------------
# Cycle parameters
#--------------------------------------
Cycle.Verbosity = 0 #the idea here is to have different levels of debug output
Cycle.ImposedVariable = 'Subcooling'
Cycle.DT_sc_target = 7.0
Cycle.Mode='AC'
Cycle.Ref='R410A'
#--------------------------------------
# Compressor parameters
#--------------------------------------
#A 3 ton cooling capacity compressor map
M=[217.3163128,5.094492028,-0.593170311,4.38E-02,-2.14E-02,
1.04E-02,7.90E-05,-5.73E-05,1.79E-04,-8.08E-05]
P=[-561.3615705,-15.62601841,46.92506685,-0.217949552,
0.435062616,-0.442400826,2.25E-04,2.37E-03,-3.32E-03,2.50E-03]
params={
'M':M,
'P':P,
'Ref':Cycle.Ref, #Refrigerant
'fp':0.0, #Fraction of electrical power lost as heat to ambient
'Vdot_ratio': 1.0, #Displacement Scale factor
'Verbosity': 0, # How verbose should the debugging be [0-10]
}
def SampleDXACSystem(Calculate=True):
"""
A sample DX Air Conditioning system. This is based on the work of Bo Shen.
"""
#########################################################################
###################### CYCLE INITIALIZATION ######################
#########################################################################
## Here we load parameters that are not a function of operating conditions
## They are primarily geometric parameters
Cycle = DXCycleClass()
#--------------------------------------
#--------------------------------------
# Cycle parameters
#--------------------------------------
#--------------------------------------
Cycle.Verbosity = 10 #the idea here is to have different levels of debug output
Cycle.ImposedVariable = 'Subcooling'
Cycle.DT_sc_target = 7.0
Cycle.Charge_target = 2.8
Cycle.Mode = 'AC'
Cycle.Ref = 'R410A'
Cycle.Backend = 'HEOS' #Backend for refrigerant properties calculation: 'HEOS','TTSE&HEOS','BICUBIC&HEOS','REFPROP','SRK','PR'
Cycle.Oil = 'POE32'
Cycle.shell_pressure = 'low-pressure'
Cycle.TestName = 'DXAC-0014' #this and the two next lines can be used to specify exact test conditions
Cycle.TestDescription = 'shows application of DXAC system'
Cycle.TestDetails = 'This is the sample cycle for the DXAC system which can be modified for other systems'
Cycle.EvapSolver = 'Moving-Boundary' #choose the type of Evaporator solver scheme (for now only 'Moving-Boundary'')
Cycle.EvapType = 'Fin-tube' #if EvapSolver = 'Moving-Boundary', choose the type of evaporator (for now only 'Fin-tube')
Cycle.CondSolver = 'Moving-Boundary' #choose the type of Condenser solver scheme (for now only 'Moving-Boundary')
Cycle.CondType = 'Fin-tube' #if CondSolver = 'Moving-Boundary', choose the type of condenser ('Fin-tube' or 'Micro-channel')
Cycle.Update()
#--------------------------------------
#--------------------------------------
# Compressor parameters
#--------------------------------------
#--------------------------------------
#A few 3 ton cooling capacity compressor maps
if Cycle.Ref == 'R410A':
M = [
217.3163128, 5.094492028, -0.593170311, 4.38E-02, -2.14E-02,
1.04E-02, 7.90E-05, -5.73E-05, 1.79E-04, -8.08E-05
] #compressor map coefficients
P = [
-561.3615705, -15.62601841, 46.92506685, -0.217949552, 0.435062616,
-0.442400826, 2.25E-04, 2.37E-03, -3.32E-03, 2.50E-03
]
params = {
'M': M,
'P': P,
'Ref': Cycle.Ref, #refrigerant
'Oil': Cycle.Oil, #Compressor lubricant oil
'V_oil_sump': 0, #Volume of oil in the sump
'shell_pressure': Cycle.shell_pressure, #Compressor shell pressure
'fp':
0.0, #Fraction of electrical power lost as heat to ambient #shell heat loss
'Vdot_ratio':
1.0, #Displacement Scale factor #up- or downsize compressor (1=original)
'Verbosity':
0, # How verbose should the debugging statements be [0 to 10]
}
Cycle.Compressor.Update(**params)
#--------------------------------------
#--------------------------------------
# Condenser parameters
# -> see GUI for illustration/units
#--------------------------------------
#--------------------------------------
Cycle.Condenser.Fins.Tubes.NTubes_per_bank = 24 #number of tubes per bank=row
Cycle.Condenser.Fins.Tubes.Nbank = 1 #number of banks/rows
Cycle.Condenser.Fins.Tubes.Ncircuits = 3
Cycle.Condenser.Fins.Tubes.Ltube = 2.252
Cycle.Condenser.Fins.Tubes.OD = 0.00913
Cycle.Condenser.Fins.Tubes.ID = 0.00849
Cycle.Condenser.Fins.Tubes.Pl = 0.0191 #distance between center of tubes in flow direction
Cycle.Condenser.Fins.Tubes.Pt = 0.0254 #distance between center of tubes orthogonal to flow direction
Cycle.Condenser.Fins.Tubes.kw = 237 #wall thermal conductivity (i.e pipe material)
Cycle.Condenser.Fins.Fins.FPI = 25 #Number of fins per inch
Cycle.Condenser.Fins.Fins.Pd = 0.001 #2* amplitude of wavy fin
Cycle.Condenser.Fins.Fins.xf = 0.001 #1/2 period of fin
Cycle.Condenser.Fins.Fins.t = 0.00011 #Thickness of fin material
Cycle.Condenser.Fins.Fins.k_fin = 237 #Thermal conductivity of fin material
Cycle.Condenser.Fins.Air.Vdot_ha = 1.7934 #rated volumetric flowrate
Cycle.Condenser.Fins.Air.Tmean = 308.15
Cycle.Condenser.Fins.Air.Tdb = Cycle.Condenser.Fins.Air.Tmean #Dry Bulb Temperature
Cycle.Condenser.Fins.Air.p = 101325 #Air pressure in Pa
Cycle.Condenser.Fins.Air.RH = 0.51 #Relative Humidity
Cycle.Condenser.Fins.Air.RHmean = 0.51
Cycle.Condenser.Fins.Air.FanPower = 260
params = {
'Verbosity': 0,
'FinsType':
'WavyLouveredFins' #Choose fin Type: 'WavyLouveredFins' or 'HerringboneFins'or 'PlainFins'
}
Cycle.Condenser.Update(**params)
# ----------------------------------
# Expanison device Parameters
# ----------------------------------
params = {
'ExpType': 'Ideal', #expansion device type
}
Cycle.ExpDev.Update(**params)
#--------------------------------------
#--------------------------------------
# Evaporator
# -> see Condenser and GUI for explanations
#--------------------------------------
#--------------------------------------
if hasattr(Cycle,
'TestName'): #update parameters for output list, if applicable
Cycle.Evaporator.TestName = Cycle.TestName
if hasattr(Cycle, 'TestDescription'):
Cycle.Evaporator.TestDescription = Cycle.TestDescription
if hasattr(Cycle, 'TestDetails'):
Cycle.Evaporator.TestDetails = Cycle.TestDetails
Cycle.Evaporator.Fins.Tubes.NTubes_per_bank = 32 #dimensional parameters
Cycle.Evaporator.Fins.Tubes.Nbank = 3
Cycle.Evaporator.Fins.Tubes.Ltube = 0.452
Cycle.Evaporator.Fins.Tubes.OD = 0.00913
Cycle.Evaporator.Fins.Tubes.ID = 0.00849
Cycle.Evaporator.Fins.Tubes.Pl = 0.0191
Cycle.Evaporator.Fins.Tubes.Pt = 0.0254
Cycle.Evaporator.Fins.Tubes.Ncircuits = 5
Cycle.Evaporator.Fins.Tubes.kw = 237 #wall thermal conductivity (i.e pipe material)
Cycle.Evaporator.Fins.Fins.FPI = 14.5
Cycle.Evaporator.Fins.Fins.Pd = 0.001
Cycle.Evaporator.Fins.Fins.xf = 0.001
Cycle.Evaporator.Fins.Fins.t = 0.00011
Cycle.Evaporator.Fins.Fins.k_fin = 237
Cycle.Evaporator.Fins.Air.Vdot_ha = 0.56319
Cycle.Evaporator.Fins.Air.Tmean = 297.039
Cycle.Evaporator.Fins.Air.Tdb = 297.039
Cycle.Evaporator.Fins.Air.p = 101325
Cycle.Evaporator.Fins.Air.RH = 0.5
Cycle.Evaporator.Fins.Air.RHmean = 0.5
Cycle.Evaporator.Fins.Air.FanPower = 438
params = {
'Ref': Cycle.Ref,
'Verbosity': 0,
'DT_sh': 5,
'FinsType':
'WavyLouveredFins' #Choose fin Type: 'WavyLouveredFins' or 'HerringboneFins'or 'PlainFins'
}
Cycle.Evaporator.Update(**params)
params = {
'L': 7.6,
'k_tube': 0.19,
't_insul': 0.02,
'k_insul': 0.036,
'T_air': 297,
'Ref': Cycle.Ref,
'h_air': 0.0000000001
}
Cycle.LineSetLiquid.Update(**params)
Cycle.LineSetSuction.Update(**params)
Cycle.LineSetLiquid.OD = 0.009525
Cycle.LineSetLiquid.ID = 0.007986
Cycle.LineSetSuction.OD = 0.01905
Cycle.LineSetSuction.ID = 0.017526
# ----------------------------------
# ----------------------------------
# Line Set Discharge Parameters
# ----------------------------------
# ----------------------------------
params = {
'L': 0.3, #tube length in m
'k_tube': 0.19,
't_insul': 0, #no insulation
'k_insul': 0.036,
'T_air': 297,
'Ref': Cycle.Ref,
'h_air': 0.0000000001,
'LineSetOption': 'Off'
}
Cycle.LineSetDischarge.Update(**params)
Cycle.LineSetDischarge.OD = 0.009525
Cycle.LineSetDischarge.ID = 0.007986
#Now solve if Calculate has not been set to False
if Calculate == True:
Cycle.PreconditionedSolve()
return Cycle
from __future__ import print_function
from ACHP.Cycle import DXCycleClass
#Instantiate the cycle class
Cycle = DXCycleClass()
#--------------------------------------
# Cycle parameters
#--------------------------------------
Cycle.Verbosity = 0 #the idea here is to have different levels of debug output
Cycle.ImposedVariable = 'Subcooling'
Cycle.DT_sc_target = 7.0
Cycle.Mode = 'AC'
Cycle.Ref = 'R410A'
Cycle.Backend = 'TTSE&HEOS' #Backend for refrigerant properties calculation: 'HEOS','TTSE&HEOS','BICUBIC&HEOS','REFPROP','SRK','PR'
#--------------------------------------
# Compressor parameters
#--------------------------------------
#A 3 ton cooling capacity compressor map
M = [
217.3163128, 5.094492028, -0.593170311, 4.38E-02, -2.14E-02, 1.04E-02,
7.90E-05, -5.73E-05, 1.79E-04, -8.08E-05
]
P = [
-561.3615705, -15.62601841, 46.92506685, -0.217949552, 0.435062616,
-0.442400826, 2.25E-04, 2.37E-03, -3.32E-03, 2.50E-03
]
params = {
from ACHP.Cycle import DXCycleClass, F2K
#Instantiate the class
Cycle = DXCycleClass()
#--------------------------------------
# Cycle parameters
#--------------------------------------
Cycle.Verbosity = 0 #the idea here is to have different levels of debug output
Cycle.ImposedVariable = 'Subcooling' #or it could be 'Charge'
Cycle.DT_sc_target = 7.0
#Cycle.Charge_target = 3.3 #uncomment for use with imposed charge
Cycle.Mode = 'HP'
Cycle.Ref = 'R410A'
#--------------------------------------
# Compressor parameters
#--------------------------------------
#A few 3 ton cooling capacity compressor maps
M = [
217.3163128, 5.094492028, -0.593170311, 4.38E-02, -2.14E-02, 1.04E-02,
7.90E-05, -5.73E-05, 1.79E-04, -8.08E-05
]
P = [
-561.3615705, -15.62601841, 46.92506685, -0.217949552, 0.435062616,
-0.442400826, 2.25E-04, 2.37E-03, -3.32E-03, 2.50E-03
]
params = {
'M': M,
'P': P,
def GUI2DXCycleInputs(GUI):
#Create the basic structure of the DXCycle
Cycle = DXCycleClass()
M = [0, 0, 0, 0, 0, 0, 0, 0, 0, 0] #Empty list
M[0] = float(GUI.txtCompM1.GetValue())
M[1] = float(GUI.txtCompM2.GetValue())
M[2] = float(GUI.txtCompM3.GetValue())
M[3] = float(GUI.txtCompM4.GetValue())
M[4] = float(GUI.txtCompM5.GetValue())
M[5] = float(GUI.txtCompM6.GetValue())
M[6] = float(GUI.txtCompM7.GetValue())
M[7] = float(GUI.txtCompM8.GetValue())
M[8] = float(GUI.txtCompM9.GetValue())
M[9] = float(GUI.txtCompM10.GetValue())
P = [0, 0, 0, 0, 0, 0, 0, 0, 0, 0] #Empty list
P[0] = float(GUI.txtCompP1.GetValue())
P[1] = float(GUI.txtCompP2.GetValue())
P[2] = float(GUI.txtCompP3.GetValue())
P[3] = float(GUI.txtCompP4.GetValue())
P[4] = float(GUI.txtCompP5.GetValue())
P[5] = float(GUI.txtCompP6.GetValue())
P[6] = float(GUI.txtCompP7.GetValue())
P[7] = float(GUI.txtCompP8.GetValue())
P[8] = float(GUI.txtCompP9.GetValue())
P[9] = float(GUI.txtCompP10.GetValue())
Cycle.Compressor.M = M
Cycle.Compressor.P = P
Cycle.Compressor.fp = float(GUI.txtCompfp.GetValue())
Cycle.Compressor.Vdot_ratio = float(GUI.txtCompVdot_ratio.GetValue())
Cycle.Evaporator.DT_sh = float(GUI.txtCycleDTsh.GetValue())
if GUI.radCycleMode.GetStringSelection() == 'Cooling Mode':
Cycle.Condenser.Fins.Air.Vdot_ha = float(
GUI.txtCondenserAirVdot.GetValue())
Cycle.Condenser.Fins.Air.Tdb = float(GUI.txtCondenserAirTdb.GetValue())
Cycle.Condenser.Fins.Air.p = float(GUI.txtCondenserAirp.GetValue())
Cycle.Condenser.Fins.Air.RH = float(GUI.txtCondenserAirRH.GetValue())
Cycle.Condenser.Fins.Air.Tmean = float(
GUI.txtCondenserAirTdb.GetValue())
Cycle.Condenser.Fins.Air.RHmean = float(
GUI.txtCondenserAirRH.GetValue())
Cycle.Condenser.Fins.Tubes.NTubes_per_bank = int(
GUI.txtCondenserTubesNtubes.GetValue())
Cycle.Condenser.Fins.Tubes.Nbank = int(
GUI.txtCondenserTubesNbank.GetValue())
Cycle.Condenser.Fins.Tubes.Ltube = float(
GUI.txtCondenserTubesL.GetValue())
Cycle.Condenser.Fins.Tubes.OD = float(
GUI.txtCondenserTubesOD.GetValue())
Cycle.Condenser.Fins.Tubes.ID = float(
GUI.txtCondenserTubesID.GetValue())
Cycle.Condenser.Fins.Tubes.Pl = float(
GUI.txtCondenserTubesPl.GetValue())
Cycle.Condenser.Fins.Tubes.Pt = float(
GUI.txtCondenserTubesPt.GetValue())
Cycle.Condenser.Fins.Tubes.Ncircuits = int(
GUI.txtCondenserTubesNcircuit.GetValue())
Cycle.Condenser.Fins.Fins.FPI = float(
GUI.txtCondenserFinFPI.GetValue())
Cycle.Condenser.Fins.Fins.Pd = float(GUI.txtCondenserFinpd.GetValue())
Cycle.Condenser.Fins.Fins.xf = float(GUI.txtCondenserFinxf.GetValue())
Cycle.Condenser.Fins.Fins.t = float(GUI.txtCondenserFint.GetValue())
Cycle.Condenser.Fins.Fins.k_fin = float(
GUI.txtCondenserFink.GetValue())
Cycle.Condenser.Fins.Air.FanPower = float(
GUI.txtCondenserPower.GetValue())
Cycle.Condenser.Verbosity = 0
Cycle.Evaporator.Fins.Air.Vdot_ha = float(
GUI.txtCoolingCoilAirVdot.GetValue())
Cycle.Evaporator.Fins.Air.Tdb = float(
GUI.txtCoolingCoilAirTdb.GetValue())
Cycle.Evaporator.Fins.Air.p = float(GUI.txtCoolingCoilAirp.GetValue())
Cycle.Evaporator.Fins.Air.RH = float(
GUI.txtCoolingCoilAirRH.GetValue())
Cycle.Evaporator.Fins.Air.Tmean = float(
GUI.txtCoolingCoilAirTdb.GetValue())
Cycle.Evaporator.Fins.Air.RHmean = float(
GUI.txtCoolingCoilAirRH.GetValue())
Cycle.Evaporator.Fins.Tubes.NTubes_per_bank = float(
GUI.txtCoolingCoilTubesNtubes.GetValue())
Cycle.Evaporator.Fins.Tubes.Nbank = float(
GUI.txtCoolingCoilTubesNbank.GetValue())
Cycle.Evaporator.Fins.Tubes.Ltube = float(
GUI.txtCoolingCoilTubesL.GetValue())
Cycle.Evaporator.Fins.Tubes.OD = float(
GUI.txtCoolingCoilTubesOD.GetValue())
Cycle.Evaporator.Fins.Tubes.ID = float(
GUI.txtCoolingCoilTubesID.GetValue())
Cycle.Evaporator.Fins.Tubes.Pl = float(
GUI.txtCoolingCoilTubesPl.GetValue())
Cycle.Evaporator.Fins.Tubes.Pt = float(
GUI.txtCoolingCoilTubesPt.GetValue())
Cycle.Evaporator.Fins.Tubes.Ncircuits = float(
GUI.txtCoolingCoilTubesNcircuit.GetValue())
Cycle.Evaporator.Fins.Fins.FPI = float(
GUI.txtCoolingCoilFinFPI.GetValue())
Cycle.Evaporator.Fins.Fins.Pd = float(
GUI.txtCoolingCoilFinpd.GetValue())
Cycle.Evaporator.Fins.Fins.xf = float(
GUI.txtCoolingCoilFinxf.GetValue())
Cycle.Evaporator.Fins.Fins.t = float(GUI.txtCoolingCoilFint.GetValue())
Cycle.Evaporator.Fins.Fins.k_fin = float(
GUI.txtCoolingCoilFink.GetValue())
Cycle.Evaporator.Fins.Air.FanPower = float(
GUI.txtCoolingCoilPower.GetValue())
Cycle.Evaporator.DT_sh = float(GUI.txtCycleDTsh.GetValue())
Cycle.Evaporator.Verbosity = 0
elif GUI.radCycleMode.GetStringSelection() == 'Heating Mode':
Cycle.Evaporator.Fins.Air.Vdot_ha = float(
GUI.txtCondenserAirVdot.GetValue())
Cycle.Evaporator.Fins.Air.Tdb = float(
GUI.txtCondenserAirTdb.GetValue())
Cycle.Evaporator.Fins.Air.p = float(GUI.txtCondenserAirp.GetValue())
Cycle.Evaporator.Fins.Air.RH = float(GUI.txtCondenserAirRH.GetValue())
Cycle.Evaporator.Fins.Air.Tmean = float(
GUI.txtCondenserAirTdb.GetValue())
Cycle.Evaporator.Fins.Air.RHmean = float(
GUI.txtCondenserAirRH.GetValue())
Cycle.Evaporator.Fins.Tubes.NTubes_per_bank = int(
GUI.txtCondenserTubesNtubes.GetValue())
Cycle.Evaporator.Fins.Tubes.Nbank = int(
GUI.txtCondenserTubesNbank.GetValue())
Cycle.Evaporator.Fins.Tubes.Ltube = float(
GUI.txtCondenserTubesL.GetValue())
Cycle.Evaporator.Fins.Tubes.OD = float(
GUI.txtCondenserTubesOD.GetValue())
Cycle.Evaporator.Fins.Tubes.ID = float(
GUI.txtCondenserTubesID.GetValue())
Cycle.Evaporator.Fins.Tubes.Pl = float(
GUI.txtCondenserTubesPl.GetValue())
Cycle.Evaporator.Fins.Tubes.Pt = float(
GUI.txtCondenserTubesPt.GetValue())
Cycle.Evaporator.Fins.Tubes.Ncircuits = int(
GUI.txtCondenserTubesNcircuit.GetValue())
Cycle.Evaporator.Fins.Fins.FPI = float(
GUI.txtCondenserFinFPI.GetValue())
Cycle.Evaporator.Fins.Fins.Pd = float(GUI.txtCondenserFinpd.GetValue())
Cycle.Evaporator.Fins.Fins.xf = float(GUI.txtCondenserFinxf.GetValue())
Cycle.Evaporator.Fins.Fins.t = float(GUI.txtCondenserFint.GetValue())
Cycle.Evaporator.Fins.Fins.k_fin = float(
GUI.txtCondenserFink.GetValue())
Cycle.Evaporator.Fins.Air.FanPower = float(
GUI.txtCondenserPower.GetValue())
Cycle.Evaporator.Verbosity = 0
Cycle.Condenser.Fins.Air.Vdot_ha = float(
GUI.txtCoolingCoilAirVdot.GetValue())
Cycle.Condenser.Fins.Air.Tdb = float(
GUI.txtCoolingCoilAirTdb.GetValue())
Cycle.Condenser.Fins.Air.p = float(GUI.txtCoolingCoilAirp.GetValue())
Cycle.Condenser.Fins.Air.RH = float(GUI.txtCoolingCoilAirRH.GetValue())
Cycle.Condenser.Fins.Air.Tmean = float(
GUI.txtCoolingCoilAirTdb.GetValue())
Cycle.Condenser.Fins.Air.RHmean = float(
GUI.txtCoolingCoilAirRH.GetValue())
Cycle.Condenser.Fins.Tubes.NTubes_per_bank = float(
GUI.txtCoolingCoilTubesNtubes.GetValue())
Cycle.Condenser.Fins.Tubes.Nbank = float(
GUI.txtCoolingCoilTubesNbank.GetValue())
Cycle.Condenser.Fins.Tubes.Ltube = float(
GUI.txtCoolingCoilTubesL.GetValue())
Cycle.Condenser.Fins.Tubes.OD = float(
GUI.txtCoolingCoilTubesOD.GetValue())
Cycle.Condenser.Fins.Tubes.ID = float(
GUI.txtCoolingCoilTubesID.GetValue())
Cycle.Condenser.Fins.Tubes.Pl = float(
GUI.txtCoolingCoilTubesPl.GetValue())
Cycle.Condenser.Fins.Tubes.Pt = float(
GUI.txtCoolingCoilTubesPt.GetValue())
Cycle.Condenser.Fins.Tubes.Ncircuits = float(
GUI.txtCoolingCoilTubesNcircuit.GetValue())
Cycle.Condenser.Fins.Fins.FPI = float(
GUI.txtCoolingCoilFinFPI.GetValue())
Cycle.Condenser.Fins.Fins.Pd = float(
GUI.txtCoolingCoilFinpd.GetValue())
Cycle.Condenser.Fins.Fins.xf = float(
GUI.txtCoolingCoilFinxf.GetValue())
Cycle.Condenser.Fins.Fins.t = float(GUI.txtCoolingCoilFint.GetValue())
Cycle.Condenser.Fins.Fins.k_fin = float(
GUI.txtCoolingCoilFink.GetValue())
Cycle.Condenser.Fins.Air.FanPower = float(
GUI.txtCoolingCoilPower.GetValue())
Cycle.Condenser.Verbosity = 0
Cycle.LineSetSupply.L = float(GUI.txtLineSetL.GetValue())
Cycle.LineSetSupply.OD = float(GUI.txtLineSetOD_supply.GetValue())
Cycle.LineSetSupply.ID = float(GUI.txtLineSetID_supply.GetValue())
Cycle.LineSetSupply.t_insul = float(GUI.txtLineSetInsult.GetValue())
Cycle.LineSetSupply.k_tube = float(GUI.txtLineSetTubek.GetValue())
Cycle.LineSetSupply.k_insul = float(GUI.txtLineSetInsulk.GetValue())
Cycle.LineSetSupply.h_air = float(GUI.txtLineSeth_air.GetValue())
Cycle.LineSetSupply.T_air = float(GUI.txtLineSetT_air.GetValue())
Cycle.LineSetReturn.L = float(GUI.txtLineSetL.GetValue())
Cycle.LineSetReturn.OD = float(GUI.txtLineSetOD_return.GetValue())
Cycle.LineSetReturn.ID = float(GUI.txtLineSetID_return.GetValue())
Cycle.LineSetReturn.t_insul = float(GUI.txtLineSetInsult.GetValue())
Cycle.LineSetReturn.k_tube = float(GUI.txtLineSetTubek.GetValue())
Cycle.LineSetReturn.k_insul = float(GUI.txtLineSetInsulk.GetValue())
Cycle.LineSetReturn.h_air = float(GUI.txtLineSeth_air.GetValue())
Cycle.LineSetReturn.T_air = float(GUI.txtLineSetT_air.GetValue())
Cycle.Charge_target = float(GUI.txtCycleCharge.GetValue())
Cycle.DT_sc_target = float(GUI.txtCycleSubcooling.GetValue())
Cycle.Mode = 'AC'
Cycle.Ref = str(GUI.cmbRefrigerant.GetValue())
Cycle.Verbosity = 10
Cycle.ParaPath = GUI.txtParaPath.GetValue()
return Cycle
def GUI2DXCycleInputs(GUI):
#Create the basic structure of the DXCycle
Cycle=DXCycleClass()
M=[0,0,0,0,0,0,0,0,0,0] #Empty list
M[0]=float(GUI.txtCompM1.GetValue())
M[1]=float(GUI.txtCompM2.GetValue())
M[2]=float(GUI.txtCompM3.GetValue())
M[3]=float(GUI.txtCompM4.GetValue())
M[4]=float(GUI.txtCompM5.GetValue())
M[5]=float(GUI.txtCompM6.GetValue())
M[6]=float(GUI.txtCompM7.GetValue())
M[7]=float(GUI.txtCompM8.GetValue())
M[8]=float(GUI.txtCompM9.GetValue())
M[9]=float(GUI.txtCompM10.GetValue())
P=[0,0,0,0,0,0,0,0,0,0] #Empty list
P[0]=float(GUI.txtCompP1.GetValue())
P[1]=float(GUI.txtCompP2.GetValue())
P[2]=float(GUI.txtCompP3.GetValue())
P[3]=float(GUI.txtCompP4.GetValue())
P[4]=float(GUI.txtCompP5.GetValue())
P[5]=float(GUI.txtCompP6.GetValue())
P[6]=float(GUI.txtCompP7.GetValue())
P[7]=float(GUI.txtCompP8.GetValue())
P[8]=float(GUI.txtCompP9.GetValue())
P[9]=float(GUI.txtCompP10.GetValue())
Cycle.Compressor.M=M
Cycle.Compressor.P=P
Cycle.Compressor.fp =float(GUI.txtCompfp.GetValue())
Cycle.Compressor.Vdot_ratio =float(GUI.txtCompVdot_ratio.GetValue())
Cycle.Evaporator.DT_sh =float(GUI.txtCycleDTsh.GetValue())
if GUI.radCycleMode.GetStringSelection()=='Cooling Mode':
Cycle.Condenser.Fins.Air.Vdot_ha =float(GUI.txtCondenserAirVdot.GetValue())
Cycle.Condenser.Fins.Air.Tdb =float(GUI.txtCondenserAirTdb.GetValue())
Cycle.Condenser.Fins.Air.p =float(GUI.txtCondenserAirp.GetValue())
Cycle.Condenser.Fins.Air.RH =float(GUI.txtCondenserAirRH.GetValue())
Cycle.Condenser.Fins.Air.Tmean =float(GUI.txtCondenserAirTdb.GetValue())
Cycle.Condenser.Fins.Air.RHmean =float(GUI.txtCondenserAirRH.GetValue())
Cycle.Condenser.Fins.Tubes.NTubes_per_bank =int(GUI.txtCondenserTubesNtubes.GetValue())
Cycle.Condenser.Fins.Tubes.Nbank =int(GUI.txtCondenserTubesNbank.GetValue())
Cycle.Condenser.Fins.Tubes.Ltube =float(GUI.txtCondenserTubesL.GetValue())
Cycle.Condenser.Fins.Tubes.OD =float(GUI.txtCondenserTubesOD.GetValue())
Cycle.Condenser.Fins.Tubes.ID =float(GUI.txtCondenserTubesID.GetValue())
Cycle.Condenser.Fins.Tubes.Pl =float(GUI.txtCondenserTubesPl.GetValue())
Cycle.Condenser.Fins.Tubes.Pt =float(GUI.txtCondenserTubesPt.GetValue())
Cycle.Condenser.Fins.Tubes.Ncircuits =int(GUI.txtCondenserTubesNcircuit.GetValue())
Cycle.Condenser.Fins.Fins.FPI =float(GUI.txtCondenserFinFPI.GetValue())
Cycle.Condenser.Fins.Fins.Pd =float(GUI.txtCondenserFinpd.GetValue())
Cycle.Condenser.Fins.Fins.xf =float(GUI.txtCondenserFinxf.GetValue())
Cycle.Condenser.Fins.Fins.t =float(GUI.txtCondenserFint.GetValue())
Cycle.Condenser.Fins.Fins.k_fin =float(GUI.txtCondenserFink.GetValue())
Cycle.Condenser.Fins.Air.FanPower =float(GUI.txtCondenserPower.GetValue())
Cycle.Condenser.Verbosity =0
Cycle.Evaporator.Fins.Air.Vdot_ha =float(GUI.txtCoolingCoilAirVdot.GetValue())
Cycle.Evaporator.Fins.Air.Tdb =float(GUI.txtCoolingCoilAirTdb.GetValue())
Cycle.Evaporator.Fins.Air.p =float(GUI.txtCoolingCoilAirp.GetValue())
Cycle.Evaporator.Fins.Air.RH =float(GUI.txtCoolingCoilAirRH.GetValue())
Cycle.Evaporator.Fins.Air.Tmean =float(GUI.txtCoolingCoilAirTdb.GetValue())
Cycle.Evaporator.Fins.Air.RHmean =float(GUI.txtCoolingCoilAirRH.GetValue())
Cycle.Evaporator.Fins.Tubes.NTubes_per_bank =float(GUI.txtCoolingCoilTubesNtubes.GetValue())
Cycle.Evaporator.Fins.Tubes.Nbank =float(GUI.txtCoolingCoilTubesNbank.GetValue())
Cycle.Evaporator.Fins.Tubes.Ltube =float(GUI.txtCoolingCoilTubesL.GetValue())
Cycle.Evaporator.Fins.Tubes.OD =float(GUI.txtCoolingCoilTubesOD.GetValue())
Cycle.Evaporator.Fins.Tubes.ID =float(GUI.txtCoolingCoilTubesID.GetValue())
Cycle.Evaporator.Fins.Tubes.Pl =float(GUI.txtCoolingCoilTubesPl.GetValue())
Cycle.Evaporator.Fins.Tubes.Pt =float(GUI.txtCoolingCoilTubesPt.GetValue())
Cycle.Evaporator.Fins.Tubes.Ncircuits=float(GUI.txtCoolingCoilTubesNcircuit.GetValue())
Cycle.Evaporator.Fins.Fins.FPI =float(GUI.txtCoolingCoilFinFPI.GetValue())
Cycle.Evaporator.Fins.Fins.Pd =float(GUI.txtCoolingCoilFinpd.GetValue())
Cycle.Evaporator.Fins.Fins.xf =float(GUI.txtCoolingCoilFinxf.GetValue())
Cycle.Evaporator.Fins.Fins.t =float(GUI.txtCoolingCoilFint.GetValue())
Cycle.Evaporator.Fins.Fins.k_fin =float(GUI.txtCoolingCoilFink.GetValue())
Cycle.Evaporator.Fins.Air.FanPower =float(GUI.txtCoolingCoilPower.GetValue())
Cycle.Evaporator.DT_sh =float(GUI.txtCycleDTsh.GetValue())
Cycle.Evaporator.Verbosity =0
elif GUI.radCycleMode.GetStringSelection()=='Heating Mode':
Cycle.Evaporator.Fins.Air.Vdot_ha =float(GUI.txtCondenserAirVdot.GetValue())
Cycle.Evaporator.Fins.Air.Tdb =float(GUI.txtCondenserAirTdb.GetValue())
Cycle.Evaporator.Fins.Air.p =float(GUI.txtCondenserAirp.GetValue())
Cycle.Evaporator.Fins.Air.RH =float(GUI.txtCondenserAirRH.GetValue())
Cycle.Evaporator.Fins.Air.Tmean =float(GUI.txtCondenserAirTdb.GetValue())
Cycle.Evaporator.Fins.Air.RHmean =float(GUI.txtCondenserAirRH.GetValue())
Cycle.Evaporator.Fins.Tubes.NTubes_per_bank =int(GUI.txtCondenserTubesNtubes.GetValue())
Cycle.Evaporator.Fins.Tubes.Nbank =int(GUI.txtCondenserTubesNbank.GetValue())
Cycle.Evaporator.Fins.Tubes.Ltube =float(GUI.txtCondenserTubesL.GetValue())
Cycle.Evaporator.Fins.Tubes.OD =float(GUI.txtCondenserTubesOD.GetValue())
Cycle.Evaporator.Fins.Tubes.ID =float(GUI.txtCondenserTubesID.GetValue())
Cycle.Evaporator.Fins.Tubes.Pl =float(GUI.txtCondenserTubesPl.GetValue())
Cycle.Evaporator.Fins.Tubes.Pt =float(GUI.txtCondenserTubesPt.GetValue())
Cycle.Evaporator.Fins.Tubes.Ncircuits =int(GUI.txtCondenserTubesNcircuit.GetValue())
Cycle.Evaporator.Fins.Fins.FPI =float(GUI.txtCondenserFinFPI.GetValue())
Cycle.Evaporator.Fins.Fins.Pd =float(GUI.txtCondenserFinpd.GetValue())
Cycle.Evaporator.Fins.Fins.xf =float(GUI.txtCondenserFinxf.GetValue())
Cycle.Evaporator.Fins.Fins.t =float(GUI.txtCondenserFint.GetValue())
Cycle.Evaporator.Fins.Fins.k_fin =float(GUI.txtCondenserFink.GetValue())
Cycle.Evaporator.Fins.Air.FanPower =float(GUI.txtCondenserPower.GetValue())
Cycle.Evaporator.Verbosity =0
Cycle.Condenser.Fins.Air.Vdot_ha =float(GUI.txtCoolingCoilAirVdot.GetValue())
Cycle.Condenser.Fins.Air.Tdb =float(GUI.txtCoolingCoilAirTdb.GetValue())
Cycle.Condenser.Fins.Air.p =float(GUI.txtCoolingCoilAirp.GetValue())
Cycle.Condenser.Fins.Air.RH =float(GUI.txtCoolingCoilAirRH.GetValue())
Cycle.Condenser.Fins.Air.Tmean =float(GUI.txtCoolingCoilAirTdb.GetValue())
Cycle.Condenser.Fins.Air.RHmean =float(GUI.txtCoolingCoilAirRH.GetValue())
Cycle.Condenser.Fins.Tubes.NTubes_per_bank =float(GUI.txtCoolingCoilTubesNtubes.GetValue())
Cycle.Condenser.Fins.Tubes.Nbank =float(GUI.txtCoolingCoilTubesNbank.GetValue())
Cycle.Condenser.Fins.Tubes.Ltube =float(GUI.txtCoolingCoilTubesL.GetValue())
Cycle.Condenser.Fins.Tubes.OD =float(GUI.txtCoolingCoilTubesOD.GetValue())
Cycle.Condenser.Fins.Tubes.ID =float(GUI.txtCoolingCoilTubesID.GetValue())
Cycle.Condenser.Fins.Tubes.Pl =float(GUI.txtCoolingCoilTubesPl.GetValue())
Cycle.Condenser.Fins.Tubes.Pt =float(GUI.txtCoolingCoilTubesPt.GetValue())
Cycle.Condenser.Fins.Tubes.Ncircuits=float(GUI.txtCoolingCoilTubesNcircuit.GetValue())
Cycle.Condenser.Fins.Fins.FPI =float(GUI.txtCoolingCoilFinFPI.GetValue())
Cycle.Condenser.Fins.Fins.Pd =float(GUI.txtCoolingCoilFinpd.GetValue())
Cycle.Condenser.Fins.Fins.xf =float(GUI.txtCoolingCoilFinxf.GetValue())
Cycle.Condenser.Fins.Fins.t =float(GUI.txtCoolingCoilFint.GetValue())
Cycle.Condenser.Fins.Fins.k_fin =float(GUI.txtCoolingCoilFink.GetValue())
Cycle.Condenser.Fins.Air.FanPower =float(GUI.txtCoolingCoilPower.GetValue())
Cycle.Condenser.Verbosity =0
Cycle.LineSetSupply.L =float(GUI.txtLineSetL.GetValue())
Cycle.LineSetSupply.OD =float(GUI.txtLineSetOD_supply.GetValue())
Cycle.LineSetSupply.ID =float(GUI.txtLineSetID_supply.GetValue())
Cycle.LineSetSupply.t_insul =float(GUI.txtLineSetInsult.GetValue())
Cycle.LineSetSupply.k_tube =float(GUI.txtLineSetTubek.GetValue())
Cycle.LineSetSupply.k_insul =float(GUI.txtLineSetInsulk.GetValue())
Cycle.LineSetSupply.h_air =float(GUI.txtLineSeth_air.GetValue())
Cycle.LineSetSupply.T_air =float(GUI.txtLineSetT_air.GetValue())
Cycle.LineSetReturn.L =float(GUI.txtLineSetL.GetValue())
Cycle.LineSetReturn.OD =float(GUI.txtLineSetOD_return.GetValue())
Cycle.LineSetReturn.ID =float(GUI.txtLineSetID_return.GetValue())
Cycle.LineSetReturn.t_insul =float(GUI.txtLineSetInsult.GetValue())
Cycle.LineSetReturn.k_tube =float(GUI.txtLineSetTubek.GetValue())
Cycle.LineSetReturn.k_insul =float(GUI.txtLineSetInsulk.GetValue())
Cycle.LineSetReturn.h_air =float(GUI.txtLineSeth_air.GetValue())
Cycle.LineSetReturn.T_air =float(GUI.txtLineSetT_air.GetValue())
Cycle.Charge_target=float(GUI.txtCycleCharge.GetValue())
Cycle.DT_sc_target=float(GUI.txtCycleSubcooling.GetValue())
Cycle.Mode='AC'
Cycle.Ref=str(GUI.cmbRefrigerant.GetValue())
Cycle.Verbosity = 10
Cycle.ParaPath = GUI.txtParaPath.GetValue()
return Cycle