108
Fitting Report for AEG
Description: ASHRAE, Ethylene GlycolSource: American Society of Heating, Refrigerating and Air-Conditioning Engineer...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -35.0 °C to 100.0 °CComposition: 10.0 % to 60.0 %, volume
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
30 0 30 60 90Temperature (°C)
980
1000
1020
1040
1060
1080
1100
Dens
ity (k
g/m
3 )
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 0 30 60 90Temperature (°C)
2800
3000
3200
3400
3600
3800
4000
Heat
Cap
acity
(J/k
g/K)
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)30 0 30 60 90
Temperature (°C)
0.30
0.35
0.40
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.40
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
30 0 30 60 90Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.40
2
1
0
1
2
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.15 0.30 0.45 0.60Volume fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.10
0.05
0.00
0.05
0.10
0.15
rel.
Erro
r (%
)
Fitting Report for AKF
Description: Antifrogen KF, Potassium FormateSource: Technical Data Sheet. Clariant GmbH, 2000.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -40.0 °C to 50.0 °CComposition: 40.0 % to 100.0 %, volume
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 20 0 20 40Temperature (°C)
1150
1200
1250
1300
1350
Dens
ity (k
g/m
3 )
showing x=0.80
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
26002700280029003000310032003300
Heat
Cap
acity
(J/k
g/K)
showing x=0.80
0.1
0.0
0.1
0.2
rel.
Erro
r (%
)40 20 0 20 40
Temperature (°C)
0.425
0.450
0.475
0.500
0.525
0.550
0.575
0.600
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.80
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.80
15
10
5
0
5
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.45 0.60 0.75 0.90Volume fraction
220
230
240
250
260
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for AL
Description: Antifrogen L, Propylene GlycolSource: Technical Data Sheet. Clariant GmbH, 2000.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -40.0 °C to 80.0 °CComposition: 10.0 % to 60.0 %, volume
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
30 0 30 60Temperature (°C)
980
1000
1020
1040
1060
1080
Dens
ity (k
g/m
3 )
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 0 30 60Temperature (°C)
3200
3400
3600
3800
4000
4200
Heat
Cap
acity
(J/k
g/K)
showing x=0.40
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)30 0 30 60
Temperature (°C)
0.35
0.40
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.40
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
30 0 30 60Temperature (°C)
10 3
10 2
10 1
100
Dyna
mic
Visc
osity
(Pas
)
showing x=0.40
1
0
1
2
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.15 0.30 0.45 0.60Volume fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for AN
Description: Antifrogen N, Ethylene GlycolSource: Technical Data Sheet. Clariant GmbH, 2000.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -40.0 °C to 80.0 °CComposition: 10.0 % to 60.0 %, volume
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
30 0 30 60Temperature (°C)
1000
1020
1040
1060
1080
1100
1120
Dens
ity (k
g/m
3 )
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 0 30 60Temperature (°C)
3000
3200
3400
3600
3800
4000
Heat
Cap
acity
(J/k
g/K)
showing x=0.40
0.15
0.10
0.05
0.00
0.05
0.10
0.15
rel.
Erro
r (%
)30 0 30 60
Temperature (°C)
0.35
0.40
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.40
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
30 0 30 60Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.40
4
2
0
2
4
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.15 0.30 0.45 0.60Volume fraction
220
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for APG
Description: ASHRAE, Propylene GlycolSource: American Society of Heating, Refrigerating and Air-Conditioning Engineer...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -35.0 °C to 100.0 °CComposition: 10.0 % to 60.0 %, volume
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
30 0 30 60 90Temperature (°C)
960
980
1000
1020
1040
1060
Dens
ity (k
g/m
3 )
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 0 30 60 90Temperature (°C)
3200
3400
3600
3800
4000
4200
Heat
Cap
acity
(J/k
g/K)
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)30 0 30 60 90
Temperature (°C)
0.30
0.35
0.40
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.40
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
30 0 30 60 90Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.40
2
0
2
4
6
8
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.15 0.30 0.45 0.60Volume fraction
220
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for AS10
Description: Aspen Temper -10, Potassium acetate/formateSource: Technical Data Sheet. Aspen Petroleum AB, 2001.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -10.0 °C to 30.0 °CComposition: pure fluid
Density: coefficients to polynomial (4, 1)Spec. Heat: coefficients to polynomial (3, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: coefficients to polynomial (4, 1)
Psat: no informationTfreeze: no information
Legend: function bounds
10 0 10 20 30Temperature (°C)
1084
1086
1088
1090
1092
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
10 0 10 20 30Temperature (°C)
35203530354035503560357035803590
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)10 0 10 20 30
Temperature (°C)
0.50
0.51
0.52
0.53
0.54
0.55
0.56
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
10 0 10 20 30Temperature (°C)
2 × 10 3
3 × 10 3
4 × 10 3
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for AS20
Description: Aspen Temper -20, Potassium acetate/formateSource: Technical Data Sheet. Aspen Petroleum AB, 2001.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -20.0 °C to 30.0 °CComposition: pure fluid
Density: coefficients to polynomial (4, 1)Spec. Heat: coefficients to polynomial (3, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: equation to exppolynomial (4, 1)
Psat: no informationTfreeze: no information
Legend: function bounds data error
15 0 15 30Temperature (°C)
1140
1142
1144
1146
1148
1150
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
15 0 15 30Temperature (°C)
3200
3220
3240
3260
3280
3300
3320
3340
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)15 0 15 30
Temperature (°C)
0.46
0.47
0.48
0.49
0.50
0.51
0.52
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
15 0 15 30Temperature (°C)
2 × 10 3
3 × 10 3
4 × 10 3
6 × 10 3
Dyna
mic
Visc
osity
(Pas
)
0.20
0.15
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for AS30
Description: Aspen Temper -30, Potassium acetate/formateSource: Technical Data Sheet. Aspen Petroleum AB, 2001.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -30.0 °C to 30.0 °CComposition: pure fluid
Density: coefficients to polynomial (4, 1)Spec. Heat: coefficients to polynomial (3, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: equation to exppolynomial (4, 1)
Psat: no informationTfreeze: no information
Legend: function bounds data error
30 15 0 15 30Temperature (°C)
1175.01177.51180.01182.51185.01187.51190.01192.5
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 15 0 15 30Temperature (°C)
2975300030253050307531003125
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)30 15 0 15 30
Temperature (°C)
0.42
0.44
0.46
0.48
0.50
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 15 0 15 30Temperature (°C)
10 2
Dyna
mic
Visc
osity
(Pas
)
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for AS40
Description: Aspen Temper -40, Potassium acetate/formateSource: Technical Data Sheet. Aspen Petroleum AB, 2001.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -40.0 °C to 30.0 °CComposition: pure fluid
Density: coefficients to polynomial (4, 1)Spec. Heat: coefficients to polynomial (3, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: equation to exppolynomial (4, 1)
Psat: no informationTfreeze: no information
Legend: function bounds data error
40 20 0 20Temperature (°C)
1205
1210
1215
1220
1225
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
2850
2900
2950
3000
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20
Temperature (°C)
0.40
0.42
0.44
0.46
0.48
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
10 2
Dyna
mic
Visc
osity
(Pas
)
0.80.60.40.2
0.00.20.40.6
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for AS55
Description: Aspen Temper -55, Potassium acetate/formateSource: Technical Data Sheet. Aspen Petroleum AB, 2001.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -55.0 °C to 30.0 °CComposition: pure fluid
Density: coefficients to polynomial (4, 1)Spec. Heat: coefficients to polynomial (3, 1)
Th. Cond.: coefficients to polynomial (3, 1)Viscosity: equation to exppolynomial (4, 1)
Psat: no informationTfreeze: no information
Legend: function bounds data error
40 20 0 20Temperature (°C)
1235
1240
1245
1250
1255
1260
1265
1270
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
2650
2700
2750
2800
2850
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20
Temperature (°C)
0.38
0.40
0.42
0.44
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
2
1
0
1
2
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for DEB
Description: Diethylbenzene mixture - Dowtherm JSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -80.0 °C to 100.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: coefficients to exppolynomial (3, 1)
Psat: no informationTfreeze: no information
Legend: function bounds
80 40 0 40 80Temperature (°C)
800
820
840
860
880
900
920
940
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
1600
1700
1800
1900
2000
2100
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40 80
Temperature (°C)
0.12
0.13
0.14
0.15
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for DSF
Description: Dynalene SFSource: Dynalene
Inc.Temperature: 0.0 °C to 315.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to logexponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
0 80 160 240 320Temperature (°C)
700
750
800
850
900
Dens
ity (k
g/m
3 )
3
2
1
0
1
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
2000
2200
2400
2600
2800
3000
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)0 80 160 240 320
Temperature (°C)
0.110
0.115
0.120
0.125
0.130
0.135
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
4
2
0
2
4
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for DowJ
Description: DowthermJSource: Technical Data Sheet. The Dow Chemical Company, 1997.
Temperature: -80.0 °C to 345.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to logexponential (3,)Tfreeze: no information
Legend: data function bounds error
100 0 100 200 300Temperature (°C)
500
600
700
800
900
Dens
ity (k
g/m
3 )
1.0
0.5
0.0
0.5
rel.
Erro
r (%
)
100 0 100 200 300Temperature (°C)
1500
1750
2000
2250
2500
2750
3000
3250
Heat
Cap
acity
(J/k
g/K)
1.0
0.5
0.0
0.5
1.0
1.5
rel.
Erro
r (%
)100 0 100 200 300
Temperature (°C)
0.06
0.08
0.10
0.12
0.14
Ther
mal
Con
duct
ivity
(W/m
/K)
0.50.40.30.20.1
0.00.10.2
rel.
Erro
r (%
)
100 0 100 200 300Temperature (°C)
10 64
10 33
10 2
1029
1060
1091
10122
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
100 0 100 200 300Temperature (°C)
103
104
105
106
Satu
ratio
n Pr
essu
re (P
a)
42
0246810
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for DowJ2
Description: Dowtherm J, Diethylbenzene mixtureSource: Technical Data Sheet. The Dow Chemical Company, 1997.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -73.0 °C to 315.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
0 100 200 300Temperature (°C)
550600650700750800850900950
Dens
ity (k
g/m
3 )
0.4
0.2
0.0
0.2
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
16001800200022002400260028003000
Heat
Cap
acity
(J/k
g/K)
0.4
0.2
0.0
0.2
0.4
0.6
0.8
rel.
Erro
r (%
)0 100 200 300
Temperature (°C)
0.110
0.115
0.120
0.125
0.130
0.135
0.140
Ther
mal
Con
duct
ivity
(W/m
/K)
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
4
2
0
2
4
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for DowQ
Description: DowthermQSource: Technical Data Sheet. The Dow Chemical Company, 1997.
Temperature: -35.0 °C to 360.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 100 200 300Temperature (°C)
700
750
800
850
900
950
1000
Dens
ity (k
g/m
3 )
0.1
0.0
0.1
0.2
0.3
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
1600
1800
2000
2200
2400
2600
Heat
Cap
acity
(J/k
g/K)
0.060.040.02
0.000.020.040.060.08
rel.
Erro
r (%
)0 100 200 300
Temperature (°C)
0.07
0.08
0.09
0.10
0.11
0.12
0.13
Ther
mal
Con
duct
ivity
(W/m
/K)
0.100
0.075
0.050
0.025
0.000
0.025
0.050
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
10 76
10 64
10 52
10 40
10 28
10 16
10 4
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
10 64
10 33
10 2
1029
1060
1091
10122
Satu
ratio
n Pr
essu
re (P
a)
100
80
60
40
20
0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for DowQ2
Description: Dowtherm Q, Diphenylethane/alkylated aromaticsSource: Technical Data Sheet. The Dow Chemical Company, 1997.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -35.0 °C to 330.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
0 100 200 300Temperature (°C)
750
800
850
900
950
1000
Dens
ity (k
g/m
3 )
0.20
0.15
0.10
0.05
0.00
0.05
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
1600
1800
2000
2200
2400
2600
Heat
Cap
acity
(J/k
g/K)
0.15
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)0 100 200 300
Temperature (°C)
0.09
0.10
0.11
0.12
0.13
Ther
mal
Con
duct
ivity
(W/m
/K)
1.5
1.0
0.5
0.0
0.5
1.0
1.5
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
10 64
10 33
10 2
1029
1060
1091
10122
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for FRE
Description: Freezium, Potassium FormateSource: Technical Data Sheet. Kemira Chemicals OY, 1998.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -40.14999999999998 °C to 39.85000000000002 °CComposition: 19.0 % to 50.0 %, mass
Density: coefficients to polynomial (2, 3)Spec. Heat: equation to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (2, 2)Viscosity: equation to exppolynomial (4, 6)
Psat: no informationTfreeze: equation to polynomial (1, 6)
Legend: function bounds data error
40 20 0 20 40Temperature (°C)
1100
1150
1200
1250
1300
1350
Dens
ity (k
g/m
3 )
showing x=0.34
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
2600
2800
3000
3200
3400
3600
Heat
Cap
acity
(J/k
g/K)
showing x=0.35
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20 40
Temperature (°C)
0.450
0.475
0.500
0.525
0.550
0.575
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.34
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.35
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.24 0.32 0.40 0.48Mass fraction
220
230
240
250
260
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for GKN
Description: Glykosol N, Ethylene GlycolSource: Technical Data Sheet. pro Kühlsole GmbH, 2005.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -53.0 °C to 100.0 °CComposition: 10.0 % to 60.0 %, volume
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 0 40 80Temperature (°C)
975
1000
1025
1050
1075
1100
1125
Dens
ity (k
g/m
3 )
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
3000
3200
3400
3600
3800
4000
4200
Heat
Cap
acity
(J/k
g/K)
showing x=0.40
0.15
0.10
0.05
0.00
0.05
0.10
0.15
rel.
Erro
r (%
)40 0 40 80
Temperature (°C)
0.35
0.40
0.45
0.50
0.55
0.60
0.65
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.40
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
10 3
10 2
10 1
100
Dyna
mic
Visc
osity
(Pas
)
showing x=0.40
0.6
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.15 0.30 0.45 0.60Volume fraction
220
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.08
0.06
0.04
0.02
0.00
0.02
0.04
0.06
rel.
Erro
r (%
)
Fitting Report for HC10
Description: Dynalene HC10Source: Technical Data Sheet. Dynalene Inc., 2014.
Temperature: -10.0 °C to 218.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 60 120 180Temperature (°C)
1100
1120
1140
1160
1180
1200
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
3300
3400
3500
3600
3700
3800
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)0 60 120 180
Temperature (°C)
0.50
0.55
0.60
0.65
0.70
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
10 3
Dyna
mic
Visc
osity
(Pas
)
0.500.25
0.000.250.500.751.001.25
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
10 40
10 33
10 26
10 19
10 12
10 5
102
Satu
ratio
n Pr
essu
re (P
a)
100
80
60
40
20
0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HC20
Description: Dynalene HC20Source: Technical Data Sheet. Dynalene Inc., 2014.
Temperature: -19.99999999999997 °C to 210.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 60 120 180Temperature (°C)
1140
1160
1180
1200
1220
1240
1260
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
3100
3200
3300
3400
3500
3600
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)0 60 120 180
Temperature (°C)
0.50
0.55
0.60
0.65
0.70
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
10 3
Dyna
mic
Visc
osity
(Pas
)
1.0
0.5
0.0
0.5
1.0
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
10 39
10 32
10 25
10 18
10 11
10 4
103
Satu
ratio
n Pr
essu
re (P
a)
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
1e10
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HC30
Description: Dynalene HC30Source: Technical Data Sheet. Dynalene Inc., 2014.
Temperature: -29.99999999999997 °C to 210.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 60 120 180Temperature (°C)
1180
1200
1220
1240
1260
1280
1300
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
3000
3100
3200
3300
3400
3500
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)0 60 120 180
Temperature (°C)
0.50
0.55
0.60
0.65
0.70
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
10 3
Dyna
mic
Visc
osity
(Pas
)
2.0
1.5
1.0
0.5
0.0
0.5
1.0
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
10 34
10 28
10 22
10 16
10 10
10 4
102
108
Satu
ratio
n Pr
essu
re (P
a)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HC40
Description: Dynalene HC40Source: Technical Data Sheet. Dynalene Inc., 2014.
Temperature: -39.99999999999997 °C to 200.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 60 120 180Temperature (°C)
1220
1240
1260
1280
1300
1320
1340
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
2800
2900
3000
3100
3200
3300
Heat
Cap
acity
(J/k
g/K)
0.15
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)0 60 120 180
Temperature (°C)
0.45
0.50
0.55
0.60
0.65
0.70
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
10 34
10 29
10 24
10 19
10 14
10 9
10 4
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 60 120 180Temperature (°C)
10 34
10 28
10 22
10 16
10 10
10 4
102
108
Satu
ratio
n Pr
essu
re (P
a)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HC50
Description: Dynalene HC50Source: Technical Data Sheet. Dynalene Inc., 2014.
Temperature: -49.99999999999997 °C to 210.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
60 0 60 120 180Temperature (°C)
12401260128013001320134013601380
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
60 0 60 120 180Temperature (°C)
2600
2700
2800
2900
3000
3100
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)60 0 60 120 180
Temperature (°C)
0.45
0.50
0.55
0.60
0.65
0.70
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
60 0 60 120 180Temperature (°C)
10 22
10 18
10 14
10 10
10 6
10 2
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
60 0 60 120 180Temperature (°C)
10 21
10 16
10 11
10 6
10 1
104
Satu
ratio
n Pr
essu
re (P
a)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HCB
Description: Hydrocarbon blend - Dynalene MVSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -80.0 °C to 100.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: coefficients to exppolynomial (3, 1)
Psat: no informationTfreeze: no information
Legend: function bounds
80 40 0 40 80Temperature (°C)
780
800
820
840
860
880
900
920
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
1500
1600
1700
1800
1900
2000
2100
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40 80
Temperature (°C)
0.12
0.13
0.14
0.15
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HCM
Description: Hydrocarbon mixture - Gilotherm D12Source: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -80.0 °C to 100.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: coefficients to exppolynomial (3, 1)
Psat: no informationTfreeze: no information
Legend: function bounds
80 40 0 40 80Temperature (°C)
700
720
740
760
780
800
820
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
1800
2000
2200
2400
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40 80
Temperature (°C)
0.100
0.105
0.110
0.115
0.120
0.125
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HFE
Description: Hydrofluoroether - HFE-7100 3M NovecSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -80.0 °C to 100.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: coefficients to exppolynomial (3, 1)
Psat: no informationTfreeze: no information
Legend: function bounds
80 40 0 40 80Temperature (°C)
1475
1500
1525
1550
1575
1600
1625
1650
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
1050
1075
1100
1125
1150
1175
1200
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40 80
Temperature (°C)
0.9625
0.9650
0.9675
0.9700
0.9725
0.9750
0.9775
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
10 3
6 × 10 4
2 × 10 3
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HFE2
Description: HFE-7100, HydrofluoroetherSource: Technical Information. 3M Company, 2007.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -80.32999999999998 °C to 64.26999999999998 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
80 40 0 40Temperature (°C)
1400
1450
1500
1550
1600
1650
1700
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
1000
1050
1100
1150
1200
1250
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.060
0.065
0.070
0.075
0.080
0.085
0.090
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 3
Dyna
mic
Visc
osity
(Pas
)
2
0
2
4
6
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HY20
Description: HYCOOL 20, Potassium formateSource: Technical Information. Hydro Chemicals, 2000.
Temperature: -20.0 °C to 50.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: equation to polynomial (4, 1)Viscosity: equation to exponential (3,)
Psat: no informationTfreeze: no information
Legend: function bounds data error
20 0 20 40Temperature (°C)
1180
1185
1190
1195
1200
1205
1210
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
20 0 20 40Temperature (°C)
2925
2950
2975
3000
3025
3050
3075
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)20 0 20 40
Temperature (°C)
0.48
0.50
0.52
0.54
0.56
0.58
Ther
mal
Con
duct
ivity
(W/m
/K)
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
20 0 20 40Temperature (°C)
10 3
2 × 10 3
3 × 10 3
4 × 10 3
Dyna
mic
Visc
osity
(Pas
)
2
1
0
1
2
3
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HY30
Description: HyCool 30, Potassium formateSource: Technical Information. Hydro Chemicals, 2000.
Temperature: -30.0 °C to 50.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: equation to polynomial (4, 1)Viscosity: equation to exponential (3,)
Psat: no informationTfreeze: no information
Legend: function bounds data error
20 0 20 40Temperature (°C)
1240
1250
1260
1270
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
20 0 20 40Temperature (°C)
2750
2800
2850
2900
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)20 0 20 40
Temperature (°C)
0.44
0.46
0.48
0.50
0.52
0.54
0.56
Ther
mal
Con
duct
ivity
(W/m
/K)
0.3
0.2
0.1
0.0
0.1
0.2
0.3
0.4
rel.
Erro
r (%
)
20 0 20 40Temperature (°C)
2 × 10 3
3 × 10 3
4 × 10 3
6 × 10 3
Dyna
mic
Visc
osity
(Pas
)
1.00
0.75
0.50
0.25
0.00
0.25
0.50
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HY40
Description: HyCool 40, Potassium formateSource: Technical Information. Hydro Chemicals, 2000.
Temperature: -40.0 °C to 20.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: equation to exponential (3,)
Psat: no informationTfreeze: no information
Legend: function bounds data error
30 15 0 15Temperature (°C)
1295
1300
1305
1310
1315
1320
1325
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 15 0 15Temperature (°C)
2560
2580
2600
2620
2640
2660
2680
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)30 15 0 15
Temperature (°C)
0.42
0.44
0.46
0.48
0.50
0.52
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 15 0 15Temperature (°C)
10 2
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HY45
Description: HyCool 45, Potassium formateSource: Technical Information. Hydro Chemicals, 2000.
Temperature: -45.0 °C to 20.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: equation to exponential (3,)
Psat: no informationTfreeze: no information
Legend: function bounds data error
45 30 15 0 15Temperature (°C)
1320
1325
1330
1335
1340
1345
1350
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
45 30 15 0 15Temperature (°C)
2475
2500
2525
2550
2575
2600
2625
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)45 30 15 0 15
Temperature (°C)
0.40
0.42
0.44
0.46
0.48
0.50
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
45 30 15 0 15Temperature (°C)
10 2
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for HY50
Description: HyCool 50, Potassium formateSource: Technical Information. Hydro Chemicals, 2000.
Temperature: -50.0 °C to 20.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: equation to exponential (3,)
Psat: no informationTfreeze: no information
Legend: function bounds data error
40 20 0 20Temperature (°C)
1350
1360
1370
1380
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
2375
2400
2425
2450
2475
2500
2525
2550
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20
Temperature (°C)
0.38
0.40
0.42
0.44
0.46
0.48
0.50
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
10 2
Dyna
mic
Visc
osity
(Pas
)
1.5
1.0
0.5
0.0
0.5
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for IceEA
Description: Ice slurry with EthanolSource: Michael Kauffeld. RP-1166 Behavior of Ice Slurries in Thermal Storage Sy...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -33.14999999999998 °C to -8.149999999999977 °CComposition: 5.0 % to 35.0 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: no informationViscosity: no information
Psat: no informationTfreeze: no information
Legend: data function bounds error
30 24 18 12Temperature (°C)
945
950
955
960
965
970
975
Dens
ity (k
g/m
3 )
showing x=0.25
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 24 18 12Temperature (°C)
20000
40000
60000
80000
100000
120000
140000
Heat
Cap
acity
(J/k
g/K)
showing x=0.25
0.2
0.1
0.0
0.1
0.2
rel.
Erro
r (%
)0.0 0.2 0.4 0.6 0.8 1.0
Temperature (°C)
0.0
0.2
0.4
0.6
0.8
1.0
Ther
mal
Con
duct
ivity
(W/m
/K)
No conductivity information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Dyna
mic
Visc
osity
(Pas
)
No viscosity information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for IceNA
Description: Ice slurry with NaClSource: Michael Kauffeld. RP-1166 Behavior of Ice Slurries in Thermal Storage Sy...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -18.149999999999977 °C to -3.1499999999999773 °CComposition: 5.0 % to 35.0 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: no informationViscosity: no information
Psat: no informationTfreeze: no information
Legend: data function bounds error
16 12 8 4Temperature (°C)
1000
1025
1050
1075
1100
1125
1150
Dens
ity (k
g/m
3 )
showing x=0.25
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
16 12 8 4Temperature (°C)
20000
40000
60000
80000
100000
120000
140000
Heat
Cap
acity
(J/k
g/K)
showing x=0.25
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)0.0 0.2 0.4 0.6 0.8 1.0
Temperature (°C)
0.0
0.2
0.4
0.6
0.8
1.0
Ther
mal
Con
duct
ivity
(W/m
/K)
No conductivity information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Dyna
mic
Visc
osity
(Pas
)
No viscosity information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for IcePG
Description: Ice slurry with Propylene GlycolSource: Michael Kauffeld. RP-1166 Behavior of Ice Slurries in Thermal Storage Sy...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -43.14999999999998 °C to -8.149999999999977 °CComposition: 5.0 % to 35.0 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: no informationViscosity: no information
Psat: no informationTfreeze: no information
Legend: data function bounds error
40 32 24 16 8Temperature (°C)
980
1000
1020
1040
1060
Dens
ity (k
g/m
3 )
showing x=0.25
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 32 24 16 8Temperature (°C)
25000
50000
75000
100000
125000
150000
175000
Heat
Cap
acity
(J/k
g/K)
showing x=0.25
0.1
0.0
0.1
0.2
0.3
rel.
Erro
r (%
)0.0 0.2 0.4 0.6 0.8 1.0
Temperature (°C)
0.0
0.2
0.4
0.6
0.8
1.0
Ther
mal
Con
duct
ivity
(W/m
/K)
No conductivity information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Dyna
mic
Visc
osity
(Pas
)
No viscosity information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for LiBr
Description: Lithium-bromide solution - aqSource: Jaroslav Pátek and Jaroslav Klomfar. A computationally effective formula...
Temperature: -0.14999999999997726 °C to 226.85000000000002 °CComposition: 0.0 % to 75.0 %, mass
Density: equation to polynomial (4, 6)Spec. Heat: equation to polynomial (4, 6)
Th. Cond.: no informationViscosity: no information
Psat: equation to exppolynomial (4, 6)Tfreeze: no information
Legend: data function bounds error
0 50 100 150 200Temperature (°C)
800
1000
1200
1400
1600
1800
2000
Dens
ity (k
g/m
3 )
showing x=0.39
0.075
0.050
0.025
0.000
0.025
0.050
0.075
rel.
Erro
r (%
)
0 50 100 150 200Temperature (°C)
10001500200025003000350040004500
Heat
Cap
acity
(J/k
g/K)
showing x=0.39
3
2
1
0
1
rel.
Erro
r (%
)0.0 0.2 0.4 0.6 0.8 1.0
Temperature (°C)
0.0
0.2
0.4
0.6
0.8
1.0
Ther
mal
Con
duct
ivity
(W/m
/K)
No conductivity information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Dyna
mic
Visc
osity
(Pas
)
No viscosity information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
150 0 150Temperature (°C)
101
102
103
104
105
106
Satu
ratio
n Pr
essu
re (P
a)
showing x=0.39
2
1
0
1
2
3
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for MAM
Description: Ammonia (NH3) - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 30.0 °CComposition: 0.0 % to 30.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
90 60 30 0 30Temperature (°C)
880
900
920
940
960
980
1000
Dens
ity (k
g/m
3 )
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
90 60 30 0 30Temperature (°C)
4200
4300
4400
4500
4600
Heat
Cap
acity
(J/k
g/K)
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)90 60 30 0 30
Temperature (°C)
0.30
0.35
0.40
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
90 60 30 0 30Temperature (°C)
10 3
10 2
10 1
100
Dyna
mic
Visc
osity
(Pas
)
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.08 0.16 0.24Mass fraction
200
220
240
260
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MAM2
Description: Melinder, AmmoniaSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -49.0 °C to 20.0 °CComposition: 7.8 % to 23.6 %, mass
Density: data to polynomial (4, 5)Spec. Heat: data to polynomial (4, 5)
Th. Cond.: data to polynomial (4, 5)Viscosity: data to exppolynomial (4, 5)
Psat: no informationTfreeze: data to exppolynomial (1, 5)
Legend: data function bounds error
40 20 0 20Temperature (°C)
910
920
930
940
950
960
970
Dens
ity (k
g/m
3 )
showing x=0.14
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
4200
4225
4250
4275
4300
4325
4350
Heat
Cap
acity
(J/k
g/K)
showing x=0.14
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20
Temperature (°C)
0.35
0.40
0.45
0.50
0.55
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.14
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.14
0.3
0.2
0.1
0.0
0.1
0.2
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.08 0.12 0.16 0.20 0.24Mass fraction
230
240
250
260
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MCA
Description: Calcium Chloride (CaCl2) - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 40.0 °CComposition: 0.0 % to 30.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
80 40 0 40Temperature (°C)
1000
1050
1100
1150
1200
1250
1300
Dens
ity (k
g/m
3 )
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
2750
3000
3250
3500
3750
4000
4250
Heat
Cap
acity
(J/k
g/K)
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.475
0.500
0.525
0.550
0.575
0.600
0.625
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.08 0.16 0.24Mass fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MCA2
Description: Melinder, Calcium ChlorideSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -44.0 °C to 30.0 °CComposition: 9.0 % to 29.4 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 20 0 20Temperature (°C)
1100
1150
1200
1250
1300
Dens
ity (k
g/m
3 )
showing x=0.19
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
2600
2800
3000
3200
3400
3600
Heat
Cap
acity
(J/k
g/K)
showing x=0.19
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20
Temperature (°C)
0.48
0.50
0.52
0.54
0.56
0.58
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.19
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.19
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.10 0.15 0.20 0.25 0.30Mass fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MEA
Description: Ethyl Alcohol (Ethanol) - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 40.0 °CComposition: 0.0 % to 60.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
80 40 0 40Temperature (°C)
880
900
920
940
960
980
1000
Dens
ity (k
g/m
3 )
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
27503000325035003750400042504500
Heat
Cap
acity
(J/k
g/K)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.300.350.400.450.500.550.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.15 0.30 0.45 0.60Mass fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MEA2
Description: Melinder, EthanolSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -44.0 °C to 20.0 °CComposition: 11.0 % to 60.0 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
45 30 15 0 15Temperature (°C)
900
920
940
960
980
Dens
ity (k
g/m
3 )
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
45 30 15 0 15Temperature (°C)
3200
3400
3600
3800
4000
4200
4400
Heat
Cap
acity
(J/k
g/K)
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)45 30 15 0 15
Temperature (°C)
0.30
0.35
0.40
0.45
0.50
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
45 30 15 0 15Temperature (°C)
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.15 0.30 0.45 0.60Mass fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MEG
Description: Ethylene Glycol - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 100.0 °CComposition: 0.0 % to 60.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
100 50 0 50 100Temperature (°C)
950
975
1000
1025
1050
1075
1100
Dens
ity (k
g/m
3 )
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
100 50 0 50 100Temperature (°C)
2750
3000
3250
3500
3750
4000
4250
Heat
Cap
acity
(J/k
g/K)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)100 50 0 50 100
Temperature (°C)
0.350.400.450.500.550.600.65
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
100 50 0 50 100Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.15 0.30 0.45 0.60Mass fraction
220
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MEG2
Description: Melinder, Ethylene GlycolSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -44.0 °C to 40.0 °CComposition: 0.0 % to 56.00000000000001 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 20 0 20 40Temperature (°C)
1000
1020
1040
1060
1080
1100
Dens
ity (k
g/m
3 )
showing x=0.26
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
28003000320034003600380040004200
Heat
Cap
acity
(J/k
g/K)
showing x=0.26
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20 40
Temperature (°C)
0.35
0.40
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.26
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.26
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.15 0.30 0.45Mass fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MGL
Description: Glycerol - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 40.0 °CComposition: 0.0 % to 60.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
80 40 0 40Temperature (°C)
1000
1050
1100
1150
Dens
ity (k
g/m
3 )
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
2750
3000
3250
3500
3750
4000
4250
Heat
Cap
acity
(J/k
g/K)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.35
0.40
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.15 0.30 0.45 0.60Mass fraction
240
245
250
255
260
265
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MGL2
Description: Melinder, GlycerolSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -40.0 °C to 40.0 °CComposition: 19.5 % to 63.0 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 20 0 20 40Temperature (°C)
1050
1075
1100
1125
1150
1175
Dens
ity (k
g/m
3 )
showing x=0.43
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
2600
2800
3000
3200
3400
3600
3800
Heat
Cap
acity
(J/k
g/K)
showing x=0.43
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20 40
Temperature (°C)
0.35
0.40
0.45
0.50
0.55
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.43
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
10 3
10 2
10 1
100
Dyna
mic
Visc
osity
(Pas
)
showing x=0.43
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.2 0.3 0.4 0.5 0.6Mass fraction
235240245250255260265270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MITSW
Description: MIT SeawaterSource: Mostafa H. Sharqawy, John H. Lienhard V, and Syed M. Zubair. Thermophysi...
Temperature: 0.0 °C to 120.0 °CComposition: 0.0 % to 12.0 %, mass
Density: equation to polynomial (4, 6)Spec. Heat: equation to polynomial (4, 6)
Th. Cond.: equation to polynomial (4, 6)Viscosity: equation to exppolynomial (4, 6)
Psat: equation to exppolynomial (4, 6)Tfreeze: no information
Legend: data function bounds error
0 30 60 90 120Temperature (°C)
950
975
1000
1025
1050
1075
1100
Dens
ity (k
g/m
3 )
showing x=0.06
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 30 60 90 120Temperature (°C)
3600
3700
3800
3900
4000
4100
4200
Heat
Cap
acity
(J/k
g/K)
showing x=0.06
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)0 30 60 90 120
Temperature (°C)
0.56
0.58
0.60
0.62
0.64
0.66
0.68
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.06
0.06
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 30 60 90 120Temperature (°C)
10 3
Dyna
mic
Visc
osity
(Pas
)
showing x=0.06
0.75
0.50
0.25
0.00
0.25
0.50
0.75
rel.
Erro
r (%
)
200 100 0 100Temperature (°C)
103
104
105
Satu
ratio
n Pr
essu
re (P
a)
showing x=0.06
0.2
0.1
0.0
0.1
0.2
0.3
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for MKA
Description: Potassium Acetate (CH3CO2K) - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 40.0 °CComposition: 0.0 % to 45.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
80 40 0 40Temperature (°C)
1000
1050
1100
1150
1200
1250
Dens
ity (k
g/m
3 )
showing x=0.23
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
2750
3000
3250
3500
3750
4000
4250
Heat
Cap
acity
(J/k
g/K)
showing x=0.23
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.40
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.23
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.23
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.1 0.2 0.3 0.4Mass fraction
220
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MKA2
Description: Melinder, Potassium AcetateSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -44.0 °C to 30.0 °CComposition: 11.0 % to 41.0 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 20 0 20Temperature (°C)
1050
1100
1150
1200
1250
Dens
ity (k
g/m
3 )
showing x=0.31
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
2800
3000
3200
3400
3600
3800
Heat
Cap
acity
(J/k
g/K)
showing x=0.31
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20
Temperature (°C)
0.4000.4250.4500.4750.5000.5250.5500.575
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.31
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.31
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.16 0.24 0.32 0.40Mass fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MKC
Description: Potassium Carbonate (K2CO3) - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 40.0 °CComposition: 0.0 % to 40.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
80 40 0 40Temperature (°C)
1000
1100
1200
1300
1400
Dens
ity (k
g/m
3 )
showing x=0.20
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
2750
3000
3250
3500
3750
4000
4250
Heat
Cap
acity
(J/k
g/K)
showing x=0.20
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.475
0.500
0.525
0.550
0.575
0.600
0.625
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.20
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.20
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.1 0.2 0.3 0.4Mass fraction
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MKC2
Description: Melinder, Potassium CarbonateSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -35.0 °C to 30.0 °CComposition: 0.0 % to 39.0 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
30 15 0 15 30Temperature (°C)
1000
1100
1200
1300
1400
Dens
ity (k
g/m
3 )
showing x=0.19
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 15 0 15 30Temperature (°C)
2750
3000
3250
3500
3750
4000
4250
Heat
Cap
acity
(J/k
g/K)
showing x=0.19
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)30 15 0 15 30
Temperature (°C)
0.480.500.520.540.560.580.600.62
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.19
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 15 0 15 30Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.19
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.1 0.2 0.3 0.4Mass fraction
240245250255260265270275
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MKF
Description: Potassium Formate (CHKO2) - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 40.0 °CComposition: 0.0 % to 48.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
80 40 0 40Temperature (°C)
10001050110011501200125013001350
Dens
ity (k
g/m
3 )
showing x=0.24
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
2500
2750
3000
3250
3500
3750
4000
4250
Heat
Cap
acity
(J/k
g/K)
showing x=0.24
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.24
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.24
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.15 0.30 0.45Mass fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MLI
Description: Lithium Chloride (LiCl) - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 40.0 °CComposition: 0.0 % to 24.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
80 40 0 40Temperature (°C)
1000
1025
1050
1075
1100
1125
1150
Dens
ity (k
g/m
3 )
showing x=0.12
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
2750
3000
3250
3500
3750
4000
4250
Heat
Cap
acity
(J/k
g/K)
showing x=0.12
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.12
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.12
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.06 0.12 0.18 0.24Mass fraction
210
220
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MMA
Description: Methyl Alcohol (Methanol) - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 40.0 °CComposition: 0.0 % to 60.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
80 40 0 40Temperature (°C)
880
900
920
940
960
980
1000
Dens
ity (k
g/m
3 )
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
2500
3000
3500
4000
Heat
Cap
acity
(J/k
g/K)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.30
0.35
0.40
0.45
0.50
0.55
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.15 0.30 0.45 0.60Mass fraction
200
220
240
260
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MMA2
Description: Melinder, MethanolSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -50.0 °C to 20.0 °CComposition: 7.8 % to 47.4 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 20 0 20Temperature (°C)
920
930
940
950
960
970
980
990
Dens
ity (k
g/m
3 )
showing x=0.27
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
3200
3400
3600
3800
4000
4200
Heat
Cap
acity
(J/k
g/K)
showing x=0.27
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20
Temperature (°C)
0.35
0.40
0.45
0.50
0.55
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.27
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.27
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.1 0.2 0.3 0.4Mass fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MMG
Description: MgCl2 - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 40.0 °CComposition: 0.0 % to 30.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
80 40 0 40Temperature (°C)
1000
1100
1200
1300
Dens
ity (k
g/m
3 )
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
2500
3000
3500
4000
Heat
Cap
acity
(J/k
g/K)
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.0
0.2
0.4
0.6
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 2
100
102
104
106
Dyna
mic
Visc
osity
(Pas
)
showing x=0.15
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.08 0.16 0.24Mass fraction
180
200
220
240
260
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MMG2
Description: Melinder, Magnesium ChlorideSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -30.0 °C to 30.0 °CComposition: 0.0 % to 20.5 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
30 15 0 15 30Temperature (°C)
1000
1050
1100
1150
1200
Dens
ity (k
g/m
3 )
showing x=0.10
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 15 0 15 30Temperature (°C)
3000
3200
3400
3600
3800
4000
4200
Heat
Cap
acity
(J/k
g/K)
showing x=0.10
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)30 15 0 15 30
Temperature (°C)
0.475
0.500
0.525
0.550
0.575
0.600
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.10
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 15 0 15 30Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.10
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.05 0.10 0.15 0.20Mass fraction
245
250
255
260
265
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MNA
Description: Sodium Chloride (NaCl) - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 40.0 °CComposition: 0.0 % to 23.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
80 40 0 40Temperature (°C)
1000
1050
1100
1150
1200
Dens
ity (k
g/m
3 )
showing x=0.12
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
3400
3600
3800
4000
4200
Heat
Cap
acity
(J/k
g/K)
showing x=0.12
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40
Temperature (°C)
0.52
0.54
0.56
0.58
0.60
0.62
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.12
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40Temperature (°C)
10 3
Dyna
mic
Visc
osity
(Pas
)
showing x=0.12
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.06 0.12 0.18 0.24Mass fraction
255
260
265
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MNA2
Description: Melinder, Sodium ChlorideSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -20.0 °C to 30.0 °CComposition: 0.0 % to 23.0 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
15 0 15 30Temperature (°C)
1000
1050
1100
1150
1200
Dens
ity (k
g/m
3 )
showing x=0.13
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
15 0 15 30Temperature (°C)
3400
3600
3800
4000
4200
Heat
Cap
acity
(J/k
g/K)
showing x=0.13
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)15 0 15 30
Temperature (°C)
0.52
0.54
0.56
0.58
0.60
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.13
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
15 0 15 30Temperature (°C)
10 3Dyna
mic
Visc
osity
(Pas
)
showing x=0.13
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.06 0.12 0.18 0.24Mass fraction
255
260
265
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MPG
Description: Propylene Glycol - aqSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -100.0 °C to 100.0 °CComposition: 0.0 % to 60.0 %, mass
Density: coefficients to polynomial (4, 6)Spec. Heat: coefficients to polynomial (4, 6)
Th. Cond.: coefficients to polynomial (4, 6)Viscosity: coefficients to exppolynomial (4, 6)
Psat: no informationTfreeze: coefficients to polynomial (1, 6)
Legend: function bounds
100 50 0 50 100Temperature (°C)
960
980
1000
1020
1040
1060
1080
Dens
ity (k
g/m
3 )
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
100 50 0 50 100Temperature (°C)
3000
3200
3400
3600
3800
4000
4200
Heat
Cap
acity
(J/k
g/K)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)100 50 0 50 100
Temperature (°C)
0.3
0.4
0.5
0.6
0.7
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
100 50 0 50 100Temperature (°C)
10 3
10 2
10 1
100
Dyna
mic
Visc
osity
(Pas
)
showing x=0.30
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.15 0.30 0.45 0.60Mass fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for MPG2
Description: Melinder, Propylene GlycolSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -45.0 °C to 40.0 °CComposition: 15.0 % to 57.00000000000001 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 20 0 20 40Temperature (°C)
10001010102010301040105010601070
Dens
ity (k
g/m
3 )
showing x=0.37
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
3400
3600
3800
4000
Heat
Cap
acity
(J/k
g/K)
showing x=0.37
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 20 0 20 40
Temperature (°C)
0.30
0.35
0.40
0.45
0.50
0.55
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.37
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
10 3
10 2
10 1
100
Dyna
mic
Visc
osity
(Pas
)
showing x=0.37
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.2 0.3 0.4 0.5Mass fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for NBS
Description: NBS, WaterSource: Ernst Schmidt. Properties of Water and Steam in SI-Units. Springer, 2nd ...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: 1.0 °C to 100.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
0 25 50 75 100Temperature (°C)
960
970
980
990
1000
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 25 50 75 100Temperature (°C)
4180
4190
4200
4210
Heat
Cap
acity
(J/k
g/K)
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)0 25 50 75 100
Temperature (°C)
0.56
0.58
0.60
0.62
0.64
0.66
0.68
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 25 50 75 100Temperature (°C)
10 3
3 × 10 4
4 × 10 4
6 × 10 4
Dyna
mic
Visc
osity
(Pas
)
0.4
0.2
0.0
0.2
0.4
0.6
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for NaK
Description: Nitrate salt, 0.6 NaNO3 and 0.4 KNO3Source: Alexis B. Zavoico. Solar Power Tower Design Basis Document. Technical Re...
Temperature: 300.0 °C to 600.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: coefficients to polynomial (4, 1)
Psat: no informationTfreeze: no information
Legend: function bounds
320 400 480 560Temperature (°C)
1700
1750
1800
1850
1900
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
320 400 480 560Temperature (°C)
1500
1510
1520
1530
1540
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)320 400 480 560
Temperature (°C)
0.50
0.51
0.52
0.53
0.54
0.55
0.56
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
320 400 480 560Temperature (°C)
10 3
2 × 10 3
3 × 10 3
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PBB
Description: Pirobloc HTF-BASICSource: http://www.fluidotermico.com
Temperature: 50.0 °C to 300.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
60 120 180 240 300Temperature (°C)
700
725
750
775
800
825
850
Dens
ity (k
g/m
3 )
0.06
0.04
0.02
0.00
0.02
0.04
0.06
rel.
Erro
r (%
)
60 120 180 240 300Temperature (°C)
2000
2200
2400
2600
2800
3000
Heat
Cap
acity
(J/k
g/K)
0.15
0.10
0.05
0.00
0.05
0.10
0.15
rel.
Erro
r (%
)60 120 180 240 300
Temperature (°C)
0.110
0.115
0.120
0.125
0.130
Ther
mal
Con
duct
ivity
(W/m
/K)
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
60 120 180 240 300Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
2
1
0
1
2
3
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PCL
Description: Paracryol, Aliphatic HydrocarbonSource: Technical Information. Sulzer Chemtech AG, 1999.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -40.0 °C to 180.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
50 0 50 100 150Temperature (°C)
675
700
725
750
775
800
825
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
50 0 50 100 150Temperature (°C)
1800
2000
2200
2400
2600
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)50 0 50 100 150
Temperature (°C)
0.1350
0.1375
0.1400
0.1425
0.1450
0.1475
0.1500
0.1525
Ther
mal
Con
duct
ivity
(W/m
/K)
0.3
0.2
0.1
0.0
0.1
0.2
0.3
rel.
Erro
r (%
)
50 0 50 100 150Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
4
2
0
2
4
6
8
10
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PCR
Description: Paratherm CRSource: Thermal Properties Calculator v6.4. Paratherm Ltd., 2013. URL: http://pa...
Temperature: -99.99999999999997 °C to 220.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to logexponential (3,)Tfreeze: no information
Legend: data function bounds error
80 0 80 160Temperature (°C)
650
700
750
800
850
900
950
Dens
ity (k
g/m
3 )
0.060.040.02
0.000.020.040.060.08
rel.
Erro
r (%
)
80 0 80 160Temperature (°C)
1400
1600
1800
2000
2200
2400
2600
Heat
Cap
acity
(J/k
g/K)
3
2
1
0
1
2
3
rel.
Erro
r (%
)
80 0 80 160Temperature (°C)
0.125
0.130
0.135
0.140
0.145
0.150
Ther
mal
Con
duct
ivity
(W/m
/K)
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
80 0 80 160Temperature (°C)
10 127
10 77
10 27
1023
1073
10123
10173
10223
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
80 0 80 160Temperature (°C)
104
105
Satu
ratio
n Pr
essu
re (P
a)
4
2
0
2
4
6
8
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PGLT
Description: Paratherm GLTSource: Thermal Properties Calculator v6.4. Paratherm Ltd., 2013. URL: http://pa...
Temperature: -15.0 °C to 315.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 80 160 240 320Temperature (°C)
700
750
800
850
900
Dens
ity (k
g/m
3 )
0.06
0.04
0.02
0.00
0.02
0.04
0.06
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
1800
2000
2200
2400
2600
2800
Heat
Cap
acity
(J/k
g/K)
2
1
0
1
2
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
0.110
0.115
0.120
0.125
0.130
0.135
Ther
mal
Con
duct
ivity
(W/m
/K)
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
10 127
10 77
10 27
1023
1073
10123
10173
10223
Dyna
mic
Visc
osity
(Pas
)
100
50
0
50
100
150
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
104
Satu
ratio
n Pr
essu
re (P
a)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PHE
Description: Paratherm HESource: Thermal Properties Calculator v6.4. Paratherm Ltd., 2013. URL: http://pa...
Temperature: 0.0 °C to 330.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 80 160 240 320Temperature (°C)
700
750
800
850
Dens
ity (k
g/m
3 )
0.06
0.04
0.02
0.00
0.02
0.04
0.06
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
1800
2000
2200
2400
2600
2800
3000
Heat
Cap
acity
(J/k
g/K)
2
1
0
1
2
3
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
0.110
0.115
0.120
0.125
0.130
0.135
Ther
mal
Con
duct
ivity
(W/m
/K)
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
10 127
10 77
10 27
1023
1073
10123
10173
10223
Dyna
mic
Visc
osity
(Pas
)
100
50
0
50
100
150
200
250
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
104
3 × 103
4 × 103
6 × 103
Satu
ratio
n Pr
essu
re (P
a)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PHR
Description: Paratherm HRSource: Thermal Properties Calculator v6.4. Paratherm Ltd., 2013. URL: http://pa...
Temperature: -15.0 °C to 370.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 100 200 300Temperature (°C)
700
750
800
850
900
950
1000
Dens
ity (k
g/m
3 )
0.06
0.04
0.02
0.00
0.02
0.04
0.06
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
2000
2200
2400
2600
Heat
Cap
acity
(J/k
g/K)
2
1
0
1
2
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
0.0850.0900.0950.1000.1050.1100.1150.120
Ther
mal
Con
duct
ivity
(W/m
/K)
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
100
101
2 × 100
3 × 100
4 × 100
6 × 100
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
0 100 200 300Temperature (°C)
104
105
Satu
ratio
n Pr
essu
re (P
a)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PK2
Description: Pekasol 2000, K acetate/formateSource: Technical Data Sheet. pro Kühlsole GmbH, 2005.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -62.0 °C to 100.0 °CComposition: 30.0 % to 100.0 %, volume
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 0 40 80Temperature (°C)
1050
1100
1150
1200
1250
1300
Dens
ity (k
g/m
3 )
showing x=0.70
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
2400
2600
2800
3000
3200
3400
3600
Heat
Cap
acity
(J/k
g/K)
showing x=0.70
0.2
0.1
0.0
0.1
0.2
rel.
Erro
r (%
)40 0 40 80
Temperature (°C)
0.40
0.45
0.50
0.55
0.60
0.65
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.70
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.70
0.50
0.25
0.00
0.25
0.50
0.75
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.4 0.6 0.8 1.0Volume fraction
210
220
230
240
250
260
Free
zing
Tem
pera
ture
(K)
0.2
0.1
0.0
0.1
rel.
Erro
r (%
)
Fitting Report for PKL
Description: Pekasol L, Propylene GlycolSource: Technical Data Sheet. pro Kühlsole GmbH, 2005.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -49.0 °C to 100.0 °CComposition: 10.0 % to 60.0 %, volume
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 0 40 80Temperature (°C)
980
1000
1020
1040
1060
1080
1100
Dens
ity (k
g/m
3 )
showing x=0.40
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
3200
3400
3600
3800
4000
4200
4400
Heat
Cap
acity
(J/k
g/K)
showing x=0.40
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)40 0 40 80
Temperature (°C)
0.35
0.40
0.45
0.50
0.55
0.60
0.65
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.40
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
10 3
10 2
10 1
100
Dyna
mic
Visc
osity
(Pas
)
showing x=0.40
0.6
0.4
0.2
0.0
0.2
0.4
0.6
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.15 0.30 0.45 0.60Volume fraction
230
240
250
260
270
Free
zing
Tem
pera
ture
(K)
0.2
0.1
0.0
0.1
0.2
rel.
Erro
r (%
)
Fitting Report for PLR
Description: Paratherm LRSource: Thermal Properties Calculator v6.4. Paratherm Ltd., 2013. URL: http://pa...
Temperature: -84.99999999999997 °C to 230.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
80 0 80 160 240Temperature (°C)
600
650
700
750
800
850
Dens
ity (k
g/m
3 )
0.06
0.04
0.02
0.00
0.02
0.04
0.06
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
1600
1800
2000
2200
2400
2600
2800
Heat
Cap
acity
(J/k
g/K)
3
2
1
0
1
2
3
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
0.135
0.140
0.145
0.150
0.155
0.160
Ther
mal
Con
duct
ivity
(W/m
/K)
0.3
0.2
0.1
0.0
0.1
0.2
0.3
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
100
101
2 × 100
3 × 100
4 × 100
6 × 100
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
104
105
Satu
ratio
n Pr
essu
re (P
a)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PMR
Description: Paratherm MRSource: Thermal Properties Calculator v6.4. Paratherm Ltd., 2013. URL: http://pa...
Temperature: -39.99999999999997 °C to 315.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 80 160 240 320Temperature (°C)
700
750
800
850
Dens
ity (k
g/m
3 )
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
2200
2400
2600
2800
3000
Heat
Cap
acity
(J/k
g/K)
2
1
0
1
2
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
0.105
0.110
0.115
0.120
0.125
0.130
0.135
Ther
mal
Con
duct
ivity
(W/m
/K)
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
100
101
2 × 100
3 × 100
4 × 100
6 × 100
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
104
Satu
ratio
n Pr
essu
re (P
a)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PMS1
Description: Polydimethylsiloxan 1 - Baysilone KT3Source: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -80.0 °C to 100.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: coefficients to exppolynomial (3, 1)
Psat: no informationTfreeze: no information
Legend: function bounds
80 40 0 40 80Temperature (°C)
850
875
900
925
950
975
1000
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
1500
1550
1600
1650
1700
1750
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40 80
Temperature (°C)
0.10
0.11
0.12
0.13
0.14
0.15
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PMS2
Description: Polydimethylsiloxan 2 - Syltherm XLTSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -80.0 °C to 100.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: coefficients to exppolynomial (3, 1)
Psat: no informationTfreeze: no information
Legend: function bounds
80 40 0 40 80Temperature (°C)
800
850
900
950
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
1600
1700
1800
1900
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40 80
Temperature (°C)
0.10
0.11
0.12
0.13
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PNF
Description: Paratherm NFSource: Thermal Properties Calculator v6.4. Paratherm Ltd., 2013. URL: http://pa...
Temperature: -10.0 °C to 315.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 80 160 240 320Temperature (°C)
700
750
800
850
900
Dens
ity (k
g/m
3 )
0.06
0.04
0.02
0.00
0.02
0.04
0.06
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
1750
2000
2250
2500
2750
3000
3250
Heat
Cap
acity
(J/k
g/K)
2
1
0
1
2
3
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
0.0900
0.0925
0.0950
0.0975
0.1000
0.1025
0.1050
0.1075
Ther
mal
Con
duct
ivity
(W/m
/K)
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
100
101
2 × 100
3 × 100
4 × 100
6 × 100
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
104
3 × 103
4 × 103
6 × 103
Satu
ratio
n Pr
essu
re (P
a)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for PNF2
Description: Paratherm NF, Hydrotreated mineral oilSource: Thermal Properties Calculator v6.4. Paratherm Ltd., 2013. URL: http://pa...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -10.0 °C to 320.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
0 80 160 240 320Temperature (°C)
700
750
800
850
900
Dens
ity (k
g/m
3 )
0.06
0.04
0.02
0.00
0.02
0.04
0.06
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
1750
2000
2250
2500
2750
3000
3250
Heat
Cap
acity
(J/k
g/K)
0.2
0.1
0.0
0.1
0.2
rel.
Erro
r (%
)0 80 160 240 320
Temperature (°C)
0.0900
0.0925
0.0950
0.0975
0.1000
0.1025
0.1050
0.1075
Ther
mal
Con
duct
ivity
(W/m
/K)
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
10 4
10 3
10 2
10 1
100
101
102
103
Dyna
mic
Visc
osity
(Pas
)
100
50
0
50
100
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for S800
Description: Syltherm 800Source: Dow Chemical Company - FLUIDFILE Software accessed May 2017
Temperature: -40.0 °C to 398.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 100 200 300 400Temperature (°C)
600
700
800
900
1000
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
1600
1800
2000
2200
Heat
Cap
acity
(J/k
g/K)
0.3
0.2
0.1
0.0
0.1
0.2
0.3
rel.
Erro
r (%
)0 100 200 300 400
Temperature (°C)
0.06
0.08
0.10
0.12
0.14
Ther
mal
Con
duct
ivity
(W/m
/K)
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
10 96
10 81
10 66
10 51
10 36
10 21
10 6
109
Dyna
mic
Visc
osity
(Pas
)
100
50
0
50
100
150
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
10 123
10 74
10 25
1024
1073
10122
10171
10220
Satu
ratio
n Pr
essu
re (P
a)
0.0
0.2
0.4
0.6
0.8
rel.
Erro
r (%
)
1e10
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for SAB
Description: Synthetic alkyl benzene - Marlotherm XSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -80.0 °C to 100.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: coefficients to exppolynomial (3, 1)
Psat: no informationTfreeze: no information
Legend: function bounds
80 40 0 40 80Temperature (°C)
800820840860880900920940
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
1650
1700
1750
1800
1850
1900
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40 80
Temperature (°C)
0.11
0.12
0.13
0.14
0.15
0.16
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for T66
Description: Therminol66Source: Therminol Heat Transfer Reference Disk v5.1. Eastman Chemical Company, 2...
Temperature: 0.0 °C to 380.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exponential (3,)Tfreeze: no information
Legend: data function bounds error
0 100 200 300 400Temperature (°C)
750
800
850
900
950
1000
Dens
ity (k
g/m
3 )
0.06
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
1600
1800
2000
2200
2400
2600
2800
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)0 100 200 300 400
Temperature (°C)
0.085
0.090
0.095
0.100
0.105
0.110
0.115
0.120
Ther
mal
Con
duct
ivity
(W/m
/K)
0.6
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
10 100
10 85
10 70
10 55
10 40
10 25
10 10
105
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
101
102
103
104
105
Satu
ratio
n Pr
essu
re (P
a)
2
0
2
4
6
8
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for T72
Description: Therminol72Source: Therminol Heat Transfer Reference Disk v5.1. Eastman Chemical Company, 2...
Temperature: -10.0 °C to 380.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 100 200 300 400Temperature (°C)
750800850900950
100010501100
Dens
ity (k
g/m
3 )
0.05
0.00
0.05
0.10
0.15
0.20
0.25
0.30
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
1600
1800
2000
2200
2400
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)0 100 200 300 400
Temperature (°C)
0.10
0.11
0.12
0.13
0.14
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
10 99
10 83
10 67
10 51
10 35
10 19
10 3
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
10 99
10 83
10 67
10 51
10 35
10 19
10 3
Satu
ratio
n Pr
essu
re (P
a)
0
1
2
3
4
rel.
Erro
r (%
)
1e9
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for TCO
Description: Citrus oil terpene - d-LimoneneSource: Åke Melinder. Properties of Secondary Working Fluids for Indirect System...
Temperature: -80.0 °C to 100.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: coefficients to exppolynomial (3, 1)
Psat: no informationTfreeze: no information
Legend: function bounds
80 40 0 40 80Temperature (°C)
780800820840860880900920
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
1200
1400
1600
1800
2000
2200
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 40 0 40 80
Temperature (°C)
0.105
0.110
0.115
0.120
0.125
0.130
0.135
0.140
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 40 0 40 80Temperature (°C)
10 3
2 × 10 3
3 × 10 3
4 × 10 3
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for TD12
Description: TherminolD12Source: Therminol Heat Transfer Reference Disk v5.1. Eastman Chemical Company, 2...
Temperature: -85.0 °C to 230.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: data to exponential (3,)Tfreeze: no information
Legend: data function bounds error
80 0 80 160 240Temperature (°C)
600
650
700
750
800
Dens
ity (k
g/m
3 )
0.15
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
1800
2000
2200
2400
2600
2800
3000
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
0.06
0.08
rel.
Erro
r (%
)80 0 80 160 240
Temperature (°C)
0.07
0.08
0.09
0.10
0.11
0.12
Ther
mal
Con
duct
ivity
(W/m
/K)
0.06
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
10 64
10 33
10 2
1029
1060
1091
10122
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
10 4
10 2
100
102
104
Satu
ratio
n Pr
essu
re (P
a)
0.6
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for TVP1
Description: TherminolVP1Source: Therminol Heat Transfer Reference Disk v5.1. Eastman Chemical Company, 2...
Temperature: 12.0 °C to 397.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: data to exponential (3,)Tfreeze: no information
Legend: data function bounds error
0 100 200 300 400Temperature (°C)
700
800
900
1000
Dens
ity (k
g/m
3 )
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
1600
1800
2000
2200
2400
2600
Heat
Cap
acity
(J/k
g/K)
0.2
0.1
0.0
0.1
0.2
0.3
0.4
rel.
Erro
r (%
)0 100 200 300 400
Temperature (°C)
0.08
0.09
0.10
0.11
0.12
0.13
0.14
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
10 3
Dyna
mic
Visc
osity
(Pas
)
2
0
2
4
6
8
rel.
Erro
r (%
)
0 100 200 300 400Temperature (°C)
100
101
102
103
104
105
106
Satu
ratio
n Pr
essu
re (P
a)
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for TVP1869
Description: Thermogen VP 1869Source: Technical Information. Hoechst AG, 1995.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -80.0 °C to 20.0 °CComposition: pure fluid
Density: coefficients to polynomial (2, 1)Spec. Heat: coefficients to polynomial (2, 1)
Th. Cond.: coefficients to polynomial (2, 1)Viscosity: equation to exppolynomial (4, 1)
Psat: no informationTfreeze: no information
Legend: function bounds data error
75 50 25 0 25Temperature (°C)
920
940
960
980
1000
1020
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
75 50 25 0 25Temperature (°C)
2000
2100
2200
2300
2400
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)75 50 25 0 25
Temperature (°C)
0.1475
0.1500
0.1525
0.1550
0.1575
0.1600
0.1625
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
75 50 25 0 25Temperature (°C)
10 2
10 1
100
Dyna
mic
Visc
osity
(Pas
)
2
0
2
4
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for TX22
Description: Texatherm22Source: Technical Data Sheet. Chevron Products Company, 2004.
Temperature: 0.0 °C to 350.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: data to exppolynomial (3,)Tfreeze: no information
Legend: data function bounds error
0 80 160 240 320Temperature (°C)
650
700
750
800
850
Dens
ity (k
g/m
3 )
0.125
0.100
0.075
0.050
0.025
0.000
0.025
0.050
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
1800
2000
2200
2400
2600
2800
3000
Heat
Cap
acity
(J/k
g/K)
0.2
0.1
0.0
0.1
rel.
Erro
r (%
)0 80 160 240 320
Temperature (°C)
0.110
0.115
0.120
0.125
0.130
0.135
Ther
mal
Con
duct
ivity
(W/m
/K)
0.3
0.2
0.1
0.0
0.1
rel.
Erro
r (%
)
0 50 100 150 200Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
0.3
0.2
0.1
0.0
rel.
Erro
r (%
)
0 80 160 240 320Temperature (°C)
100
108
1016
1024
1032
1040
1048
1056
Satu
ratio
n Pr
essu
re (P
a)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for TY10
Description: Tyfoxit 1.10, Potassium AcetateSource: Technical Information. Tyforop Chemie Gmbh, 1999.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -10.0 °C to 40.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
0 15 30Temperature (°C)
1095
1100
1105
1110
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 15 30Temperature (°C)
3480
3500
3520
3540
3560
3580
Heat
Cap
acity
(J/k
g/K)
0.06
0.04
0.02
0.00
0.02
0.04
0.06
rel.
Erro
r (%
)0 15 30Temperature (°C)
0.5100.5150.5200.5250.5300.5350.5400.545
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 15 30Temperature (°C)
2 × 10 3
3 × 10 3
4 × 10 3
Dyna
mic
Visc
osity
(Pas
)
3
2
1
0
1
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for TY15
Description: Tyfoxit 1.15, Potassium AcetateSource: Technical Information. Tyforop Chemie Gmbh, 1999.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -20.0 °C to 40.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
15 0 15 30Temperature (°C)
1145
1150
1155
1160
1165
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
15 0 15 30Temperature (°C)
3220
3240
3260
3280
3300
3320
3340
Heat
Cap
acity
(J/k
g/K)
0.1000.0750.0500.025
0.0000.0250.0500.075
rel.
Erro
r (%
)15 0 15 30
Temperature (°C)
0.47
0.48
0.49
0.50
0.51
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
15 0 15 30Temperature (°C)
10 2
2 × 10 3
3 × 10 3
4 × 10 3
6 × 10 3
Dyna
mic
Visc
osity
(Pas
)
3
2
1
0
1
2
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for TY20
Description: Tyfoxit 1.20, Potassium AcetateSource: Technical Information. Tyforop Chemie Gmbh, 1999.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -40.0 °C to 40.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
40 20 0 20 40Temperature (°C)
1195
1200
1205
1210
1215
1220
1225
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
29502975300030253050307531003125
Heat
Cap
acity
(J/k
g/K)
0.15
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)40 20 0 20 40
Temperature (°C)
0.43
0.44
0.45
0.46
0.47
0.48
Ther
mal
Con
duct
ivity
(W/m
/K)
0.075
0.050
0.025
0.000
0.025
0.050
0.075
rel.
Erro
r (%
)
40 20 0 20 40Temperature (°C)
10 2
Dyna
mic
Visc
osity
(Pas
)
4
2
0
2
4
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for TY24
Description: Tyfoxit 1.24, Potassium AcetateSource: Technical Information. Tyforop Chemie Gmbh, 1999.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -55.0 °C to 40.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
50 25 0 25Temperature (°C)
1230
1240
1250
1260
1270
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
50 25 0 25Temperature (°C)
2750
2800
2850
2900
2950
3000
Heat
Cap
acity
(J/k
g/K)
0.100.05
0.000.050.100.150.20
rel.
Erro
r (%
)50 25 0 25
Temperature (°C)
0.40
0.41
0.42
0.43
0.44
0.45
Ther
mal
Con
duct
ivity
(W/m
/K)
0.10
0.05
0.00
0.05
rel.
Erro
r (%
)
50 25 0 25Temperature (°C)
10 113
10 73
10 33
107
1047
1087
10127
10167
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for VCA
Description: VDI, Calcium ClorideSource: Ewald Preisegger, Felix Flohr, Gernot Krakat, Andreas Glück, and Dietmar...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -55.0 °C to 20.0 °CComposition: 14.7 % to 29.9 %, mass
Density: data to polynomial (4, 5)Spec. Heat: data to polynomial (4, 5)
Th. Cond.: data to polynomial (4, 5)Viscosity: data to exppolynomial (4, 5)
Psat: no informationTfreeze: data to exppolynomial (1, 5)
Legend: data function bounds error
40 20 0 20Temperature (°C)
1150
1200
1250
1300
Dens
ity (k
g/m
3 )
showing x=0.26
0.15
0.10
0.05
0.00
0.05
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
2600
2800
3000
3200
3400
Heat
Cap
acity
(J/k
g/K)
showing x=0.26
0.4
0.2
0.0
0.2
rel.
Erro
r (%
)40 20 0 20
Temperature (°C)
0.46
0.48
0.50
0.52
0.54
0.56
0.58
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.26
0.10
0.05
0.00
0.05
rel.
Erro
r (%
)
40 20 0 20Temperature (°C)
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.26
4
2
0
2
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.16 0.20 0.24 0.28Mass fraction
220
230
240
250
260
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for VKC
Description: VDI, Potassium CarbonateSource: Ewald Preisegger, Felix Flohr, Gernot Krakat, Andreas Glück, and Dietmar...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -35.0 °C to 20.0 °CComposition: 12.8 % to 38.9 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
30 15 0 15Temperature (°C)
1150
1200
1250
1300
1350
1400
Dens
ity (k
g/m
3 )
showing x=0.34
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 15 0 15Temperature (°C)
2600
2800
3000
3200
3400
Heat
Cap
acity
(J/k
g/K)
showing x=0.34
0.05
0.00
0.05
0.10
0.15
rel.
Erro
r (%
)30 15 0 15
Temperature (°C)
0.46
0.48
0.50
0.52
0.54
0.56
0.58
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.34
0.15
0.10
0.05
0.00
0.05
rel.
Erro
r (%
)
30 15 0 15Temperature (°C)
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.34
0.8
0.6
0.4
0.2
0.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.12 0.18 0.24 0.30 0.36Mass fraction
240
245
250
255
260
265
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for VMA
Description: VDI, MethanolSource: Ewald Preisegger, Felix Flohr, Gernot Krakat, Andreas Glück, and Dietmar...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -80.0 °C to 0.0 °CComposition: 10.0 % to 90.0 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
80 60 40 20 0Temperature (°C)
825850875900925950975
Dens
ity (k
g/m
3 )
showing x=0.50
0.05
0.00
0.05
0.10
0.15
rel.
Erro
r (%
)
80 60 40 20 0Temperature (°C)
2500
3000
3500
4000
Heat
Cap
acity
(J/k
g/K)
showing x=0.50
0.100
0.075
0.050
0.025
0.000
0.025
0.050
0.075
rel.
Erro
r (%
)80 60 40 20 0
Temperature (°C)
0.25
0.30
0.35
0.40
0.45
0.50
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.50
0.050.000.050.100.150.200.250.30
rel.
Erro
r (%
)
80 60 40 20 0Temperature (°C)
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.50
0.0
2.5
5.0
7.5
10.0
12.5
15.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.2 0.4 0.6 0.8Mass fraction
180
200
220
240
260
Free
zing
Tem
pera
ture
(K)
1.0
0.5
0.0
0.5
rel.
Erro
r (%
)
Fitting Report for VMG
Description: VDI, Magnesium ChlorideSource: Ewald Preisegger, Felix Flohr, Gernot Krakat, Andreas Glück, and Dietmar...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -33.0 °C to 20.0 °CComposition: 7.200000000000001 % to 20.6 %, mass
Density: data to polynomial (4, 5)Spec. Heat: data to polynomial (4, 5)
Th. Cond.: data to polynomial (4, 5)Viscosity: data to exppolynomial (4, 5)
Psat: no informationTfreeze: data to exppolynomial (1, 5)
Legend: data function bounds error
30 15 0 15Temperature (°C)
1060
1080
1100
1120
1140
1160
1180
1200
Dens
ity (k
g/m
3 )
showing x=0.14
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 15 0 15Temperature (°C)
3000
3200
3400
3600
3800
Heat
Cap
acity
(J/k
g/K)
showing x=0.14
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)30 15 0 15
Temperature (°C)
0.46
0.48
0.50
0.52
0.54
0.56
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.14
0.1
0.0
0.1
0.2
rel.
Erro
r (%
)
30 15 0 15Temperature (°C)
10 2
Dyna
mic
Visc
osity
(Pas
)
showing x=0.14
0.75
0.50
0.25
0.00
0.25
0.50
0.75
1.00
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.09 0.12 0.15 0.18 0.21Mass fraction
240
245
250
255
260
265
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for VNA
Description: VDI, Sodium ChlorideSource: Ewald Preisegger, Felix Flohr, Gernot Krakat, Andreas Glück, and Dietmar...
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -21.0 °C to 20.0 °CComposition: 7.000000000000001 % to 23.1 %, mass
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
20 10 0 10 20Temperature (°C)
1060108011001120114011601180
Dens
ity (k
g/m
3 )
showing x=0.19
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
20 10 0 10 20Temperature (°C)
3300
3400
3500
3600
3700
3800
Heat
Cap
acity
(J/k
g/K)
showing x=0.19
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)20 10 0 10 20
Temperature (°C)
0.52
0.54
0.56
0.58
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.19
0.0
0.1
0.2
0.3
rel.
Erro
r (%
)
20 10 0 10 20Temperature (°C)
10 3
2 × 10 3
3 × 10 3
4 × 10 3
6 × 10 3
Dyna
mic
Visc
osity
(Pas
)
showing x=0.19
2.52.01.51.00.5
0.00.51.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.08 0.12 0.16 0.20Mass fraction
252.5
255.0
257.5
260.0
262.5
265.0
267.5
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for Water
Description: Fit of EOS from 1 bar to 100 barSource: W. Wagner and A. Pruß. The IAPWS Formulation 1995 for the Thermodynamic ...
M.L. Huber, R.A. Perkins, A. Laesecke, D.G. Friend, J.V. Sengers, M.J As...Temperature: 0.0 °C to 200.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: data to exponential (3,)Tfreeze: no information
Legend: data function bounds error
0 50 100 150 200Temperature (°C)
880
900
920
940
960
980
1000
Dens
ity (k
g/m
3 )
0.100
0.075
0.050
0.025
0.000
0.025
0.050
rel.
Erro
r (%
)
0 50 100 150 200Temperature (°C)
4200
4250
4300
4350
4400
4450
Heat
Cap
acity
(J/k
g/K)
0.1
0.0
0.1
0.2
0.3
rel.
Erro
r (%
)0 50 100 150 200
Temperature (°C)
0.56
0.58
0.60
0.62
0.64
0.66
0.68
Ther
mal
Con
duct
ivity
(W/m
/K)
0.4
0.3
0.2
0.1
0.0
0.1
rel.
Erro
r (%
)
0 50 100 150 200Temperature (°C)
10 3
Dyna
mic
Visc
osity
(Pas
)
0.5
0.0
0.5
1.0
rel.
Erro
r (%
)
0 50 100 150 200Temperature (°C)
103
104
105
106
Satu
ratio
n Pr
essu
re (P
a)
0.3
0.2
0.1
0.0
0.1
0.2
0.3
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for XLT
Description: SylthermXLTSource: Technical Data Sheet. The Dow Chemical Company, 1997.
Temperature: -100.0 °C to 260.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
80 0 80 160 240Temperature (°C)
600
700
800
900
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
1600
1800
2000
2200
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 0 80 160 240
Temperature (°C)
0.06
0.08
0.10
0.12
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
10 99
10 83
10 67
10 51
10 35
10 19
10 3
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
20
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for XLT2
Description: Syltherm XLT, PolydimethylsiloxanSource: Technical Data Sheet. The Dow Chemical Company, 1997.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -100.0 °C to 260.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
80 0 80 160 240Temperature (°C)
600
700
800
900
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
1600
1800
2000
2200
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)80 0 80 160 240
Temperature (°C)
0.06
0.08
0.10
0.12
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
80 0 80 160 240Temperature (°C)
102
1012
1022
1032
1042
1052
1062
Dyna
mic
Visc
osity
(Pas
)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for ZAC
Description: Zitrec AC, Corrosion InhibitorSource: Technical Information. Arteco NV/SA, 2010.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: 0.0 °C to 100.0 °CComposition: 6.0 % to 50.0 %, volume
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
0 25 50 75 100Temperature (°C)
960
980
1000
1020
1040
Dens
ity (k
g/m
3 )
showing x=0.20
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
0 25 50 75 100Temperature (°C)
4050
4075
4100
4125
4150
4175
4200
Heat
Cap
acity
(J/k
g/K)
showing x=0.20
0.15
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)0 25 50 75 100
Temperature (°C)
0.500
0.525
0.550
0.575
0.600
0.625
0.650
0.675
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.20
0.05
0.00
0.05
0.10
0.15
0.20
rel.
Erro
r (%
)
0 25 50 75 100Temperature (°C)
10 3
Dyna
mic
Visc
osity
(Pas
)
showing x=0.20
3
2
1
0
1
2
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.1 0.2 0.3 0.4 0.5Volume fraction
269
270
271
272
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for ZFC
Description: Zitrec FC, Propylene GlycolSource: Technical Information. Arteco NV/SA, 2010.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -40.0 °C to 100.0 °CComposition: 30.0 % to 60.0 %, volume
Density: data to polynomial (4, 4)Spec. Heat: data to polynomial (4, 4)
Th. Cond.: data to polynomial (4, 4)Viscosity: data to exppolynomial (4, 4)
Psat: no informationTfreeze: data to exppolynomial (1, 4)
Legend: data function bounds error
40 0 40 80Temperature (°C)
980
1000
1020
1040
1060
Dens
ity (k
g/m
3 )
showing x=0.50
0.20
0.15
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
3200
3400
3600
3800
4000
Heat
Cap
acity
(J/k
g/K)
showing x=0.50
0.4
0.3
0.2
0.1
0.0
0.1
0.2
rel.
Erro
r (%
)40 0 40 80
Temperature (°C)
0.3250.3500.3750.4000.4250.4500.4750.500
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.50
0.2
0.1
0.0
0.1
0.2
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
10 3
10 2
10 1
100
Dyna
mic
Visc
osity
(Pas
)
showing x=0.50
7.5
5.0
2.5
0.0
2.5
5.0
7.5
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.32 0.40 0.48 0.56Volume fraction
220
230
240
250
260
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for ZLC
Description: Zitrec LC, Propylene GlycolSource: Technical Information. Arteco NV/SA, 2010.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -50.0 °C to 100.0 °CComposition: 30.0 % to 70.0 %, volume
Density: data to polynomial (4, 5)Spec. Heat: data to polynomial (4, 5)
Th. Cond.: data to polynomial (4, 5)Viscosity: data to exppolynomial (4, 5)
Psat: no informationTfreeze: data to exppolynomial (1, 5)
Legend: data function bounds error
40 0 40 80Temperature (°C)
980
1000
1020
1040
1060
1080
1100
Dens
ity (k
g/m
3 )
showing x=0.50
0.5
0.4
0.3
0.2
0.1
0.0
0.1
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
2800
3000
3200
3400
3600
3800
4000
Heat
Cap
acity
(J/k
g/K)
showing x=0.50
0.3
0.2
0.1
0.0
0.1
0.2
rel.
Erro
r (%
)40 0 40 80
Temperature (°C)
0.30
0.35
0.40
0.45
0.50
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.50
0.10
0.05
0.00
0.05
0.10
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
10 3
10 2
10 1
100
101
102
Dyna
mic
Visc
osity
(Pas
)
showing x=0.50
10
5
0
5
10
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.3 0.4 0.5 0.6 0.7Volume fraction
200
210
220
230
240
250
260
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for ZM
Description: Zitrec M, Ethylene GlycolSource: Technical Information. Arteco NV/SA, 2010.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -50.0 °C to 120.0 °CComposition: 0.0 % to 100.0 %, volume
Density: data to polynomial (4, 6)Spec. Heat: data to polynomial (4, 6)
Th. Cond.: data to polynomial (4, 6)Viscosity: data to exppolynomial (4, 6)
Psat: no informationTfreeze: data to exppolynomial (1, 6)
Legend: data function bounds error
40 0 40 80 120Temperature (°C)
950
1000
1050
1100
1150
Dens
ity (k
g/m
3 )
showing x=0.60
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 0 40 80 120Temperature (°C)
2000
2500
3000
3500
4000
Heat
Cap
acity
(J/k
g/K)
showing x=0.60
0.0
0.2
0.4
0.6
rel.
Erro
r (%
)
40 0 40 80 120Temperature (°C)
0.2
0.3
0.4
0.5
0.6
0.7
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.60
1.2
1.0
0.8
0.6
0.4
0.2
0.0
rel.
Erro
r (%
)
40 0 40 80 120Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.60
642
02468
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.00 0.25 0.50 0.75 1.00Volume fraction
160
180
200
220
240
260
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for ZMC
Description: Zitrec MC, Ethylene GlycolSource: Technical Information. Arteco NV/SA, 2010.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -50.0 °C to 110.0 °CComposition: 30.0 % to 70.0 %, volume
Density: data to polynomial (4, 5)Spec. Heat: data to polynomial (4, 5)
Th. Cond.: data to polynomial (4, 5)Viscosity: data to exppolynomial (4, 5)
Psat: no informationTfreeze: data to exppolynomial (1, 5)
Legend: data function bounds error
40 0 40 80Temperature (°C)
1000
1025
1050
1075
1100
1125
Dens
ity (k
g/m
3 )
showing x=0.50
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
2500
2750
3000
3250
3500
3750
4000
Heat
Cap
acity
(J/k
g/K)
showing x=0.50
0.4
0.2
0.0
0.2
0.4
rel.
Erro
r (%
)40 0 40 80
Temperature (°C)
0.35
0.40
0.45
0.50
Ther
mal
Con
duct
ivity
(W/m
/K)
showing x=0.50
0.2
0.0
0.2
0.4
0.6
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
10 3
10 2
10 1
Dyna
mic
Visc
osity
(Pas
)
showing x=0.50
6
4
2
0
2
4
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.3 0.4 0.5 0.6 0.7Volume fraction
210
220
230
240
250
Free
zing
Tem
pera
ture
(K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
Fitting Report for ZS10
Description: Zitrec S10, Potassium formate/Sodium propionateSource: Technical Information. Arteco NV/SA, 2010.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -8.0 °C to 90.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
0 25 50 75Temperature (°C)
1060
1070
1080
1090
1100
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 25 50 75Temperature (°C)
3550
3575
3600
3625
3650
3675
3700
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)0 25 50 75
Temperature (°C)
0.50
0.52
0.54
0.56
0.58
0.60
0.62
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
0 25 50 75Temperature (°C)
10 3
Dyna
mic
Visc
osity
(Pas
)
1.5
1.0
0.5
0.0
0.5
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for ZS25
Description: Zitrec S25, Potassium formate/Sodium propionateSource: Technical Information. Arteco NV/SA, 2010.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -23.0 °C to 90.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
25 0 25 50 75Temperature (°C)
1150
1160
1170
1180
1190
1200
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 0 30 60 90Temperature (°C)
3180
3190
3200
3210
3220
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)30 0 30 60 90
Temperature (°C)
0.44
0.46
0.48
0.50
0.52
0.54
0.56
0.58
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
25 0 25 50 75Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
2.0
1.5
1.0
0.5
0.0
0.5
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for ZS40
Description: Zitrec S40, Potassium formate/Sodium propionateSource: Technical Information. Arteco NV/SA, 2010.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -38.0 °C to 90.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
30 0 30 60 90Temperature (°C)
12101220123012401250126012701280
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 0 30 60 90Temperature (°C)
2700
2750
2800
2850
2900
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)30 0 30 60 90
Temperature (°C)
0.42
0.44
0.46
0.48
0.50
0.52
0.54
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 0 30 60 90Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
4
2
0
2
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for ZS45
Description: Zitrec S45, Potassium formate/Sodium propionateSource: Technical Information. Arteco NV/SA, 2010.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -43.0 °C to 90.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exponential (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
30 0 30 60 90Temperature (°C)
1240
1260
1280
1300
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 0 30 60 90Temperature (°C)
2550
2600
2650
2700
2750
2800
2850
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)30 0 30 60 90
Temperature (°C)
0.40
0.42
0.44
0.46
0.48
0.50
0.52
0.54
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
30 0 30 60 90Temperature (°C)
10 3
10 2
Dyna
mic
Visc
osity
(Pas
)
6
4
2
0
2
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
Fitting Report for ZS55
Description: Zitrec S55, Potassium formate/Sodium propionateSource: Technical Information. Arteco NV/SA, 2010.
Morten Juel Skovrup. SecCool Properties v1.33. IPU Refrigeration and Ene...Temperature: -55.0 °C to 90.0 °CComposition: pure fluid
Density: data to polynomial (4, 1)Spec. Heat: data to polynomial (4, 1)
Th. Cond.: data to polynomial (4, 1)Viscosity: data to exppolynomial (3,)
Psat: no informationTfreeze: no information
Legend: data function bounds error
40 0 40 80Temperature (°C)
1280
1300
1320
1340
1360
Dens
ity (k
g/m
3 )
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
2450
2500
2550
2600
2650
2700
Heat
Cap
acity
(J/k
g/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)40 0 40 80
Temperature (°C)
0.40
0.42
0.44
0.46
0.48
0.50
0.52
Ther
mal
Con
duct
ivity
(W/m
/K)
0.04
0.02
0.00
0.02
0.04
rel.
Erro
r (%
)
40 0 40 80Temperature (°C)
100
101
2 × 100
3 × 100
4 × 100
6 × 100
Dyna
mic
Visc
osity
(Pas
)
100
80
60
40
20
0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Temperature (°C)
100
101
Satu
ratio
n Pr
essu
re (P
a)
No saturation state information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
0.0 0.2 0.4 0.6 0.8 1.0Fraction
0.0
0.2
0.4
0.6
0.8
1.0
Free
zing
Tem
pera
ture
(K)
No freezing point information
0.0
0.2
0.4
0.6
0.8
1.0
rel.
Erro
r (%
)
