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Define Mixture
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Data Comparision
API
2232118-M2 Thermodynamic & Transport Properties (Based on Mercury model)
Recommend:
2232118-M2 A BETTER Caculation Venus Model
CAS Number
Name
Category
Pure Or Mix Name
English Short Name
English Full Name
Chemical Formula
Molecular Weight
Synonym
Molecular Weight
g/mol
Triple Point Temperature
℃
K
°F
°R
Normal Boiling Point
℃
K
°F
°R
Critical Temperature
℃
K
°F
°R
Critical Pressure
MPa(absolute)
KPa(absolute)
Pa(absolute)
bar(absolute)
psi(absolute)
atm(absolute)
kg/cm2(absolute)
mmHg(Torr)(absolute)
inHg(absolute)
mmH2O(absolute)
inH2O(absolute)
ftH2O(absolute)
MPa(gauge)
KPa(gauge)
Pa(gauge)
bar(gauge)
psi(gauge)
atm(gauge)
kg/cm
2
(gauge)
mmHg(Torr)(gauge)
inHg(gauge)
mmH2O(gauge)
inH2O(gauge)
ftH2O(gauge)
Critical Density
kg/m
3
g/cm
3
lb/ft
3
lb/in
3
lb/gal
Critical Compress Factor
Acentric Factor
kJ/(kg·℃)
J/(kg·℃)
Btu/(lb°F)
Dipole Moment
Debye
Composition
Fraction:
Mole percentage:
propane
0.1%,
propylene
0.1%,
isobutane
35.4%,
n-butane
8.8%,
neopentane
0.1%,
trans-2-butene
18.9%,
1-butene
16%,
2-methylpropene
6%,
cis-2-butene
13.1%,
isopentane
0.5%,
1,3-butadiene
0.4%,
3-methyl-1-butene
0.4%,
n-pentane
0.1%,
cyclopentane
0.1%,
Mass percentage:propane 0.0771681176154982%, propylene 0.0736402552369143%, isobutane 36.007084404061%, n-butane 8.95091363716771%, neopentane 0.126260337759844%, trans-2-butene 18.5552715977414%, 1-butene 15.7081664319504%, 2-methylpropene 5.8905624119814%, cis-2-butene 12.8610612661594%, isopentane 0.631307813864115%, 1,3-butadiene 0.378634011722013%, 3-methyl-1-butene 0.490935501584373%, n-pentane 0.126260337759844%, cyclopentane 0.122733875396093%,
2232118-M2 :Introduction
Single Value
Table
Temperature =
℃
K
°F
°R
Acceptable Range:
< T <
Pressure =
MPa(absolute)
KPa(absolute)
Pa(absolute)
bar(absolute)
psi(absolute)/option>
atm(absolute)/option>
kg/cm2(absolute)
mmHg(Torr)(absolute)
inHg(absolute)
mmH2O(absolute)
inH2O(absolute)
ftH2O(absolute)
MPa(gauge)
KPa(gauge)
Pa(gauge)
bar(gauge)
psi(gauge)
atm(gauge)
kg/cm
2
(gauge)
mmHg(Torr)(gauge)
inHg(gauge)
mmH2O(gauge)
inH2O(gauge)
ftH2O(gauge)
< P <
Density =
kg/m
3
g/cm
3
lb/ft
3
lb/in
3
lb/gal
Specific Enthalpy =
kJ/kg
J/kg
Btu/lb
cal/g
Specific Entropy =
kJ/(kg·K)
J/(kg·K)
Btu/(lb°F)
cal/(g·K)
Reference
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2232118-M2 :Thermodynamic & Transport Properties Calculated Result
State:
Molecular Weight=
g/mol
Temperature=
℃
K
°F
°R
Pressure=
MPa(absolute)
KPa(absolute)
Pa(absolute)
bar(absolute)
psi(absolute)
atm(absolute)
kg/cm2(absolute)
mmHg(Torr)(absolute)
inHg(absolute)
mmH2O(absolute)
inH2O(absolute)
ftH2O(absolute)
MPa(gauge)
KPa(gauge)
Pa(gauge)
bar(gauge)
psi(gauge)
atm(gauge)
kg/cm
2
(gauge)
mmHg(Torr)(gauge)
inHg(gauge)
mmH2O(gauge)
inH2O(gauge)
ftH2O(gauge)
Density=
kg/m
3
g/cm
3
lb/ft
3
lb/in
3
lb/gal
Specific Votume=
m
3
/kg
cm
3
/g
ft
3
/lb
in
3
/lb
gal/lb
Specific Enthalpy=
kJ/kg
J/kg
Btu/lb
cal/g
Specific Entropy =
kJ/(kg·K)
J/(kg·K)
Btu/(lb°F)
cal/(g·K)
Internal energy=
kJ/kg
J/kg
Btu/lb
cal/g
Molar Volume Fraction=
Saturated Vapor Pressure, Boiling Point, the latent heat of vaporization is saturated. Only one parameter can be found.
Saturated Vapor Pressure=
MPa(absolute)
KPa(absolute)
Pa(absolute)
bar(absolute)
psi(absolute)
atm(absolute)
kg/cm2(absolute)
mmHg(Torr)(absolute)
inHg(absolute)
mmH2O(absolute)
inH2O(absolute)
ftH2O(absolute)
MPa(gauge)
KPa(gauge)
Pa(gauge)
bar(gauge)
psi(gauge)
atm(gauge)
kg/cm
2
(gauge)
mmHg(Torr)(gauge)
inHg(gauge)
mmH2O(gauge)
inH2O(gauge)
ftH2O(gauge)
Boiling Point=
℃
K
°F
°R
Latent Heat of Vaporization=
kJ/kg
J/kg
Btu/lb
cal/g
Specific Heat at Constant Pressure(Cp)=
kJ/(kg·K)
J/(kg·K)
Btu/(lb°F)
cal/(g·K)
Constant Volume Specific Heat(Cv)=
kJ/(kg·℃)
J/(kg·℃)
Btu/(lb°F)
cal/(g·K)
Cp/Cv=
Vapor Quality=
Compression Factor=
Helmholtz energy=
kJ/kg
J/kg
Btu/lb
cal/g
Gibbs Free Energy=
kJ/kg
J/kg
Btu/lb
cal/g
Fugacity=
MPa
KPa
Pa
bar
psi
atm
kg/cm2
mmHg(Torr)
inHg
mmH2O
inH2O
ftH2O
Fugacity coefficient=
Joule-Thomson Coefficient=
K/kPa
K/MPa
K/Pa
°C/bar
Sound Velocity=
m/s
ft/s
ft/min
km/h
mph
Second Virial coefficient=
m
3/kg
cm
3
/g
ft
3
/lb
in
3
/lb
gal/lb
Third virial coefficient=
(m
3
/kg)
2
(cm
3
/g)
2
(ft
3
/lb)
2
(in
3
/lb)
2
(gal/lb)
2
Thermal Conductivity=
W/(m·K)
kcal/(m·h·℃)
Btu/(ft·h·°F)
Thermal Diffusivity=
m2/s
ft2/s
Kinematic Viscosity =
m2/s
St
ft2/s
Dynamic Viscosity =
Pa·s
P
lbf·s/ft2
kgf·s/m2
Surface tension=
N/m
gf/cm
dyn/cm
erg/cm2
erg/mm2
lbf/in
Prandtl Number=
Relative Dielectric Constant
Lower limit
Upper limit
Temperature =
℃
Pressure =
MPa(a)
Density =
kg/m
3
Specific Enthalpy =
kJ/kg
Specific Entropy =
kJ/(kg·K)
Internal energy =
kJ/kg
Step:
1
2
3
4
5
6
7
8
9
10
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L:Saturated liquid,V:Saturated gas
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