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Define Mixture
Moist Air
Pure Fluild
Data Comparision
API
ethene Thermodynamic & Transport Properties (Based on Venus model)
CAS number
Name
Category
Pure/Mixture
Short Name
Full Name
Chemical Formula
Synonym
R-1150 ,Ethylene;acetene;athylen
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
Mixture Component
Composition:
ethene : Introduction
Ethylene (IUPAC name: ethene) is a hydrocarbon which has the formula C2H4 or H2C=CH2. It is a colorless flammable gas with a faint "sweet and musky" odor when pure.[4] It is the simplest alkene (a hydrocarbon with carbon-carbon double bonds), and the second simplest unsaturated hydrocarbon after acetylene (C2H2).Ethylene is widely used in chemical industry, and its worldwide production (over 109 million tonnes in 2006) exceeds that of any other organic compound.Ethylene is also an important natural plant hormone, used in agriculture to force the ripening of fruits.Ethylene's hydrate is ethyl alcohol.
Single Value
Table
Temperature=
℃
K
°F
°R
Acceptable Range :
< T <
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)
< 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)
Internal Energy=
kJ/kg
J/kg
Btu/lb
cal/g
Reference
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ethene :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 Volume=
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
Composition=
Saturated Vapor Pressure, Boiling Point(dew point), Latent Heat of Vaporization are saturated properties, just enter One parameter to calculate them!
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 (Dew Point)=
℃
K
°F
°R
Vaporization Latent Heat=
kJ/kg
J/kg
Btu/lb
cal/g
Specific Heat(Cp)=
kJ/(kg·K)
J/(kg·K)
Btu/(lb°F)
cal/(g·K)
Specific Heat(Cv)=
kJ/(kg·℃)
J/(kg·℃)
Btu/(lb°F)
cal/(g·K)
Cp/Cv=
Vapor Quality=
Compressibility 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
Speed of Sound=
m/s
ft/s
ft/min
km/h
mph
2nd Virial Coefficient =
m
3/kg
cm
3
/g
ft
3
/lb
in
3
/lb
gal/lb
3rd 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
Enthalpy =
kJ/kg
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
Comment
sdebnath : How do I get saturated vapour pressure ?
(2023/7/13 17:53:38)
sdebnath : How to get both vapour and liquid data together
(2023/7/13 17:52:08)
Read More ...
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Reference
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