Membership Fee
|
Partner
|
Register
|
Login
|
[]
|
Exit
|
About us
Share:
Home
Water&Steam
Air
Refrigerant
Define Mixture
Moist Air
Pure Fluild
Data Comparision
API
12.2132.115 Thermodynamic & Transport Properties (Based on Mercury model)
Recommend:
12.2132.115 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:
1-butene
0.08%,
carbon dioxide
0.01%,
cis-2-butene
0.01%,
ethane
16.17%,
ethylene
16.34%,
n-hexane
0.1%,
hydrogen
12.95%,
isobutane
0.19%,
isopentane
0.02%,
methane
36.88%,
carbon monoxide
1.83%,
nitrogen
12.17%,
n-butane
0.03%,
oxygen
0.2%,
propane
0.52%,
propylene
2.48%,
trans-2-butene
0.02%,
Mass percentage:1-butene 0.21174600428076%, carbon dioxide 0.0207594121843883%, cis-2-butene 0.026468250535095%, ethane 22.9398926127346%, ethylene 21.6268734744119%, n-hexane 0.406579504176828%, hydrogen 1.3185104746503%, isobutane 0.521024350691036%, isopentane 0.0680802091758079%, methane 27.9141400457654%, carbon monoxide 2.41839131266143%, nitrogen 16.0849152258462%, n-butane 0.0822670027406899%, oxygen 0.30193621412548%, propane 1.08183486972117%, propylene 4.92364453522863%, trans-2-butene 0.0529365010701901%,
12.2132.115 :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
Please Login before calculating
Login
Or
Register
12.2132.115 :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
Please Login before calculating
Login
or
Register
L:Saturated liquid,V:Saturated gas
Comment
Read More ...
Post your comment after login/register.
Login
or
Register
Refrigerant
||
Enthalpy
||
Reference
Ethermo Thermodynamic & Transport Properties Caculation Platform
Copyright©2009 eThermo.us All Rights Reserved
View source
×