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DESCRIPTION
ThermoHidro
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EQUATIONS OF STATE Ideal Gas
(Only valid for gas at low pressure conditions)
RTPv =
Van der Waals
( ) RTbvvaPor
va
bvRTP =−⎟
⎠⎞
⎜⎝⎛ +−
−= 22
Relation with Z = compressibility factor:
RTva
bvb
RTPvZ −
−+== 1
c
c
c
c
PRTband
PTRa
86427 22
==
For mixtures:
∑∑ == iiii bxbandaxa
Van der Waals EOS, in term of Z:
( ) 01 23 =−++− ABAZZBZ
with ( )2RTaPAand
RTbPB ==
Redlich-Kwong
( )bvvTa
bvRTP . +
−−
= 50
Relation with Z = compressibility factor:
v/bv/b
RT/bTR/a
v/bRTPvZ
.
+⎟⎟⎠
⎞⎜⎜⎝
⎛−
−==
111 522
c
c
c
.c
PRT.band
PTR.a 0867042780 522
==
For mixtures:
∑∑ == iiii bxbandaxa
Redlich-Kwong EOS, in term of Z:
( ) 0223 =−−−+− ABZBBAZZ
with ( )2RTaPAand
RTbPB ==
Peng-Robinson
( )( ) ( )bvbbvv
Tabv
RTP−++
−−
=
Relation with Z = compressibility factor:
( )( ) ( )( )RTv/bbbv
Tav/bRT
PvZ−++
−−
==11
1
( ) ( )c
c
c
c
PRT.bandT
PTR.Ta 07780457240 22
== α
( ) ( ) ⎟⎟⎠
⎞⎜⎜⎝
⎛−−++=
cTT...T 12699205422613746401 2ωωα
For mixtures:
∑∑ == iiii bxbandaxa
Peng-Robinson EOS, in term of Z:
( ) ( ) ( ) 0231 32223 =−++−−+−+ ABBBZBBAZBZ
with ( )2RTaPAand
RTbPB ==
Benedict-Webb-Rubbin (BWR)
( ) ( )22
23632
2
1 dexpT
dcddadabRTdTCARTBRTdP o
oo γγα −+
++−+⎟⎠⎞
⎜⎝⎛ −−+=
Relation with Z = compressibility factor:
( )23
2252
21 dexp
RTdcdd
RTad
RTabd
RTC
RTAB
RTPvZ oo
o γγα−
+++⎟
⎠⎞
⎜⎝⎛ −+⎟
⎠⎞
⎜⎝⎛ −−==
where
vd 1= ; Bo, Ao, Co, b, a, c, α, γ are emphirical constants
for each substances.
For mixtures, use appropriate mixing rules such as:
( )[ ] ( )[ ]331331 ∑∑∑ === /ii
/iioiio xbxbBxB αα
Calculations of other properties from EOS