Arab J Sci Eng (2014) 39:8341–8346
DOI 10.1007/s13369-014-1355-5
RESEARCH ARTICLE - PETROLEUM ENGINEERING
A New Correlation to Predict Dew Point Pressure
in Wet Gas Reservoirs
Ehsan Ghanaatpisheh · Hosein Vahdani ·
Kamal Bolandparvaz Jahromi
Received: 26 June 2013 / Accepted: 31 January 2014 / Published online: 13 September 2014
© King Fahd University of Petroleum and Minerals 2014
Abstract Correlations and equation of state (EOS) are two
important tools for dew point pressure calculation. Several
correlations introduced for gas condensate reservoirs, these
correlations have limited range of use, and they could not
be applied for wet gas reservoirs. Although EOS is more
general, but sometimes dew point pressure could not be cal-
culated from EOS (i.e., when limited range of components
are available). So a new correlation is needed to calculate
dew point pressure for wet gas reservoirs (47749 < GOR <
231708 scf/STB) when limited range of component (i.e., up
to C
7+
fraction) is available. A total of 114 samples from wet
gas fields of south west of Iran are used to generate a corre-
lation. The new correlation has an average relative deviation
(ARD) of -0.15 % and average absolute deviation (AAD) of
2.28 %. The accuracy of the correlation has been compared
with Soave–Redlich–Kwong and Peng–Robinson equations
of states and available correlations in the literature. In some
cases, it is not possible to calculate dew point pressure with
regard to equation of states; moreover, gas condensate corre-
lations available in literature are applicable for limited range
of data. As a result, it is shown that for this range of data,
the presented new correlation outperforms equations of state
and gas condensate correlations available in literature.
Keywords Correlation · Dew point pressure · Wet gas ·
Equation of state
E. Ghanaatpisheh (B ) · H. Vahdani · K. Bolandparvaz Jahromi
National Iran Oil Company (South Zagros Oil and Gas
Production Co.), Shiraz Fars, Islamic Republic of Iran
e-mail: ehsan.ghanaatpisheh@gmail.com
Abbreviations
a, b Constants for EOS
AAD Average absolute deviation
=
∑
(abs |( P
dc
- P
d
)/ P
d
|)/ N
ARD Average relative deviation
=
∑
(( P
dc
- P
d
)/ P
d
)/ N
¯
B Molal average boiling point
COC Coefficient of correlation
=
1 -
∑
( P
dc
- P
d
)
2
/
∑(
P
dc
- P
d
)
2
EOS Equation of state
f Fugacity
k Equilibrium ratio for the component
MW
C7+
Molecular weight of C
7+
P
d
Experimental dew point pressure (psia)
P
dc
Calculated dew point pressure (psia)
123