SPE Journal
Volume 15,
Number 4,
December 2010,
pp. 952-962
Summary
This paper presents a study of gas/condensate hydrocarbon mixtures and the
effect of water, methanol, and isopropanol on their phase behavior. Only sparse
data are available on the phase behavior of hydrocarbon/water/methanol mixtures
at the high temperatures typical of these reservoirs. Such data are needed for
compositional reservoir simulations of well treatments to optimize the
performance of solvent treatments of blocked wells. Constant-composition
expansion (CCE) experiments were performed to measure the phase behavior of
hydrocarbon/water/methanol mixtures up to 300°F. The effects of temperature,
pressure, and water and methanol concentration on the phase behavior were
measured. The Peng-Robinson equation of state (EOS) was used to model
hydrocarbon/water/methanol mixtures. The binary interaction parameters were
tuned to fit the data and were found to show a linear variation with
temperature. The binary interaction parameters and temperature-dependent
volume-shift parameters are the key parameters to model these complex polar
mixtures. Both the classical van der Waals and the Huron-Vidal (Huron and Vidal
1979) mixing rules were used and were found to give good agreement with the
data. Phase-behavior experiments performed on hydrocarbon/water/isopropanol
mixtures showed that isopropanol decreases the aqueous-phase volume fraction
and increases the liquid-hydrocarbon-phase volume fraction compared with the
analogous hydrocarbon/water/methanol mixtures. These data are needed to predict
the conditions under which methanol/isopropanol treatments can be applied
successfully in gas wells to remove water and condensate blockage.
© 2010. Society of Petroleum Engineers
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History
- Original manuscript received:
8 July 2006
- Meeting paper published:
25 September 2006
- Revised manuscript received:
20 May 2009
- Manuscript approved:
20 January 2010
- Published online:
22 June 2010
- Version of record:
2 December 2010