SPE Projects, Facilities & Construction
Volume 4, Number 4, December 2009, pp. 132-140

SPE-118133-PA

Compositional and PVT Analysis for Determining Liquid Dropout in Pipelines

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DOI  More information 10.2118/118133-PA http://dx.doi.org/10.2118/118133-PA

Citation

  • Esmaiel, T.E.H. and Al Qallaf, A.A.A. 2009. Compositional and PVT Analysis for Determining Liquid Dropout in Pipelines. SPE Proj Fac & Const  4 (4): 132-140. SPE-118133-PA. doi: 10.2118/118133-PA.

Discipline Categories

  • 4 Projects, Facilities and Construction
  • 4.1 Processing Systems and Design
  • 4.1.1 Process Simulation
  • 4.6 Flow Assurance
  • 5 Production and Operations

Summary

A lot of equipment is not designed to handle liquids in the operations of a gathering center or gas booster station. In the study area, some compressors were having vibration problems because of amounts of liquid condensate in the flowline caused by sudden changes in pressure and temperature.

The primary objectives of this study are to determine under what pressure and temperature conditions liquids occur and to determine the proper operating conditions. The process involves collecting samples in the field, laboratory analysis, computer equation of state (EOS) modeling of the fluids, and analysis of the phase regions.

Samples were collected at two different locations in the gas line. The samples were sent to the laboratory for compositional and PVT analysis, where physical properties were measured. Compositional analysis was performed on the gas and the condensate samples, and liquid dropout tests were performed on the samples.

An EOS simulator was used to characterize the samples and was tuned to match the pressure, volume, and temperature (PVT) data. The tuned simulator was used to perform flash calculations to calculate vapor liquid equilibrium (VLE) for the samples. The simulator was used to develop phase envelopes and physical properties of the gas to determine the amount of liquid dropout at the current operating conditions. These phase envelopes were used to determine new operating conditions to avoid liquid dropout. As anticipated, the primary solution was an increase in the pressure in the line to avoid the two-phase region.

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History

  • Original manuscript received: 2 September 2008
  • Meeting paper published: 3 November 2008
  • Revised manuscript received: 14 January 2009
  • Manuscript approved: 20 January 2009
  • Published online: 14 January 2010
  • Version of record: 14 January 2010