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ÇAĞRILI KONUŞMALAR / KEYNOTES Invited Speeches ... - TPJD

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Prediction of Temperature Change of Hydrocarbon Gases Using A Two-<br />

Parameter Z-Factor Correlation Under Isenthalpic Flash Conditions<br />

Cansu Uğur 1 , Şenol Yamanlar 2<br />

1 BVG Shipping and Trading Lmd, İstanbul<br />

2 İstanbul Technical Universİty, Faculty of Mines, Department of Petroleum and Natural Gas<br />

Engineering, İstanbul<br />

Isenthalpic expansion processes of real gases through restrictions are usually accompanied<br />

by a temperature change of the gas phase. This phenomena is known as the Joule-Thomson<br />

cooling (or heating). The temperature change depends on the initial and final pressures and<br />

initial temperature as well as the composition of the gas phase. Natural gases cool down at<br />

moderate pressures upon expansion in downhole perforations or in surface chokes whereas gas<br />

condensates may heat up when expanded at elevated reservoir pressures and temperatures.<br />

The direction and the magnitude of the temperature change may be predicted by using an<br />

isenthalpic flash calculation procedure. The constant enthalpy expansion of a real gas may result<br />

with condensation of a liquid phase due to the lowered gas temperature. In such processes,<br />

simultaneous solution of mass and enthalpy balance equations is required. If there is no<br />

liquid condensation after the expansion, the enthalpy balance equation should be solved for<br />

downstream temperature given up and downstream pressures and upstream temperature.<br />

An equation of state or a two-parameter z-factor correlation can be used to model the PVT<br />

behavior of the single phase natural gas in constant enthalpy flash calculations. Two-parameter z<br />

factor correlations are simpler to code and reduce computational time. However their accuracy<br />

in energetic computations is not well understood. In this paper, predictive capability of Abu<br />

Kassem-Dranchuk z-factor correlation is studied when used in calculating temperature changes<br />

during a constant enthalpy flash process. The results are compared to Peng-Robinson equation<br />

of state and to a leading reference thermodynamic fluid properties program results.<br />

Keywords: Natural gas, hydrocarbon, enthalpy, expansion, temperature change, z-factor,<br />

equation of state<br />

371

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