ISSN:
1572-9567
Keywords:
characterization
;
equations of state
;
liquid dropout
;
natural gas
;
phase behavior
;
potential hydrocarbon liquid content
;
retrograde condensation
;
supercritical solubility
Source:
Springer Online Journal Archives 1860-2000
Topics:
Physics
Notes:
Abstract The occurrence of liquid dropout in natural gas pipelines may cause operational problems during storage, transport, and processing. Therefore, the availability of a model that accurately predicts the amount of liquid formed is of great importance for the natural gas industry. The objective of this study is to develop a thermodynamic model for the accurate prediction of the amount of liquid formed in natural gas pipelines at transportation conditions. As input, the model requires an accurate gas analysis. A modified Peng-Robinson equation of state was selected for the phase equilibrium calculations. Interaction parameters were optimized from experimental data at conditions of practical interest, i.e., at pressures 10 〈 p 〈 70 bar and at temperatures 250 〈 T 〈 290 K. For a number of “keysystems,” the interaction parameters were calculated from new accurate solubility data of heavy hydrocarbons in some of the main constituents of natural gas like methane and nitrogen. Also, an extensive experimental program was carried out to study the influence of minute amounts of nitrogen, ethane and carbon dioxide in methane on the solubility behavior of decane in these gas mixtures. From a sensitivity analysis, it could be concluded that the liquid dropout is influenced mainly by the concentration and characterization of C7-C13 fractions. In this work, two characterization procedures to represent these fractions are compared. For two types of lean natural gas, the model predictions are compared with field measurement data, recently supplied by the Dutch natural gas industry.
Type of Medium:
Electronic Resource
URL:
http://dx.doi.org/10.1007/BF01438848
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