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Prediction of the Potential Hydrocarbon Liquid Content of Lean Natural Gas Comparison with Field Tests

机译:与现场测试比较预测贫天然气的潜在碳氢化合物液体含量

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The objective of this study is to design a model which allows to predict at specified temperature and pressure the amount of liquid formed in pipelines transporting lean natural gas (potential hydrocarbon liquid content). The only input information that is used is an extensive gas chromatographic analysis of natural gas, which was recently developed by N. V. Nederlandse Gasunie. The availability of such a model is of great importance for the natural gas industry because the formation of liquid during storage, transport and processing needs to be anticipated. In order to achieve our objectives a two stage project has been proposed. At the first part, new highly accurate solubility data of heavy hydrocarbons in some of the main constituents of natural gas like methane and nitrogen have been measured. Also an attempt has been made to simulate the behaviour of real natural gas by performing solubility measurements of heavy hydrocarbons in mixtures of methane, nitrogen, carbon dioxide and ethane. Based on the information and experience gained at the first part, the next step was the modelling of real natural gas. For this purpose the Peng-Robinson equation of state was selected and applied with interaction parameters optimized at conditions of practical interest, i.e. at pressures 9 < p/bar < 67 and at temperatures 250 < T/K < 290. Prom a sensitivity analysis it could be concluded that the Potential Hydrocarbon Liquid Content (PHLC) is mainly influenced by the concentration and characterization of C_7-C_(12) fractions. In this work the PHLC deriving from two different characterization procedures to represent these fractions are compared with experimental PHLC of real natural gas measured by Gasunie.
机译:这项研究的目的是设计一个模型,该模型可以预测在指定的温度和压力下输送稀薄天然气的管道中形成的液体量(潜在的碳氢化合物液体含量)。唯一使用的输入信息是对天然气的广泛气相色谱分析,该分析最近由N. V. Nederlandse Gasunie开发。对于天然气行业而言,这种模型的可用性非常重要,因为需要预料到在存储,运输和加工过程中会形成液体。为了实现我们的目标,已经提出了一个分为两个阶段的项目。在第一部分中,已经测量了重碳氢化合物在天然气的一些主要成分(如甲烷和氮气)中的新的高精度溶解度数据。还尝试通过对甲烷,氮气,二氧化碳和乙烷的混合物中的重质烃进行溶解度测量来模拟真实天然气的行为。根据在第一部分中获得的信息和经验,下一步是对真实天然气进行建模。为此,选择了Peng-Robinson状态方程,并在实际感兴趣的条件下,即在压力9

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