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引用次数: 0
摘要
天然气可压缩系数反映了天然气在不同条件下的压缩膨胀特性。这是一个热力学性质,用于考虑实际天然气的行为与理想气体的行为的偏差。天然气的压缩系数Z值在大多数油气工程计算中是必需的。在本研究中,采用了加拿大石油生产商协会、Azizi、Behbahani和Isazadeh、Dranchuk- Purvis- Robinson、Dranchuk- abu - kassem和Standing- Katz方法,比较了在不同条件(压力和温度)下确定同一天然气关键参数的五种不同计算方法。基于状态方程的相关性通常是隐式的,因为它们需要迭代。为了提高简单性,推导出了许多相关性;然而,对于整个伪还原压和温度范围,还没有建立相关关系。Azizi, Behbahani和Isazadeh的方法在T=20℃时得到的结果误差最大,p=20 bar不再适用。
THE INFLUENCE OF PRESSURE AND TEMPERATURE ON THE COMPRESSIBILITY FACTOR
The natural gas compressibility factor indicates the compression and expansion characteristics of natural gas under different conditions. It is a thermodynamic property used to take into account the deviation of the behaviour of real natural gases from that of an ideal gas. Compressibility factor, Z, values of natural gases are necessary for most petroleum gas engineering calculations. In this study, a comparison between five different calculation methods is presented to determine this critical parameter for the same natural gas at different conditions (pressure and temperature), using Canadian Association of Petroleum Producers, Azizi, Behbahani and Isazadeh, Dranchuk- Purvis- Robinson, Dranchuk-Abu-Kassem and Standing- Katz methods. The correlations are based on the equation of state are often implicit because they require iteration. Many correlations have been derived to enhance simplicity; however, no correlation has been developed for the entire range of pseudo-reduced pressures and temperatures. Azizi, Behbahani and Isazadeh’s method was found to have the biggest error as a result obtained for T=20° C, and p=20 bar is no longer in the field of applicability.