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GENERALIZED GRAPHICAL METHOD TO DETERMINE THE REQUIRED MEG AND METHANOL INJECTION RATE FOR NATURAL-GAS HYDRATE INHIBITION

机译:通用图形方法确定天然气水合物抑制所需的乙二醇和甲醇注入速率

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摘要

In the 87th annual GPA convention, we presented a new shortcut/graphical method for inhibition of hydrate formation temperature. Four diagrams were presented to predict the required mono ethylene glycol (MEG) weight percent in the rich solution and flowrate for the desired depression of hydrate formation temperature of natural gases with relative densities of 0.6 to 0.8. The method was applicable for a wide range of pressures (3 to 9 MPa), wet gas temperatures (20 to 50 °C) but its application was limited to only MEG with lean concentration of 80 weight percent. In order to overcome this shortcoming, we are extending our graphical method to other lean MEG concentrations and methanol (MeOH) in this paper. We used a slightly different methodology to generate the required diagrams for natural gases with relative density of 0.6 to 0.8 at pressures of 3, 5, 7 and 9 MPa and wet gas temperatures of 20, 30, 40 and 50 °C. These proposed charts are based on rigorous computer simulation. The accuracy of this generalized shortcut method is compared with rigorous computer simulation results obtained by process simulators. In addition, the results of the proposed method were compared with the available experimental data. Overall, excellent agreements have been obtained.
机译:在第87届GPA年度大会上,我们提出了一种抑制水合物形成温度的新捷径/图形方法。给出了四个图表,以预测富溶液中所需的单乙二醇(MEG)重量百分比和流速,以期望降低相对密度为0.6至0.8的天然气的水合物形成温度。该方法适用于宽范围的压力(3至9 MPa),湿气温度(20至50°C),但其应用仅限于稀薄浓度为80 wt%的MEG。为了克服这一缺点,在本文中,我们将图形方法扩展到其他贫MEG浓度和甲醇(MeOH)。我们使用略有不同的方法来生成所需的图表,这些图表的压力为3、5、7和9 MPa,湿气温度为20、30、40和50°C时,相对密度为0.6至0.8。这些建议的图表基于严格的计算机模拟。将这种广义快捷方式的准确性与过程模拟器获得的严格的计算机模拟结果进行了比较。此外,该方法的结果与现有的实验数据进行了比较。总体而言,已经获得了出色的协议。

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