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Experimental Investigation of Interfacial Interactions of Condensate/Brine/SC-CO_2 Systems at High Pressure and High Temperature Conditions

机译:高压和高温条件下冷凝水/盐水/ SC-CO_2系统界面相互作用的实验研究

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The subject of enhanced natural gas and condensate recovery by supercritical CO_2 (SCCO_2) injection tends to be bypassed by researchers despite the existence of several laboratory and field studies of CO_2 displacements in conventional oil reservoirs. While the phase behavior of SCCO_2/condensate system is a critical factor in determining the effectiveness of the recovery process nevertheless, the interfacial tension (IFT) is an important parameter in verifying the efficiency of the displacement process. This paper investigates the IFT behaviour for a CO_2/condensate/brine system at temperatures of 95, 120, 140 and 160 °C, and a pressure range of 1000 to 6000 psi. A high pressure high temperature rig incorporating a pendent drop facility was utilised to simulate reservoir conditions and was subsequently employed to measure the interfacial tensions. The results of this study show that while pressure acts to reform the surface molecules of the CO_2 drop and thus significantly lowers the IFT; temperature however, tends to increase this tension resulting in a declining miscibility of the CO_2-condensate system. This work is part of an integrated project that is conducted for a West Australasian field.
机译:尽管存在常规储油储层中的CO_2位移的若干实验室和现场研究,但是通过研究人员绕过增强天然气和超临界CO_2(SCCO_2)注射的受试者往往被研究人员绕过。虽然SCCO_2 /缩合系统的相位行为是确定恢复过程的有效性的关键因素,但界面张力(IFT)是验证位移过程效率的重要参数。本文研究了在95,120,140和160℃的温度下的CO_2 /冷凝水/盐水系统的IFT行为,压力范围为1000至6000psi。利用包含吊坠设施的高压高温钻机来模拟储层条件,随后用于测量界面紧张局部。本研究的结果表明,虽然压力作用于改革CO_2下降的表面分子,因此显着降低IFT;然而,温度趋于增加这种张力,导致CO_2-冷凝水系统的混溶性下降。这项工作是为西澳大利亚领域进行的综合项目的一部分。

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