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Modelling of Gas Exsolution and Transport in a Live Heavy Oil Reservoir

机译:活重油储层燃气扑火和运输建模

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Depressurization causes the exsolution of dissolved gases as bubbles within the live heavy oil reservoirs. The exsolution of bubbles increases the fluid volume within the reservoir, forcing both oil and bubbles to the well. Subsequently, growth and coalescence lead different sizes of gas bubbles accumulation in the producing zone which mainly controlled by viscous and capillary forces. Laboratory data show a significant amount of gas bubbles become trapped in the flow system. This entrapment of the gas phase results in higher critical gas saturation. Modelling of gas bubble exsolution and transport is vitally important in designing production technology for improving oil recovery. This project was devoted to develop a mechanistic foamy oil model for quantifying gas exsolution and transport which can operate within the commercial reservoir simulator. The foamy oil model has been completed in two parts: In Part 1, a kinetic model with five components and four reactions was developed to simulate gas exsolution in a live heavy oil reservoir. The kinetic model coupled with the commercial simulator (CMG STARS) was applied to history matching of several laboratory gas exsolution experimental data. Performance of the model in special form under different flow regimes has been presented at the 2005 SPE/PS-CIM/CHOA Symposium. In Part 2, we developed a set of analytical functions to quantify gas bubbles partition and gas-oil relative mobility in reservoir porous media as function of capillary number. In this paper, the foamy oil model in generalized form is systematically presented: (1) history matches of mercury withdrawal experiments – studying the gas exsolution parameters with capillary number, (2) analysis of micro-model tests – developing a gas bubbles partition function depending on capillary number, and (3) history matches of radial drainage pressure depletion experiments – developing a set of relative permeability alteration functions depending on grid block capillary number for field scale modeling.
机译:减压导致溶解气体作为活重油储层内的气泡。气泡的输出增加了储存器内的流体体积,迫使油和气泡到井。随后,生长和聚结的产生不同大小的气泡积聚在主要由粘性和毛细力控制的产生区中。实验室数据显示出大量的气泡被困在流动系统中。这种气相的夹杂物导致临界气体饱和度更高。气泡扑灭和运输的建模在设计生产技术方面至关重要。该项目致力于开发机械泡沫油模型,用于量化燃气爆震和运输,可在商业储层模拟器内运行。泡沫油模型已完成两部分:在第1部分中,开发了具有五种组分和四种反应的动力学模型,以模拟活重油储存器中的气体泄露。与商业模拟器(CMG恒星)相结合的动力学模型应用于几种实验室气体输出实验数据的历史匹配。在2005年SPE / PS-CIM / CHOA研讨会上介绍了不同流动制度下特殊形式的模型的性能。在第2部分中,我们开发了一组分析功能,以在储层多孔介质中量化气泡分区和气体油相对迁移率作为毛细数量。在本文中,系统地呈现了广义形式的泡沫油模型:(1)汞戒断实验的历史匹配 - 利用毛细管数研究气体输出参数,(2)微型试验分析 - 开发气泡分区功能根据毛细管数,(3)径向排水压力耗尽实验的历史匹配 - 根据网格块毛细管编号,开发一组相对渗透性改变功能,用于现场规模建模。

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