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Transport mechanism of desorbed gas in coalbed methane reservoirs

机译:煤层气藏解吸气运移机理

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The gas-liquid two-phase flow and mass transfer principle shows that the diffusion caused by concentration difference only happens in a single-phase fluid; gas-liquid two-phase diffluent solution happens in the way of dissolution; and gas-liquid two-phase insoluble or semi- soluble solution flows under differential pressure driving. These facts demonstrate that the transport of desorbed gas through matrix pores is the flow, and it doesn't conform to Fick law. The dissolution, diffusion, nucleation and bubble processes of desorbed gas through depressurization are studied, and the nonlinear flow model of free gas from matrix pores to the cleat and fracture system is established based on force analyses of the gas bubble and the gas column. Research shows that a small amount of desorbed gas diffuses by dissolution; most of them becomes nucleation and bubble, and then flows to the coal cleat and fracture system under the pressure difference driving; considering the existence of the pressure difference between the matrix pores and cleats, the pressure in coal matrix will reduce more slowly, the investigated radius will be shorter, and the outflow lag phenomenon of desorbed gas will appear. The dynamic reserve should be calculated not by using cleat pressure but by the pressure in coal matrix. The mechanism of enhanced methane recovery by CO2injection is not only replacement but displacement. Improved methane recovery can be obtained by optimizing the production pressure difference, it is not reasonable that the lower formation pressure gives higher methane recovery.
机译:气液两相流动和传质原理表明,由浓度差引起的扩散仅发生在单相流体中。气液两相扩散溶液以溶解方式发生。气液两相不溶或半溶性溶液在压差驱动下流动。这些事实表明,解吸后的气体通过基质孔进行的传输是流动,并且不符合菲克定律。研究了减压后解吸后的气体的溶解,扩散,成核和气泡过程,并基于气泡和气柱的力分析,建立了自由气体从基体孔隙到割理和裂缝系统的非线性流动模型。研究表明,少量的解吸气体通过溶解扩散。它们中的大部分成核并形成气泡,然后在压差驱动下流向煤楔和裂缝系统。考虑到基体孔隙与割理之间存在压力差,煤基体中的压力下降速度将更慢,所研究的半径将更短,并出现解吸气体的流出滞后现象。动储量不应使用割理压力来计算,而应通过煤基质中的压力来计算。通过注入二氧化碳提高甲烷采收率的机理不仅是置换,而且是置换。通过优化生产压力差可以提高甲烷的采收率,较低的地层压力提供较高的甲烷采收率是不合理的。

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