低阶煤体瓦斯减阻增渗与强化驱替试验研究

Experimental study on drag reduction-permeability increase and enhanced displacement of low-rank coal gas

  • 摘要: 为实现低阶煤体瓦斯的减阻增渗与强化驱替,基于煤体多孔介质本真属性下瓦斯吸附与驱替机理,首先利用水介质、表面活性剂CTAB、微纳米气泡的共存特性获得了液气耦合介质,以环管流量、旋转黏度表征了液气耦合介质的优化性能与提质增效特征;之后结合渗流瞬时流量、气测渗透率量化了液气耦合介质对低阶煤体瓦斯的减阻增渗与强化驱替效应。结果表明:质量分数0.05%的表面活性剂CTAB可有效降低液相表面张力50.41%,微纳米气泡可平均降低液相表面张力5.50 mN/m;基于表面活性剂CTAB与微纳米气泡的表面活性,液气耦合介质环管流量相对蒸馏水介质、含表面活性剂介质分别增大1.44、1.27倍;转速为100、200、300、600 r/min时,液气耦合介质旋转黏度相对蒸馏水介质分别降低60.00%、71.43%、50.00%、45.45%,相对含表面活性剂介质分别降低42.86%、60.00%、37.50%、25.00%。煤体分别在蒸馏水介质、含表面活性剂水介质、液气耦合介质平衡作用下甲烷渗流驱替时,随着介质环管流量的增大和旋转黏度的降低,瞬时流量与气测渗透率呈现逐渐增大的趋势。基于液气耦合介质良好的减阻性能与流动性能,对长焰煤分别在轴压为3、5 MPa,围压为3、5 MPa瓦斯驱替时,瞬时流量相对蒸馏水介质分别增大1.43、1.67倍,气测渗透率相对蒸馏水介质分别增大1.44、1.68倍,且不同轴压、围压之间的渗流差异明显缩小。液气耦合介质进一步活化了表面性能,在高流量、低黏度作用下强化对低阶煤体瓦斯的减阻增渗与强化驱替,尤其对煤体增渗解吸与抽采达标、高产工作面瓦斯涌出防治具有明确的工程导向。

     

    Abstract: In order to achieve drag reduction-permeability increase and enhanced displacement of low-order coal gas, based on the mechanism of gas adsorption and displacement under the inherent properties of coal porous media, the liquid-gas coupling medium was firstly obtained by using the coexistence characteristics of water medium, surfactant CTAB and micro and nano bubbles. The optimization performance and quality improvement characteristics of the liquid-gas coupling medium were characterized by the flow rate of the circular pipe and the rotational viscosity. Combined with the instantaneous flow of seepage and gas permeability measurement, the effects of liquid gas coupling medium on reducing drag and increasing permeability and strengthening displacement of low-rank coal gas were quantified. The results show that the liquid phase surface tension can be reduced by 50.41% with 0.05% CTAB and the average liquid phase surface tension can be reduced by 5.50 mN/m with micro-nano bubbles. Based on the surface activity of CTAB and micro and nano bubbles, the annular flow rate of liquid-gas coupled medium increases by 1.44 times and 1.27 times respectively compared with distilled water medium and surfactant containing medium. The rotational viscosity at 100, 200, 300 and 600 r/min decreased by 60.00%, 71.43%, 50.00% and 45.45% compared with distilled water medium and 42.86%, 60.00%, 37.50% and 25.00% compared with surfactant medium respectively. In the case of methane seepage displacement in distilled water medium, water medium containing surfactant and liquid gas coupling medium, the instantaneous flow rate and gas permeability gradually increase with the increase of annular flow and the decrease of rotational viscosity. Based on the good drag reduction and flow performance of the liquid gas coupling medium, when the axial pressure is 3, 5 MPa and confining pressure is 3, 5 MPa, the instantaneous flow rate increases by 1.43 and 1.67 times and the permeability measured by gas increases by 1.44 and 1.68 times respectively compared with the distilled water medium, and the seepage difference between different axial pressure/confining pressure is significantly reduced. The coupling medium of liquid and gas further activates the surface properties, strengthens the drag reduction, permeability increase and displacement of low-grade coal gas under the action of high flow and low viscosity, and has clear engineering guidance for the coal gas increase, desorption and extraction standards, and the gas emission prevention and control of high-yield working face.

     

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