徐孝轩, 刘德生, 宫敬, 孙长征. 液相粘度对水平管气液两相流型的影响[J]. 油气储运, 2013, 32(3): 236-240. DOI: 10.6047/j.issn.1000-8241.2013.03.002
引用本文: 徐孝轩, 刘德生, 宫敬, 孙长征. 液相粘度对水平管气液两相流型的影响[J]. 油气储运, 2013, 32(3): 236-240. DOI: 10.6047/j.issn.1000-8241.2013.03.002
Xu Xiaoxuan, Liu Desheng, Gong Jing, Sun Changzheng. The influence of liquid viscosity on gas-liquid two-phase flow in horizontal pipe[J]. Oil & Gas Storage and Transportation, 2013, 32(3): 236-240. DOI: 10.6047/j.issn.1000-8241.2013.03.002
Citation: Xu Xiaoxuan, Liu Desheng, Gong Jing, Sun Changzheng. The influence of liquid viscosity on gas-liquid two-phase flow in horizontal pipe[J]. Oil & Gas Storage and Transportation, 2013, 32(3): 236-240. DOI: 10.6047/j.issn.1000-8241.2013.03.002

液相粘度对水平管气液两相流型的影响

The influence of liquid viscosity on gas-liquid two-phase flow in horizontal pipe

  • 摘要: 在长52 m、内径25.7 mm的不锈钢管水平环道上,研究了液相粘度对水平管气液两相流流型的影响。试验中观测到5种流型:气团流、分层流、分层波浪流、段塞流、波浪流。在气、液折算速度相同的情况下,随液相粘度增大,气团流的长气泡增长,分层流和段塞流的液膜高度减小,段塞频率增大,波浪的平均液高和振幅增大,波浪的速度和频率减小。绘制了不同液相粘度下的气液两相流型图,当液相粘度不小于20 mPa·s时,未观察到分层波浪流;随液相粘度增大,分层流的区域逐渐减小,气团流向段塞流的转换边界向小气速方向偏移,生成波浪流的边界向小液速大气速方向偏移,且更易形成段塞流。使用T-D模型进行对比验证,当液相粘度相对较大时,该模型不适用于本实验条件下的流型计算。

     

    Abstract: The paper researches the influence of liquid viscosity on gas-liquid two-phase flow in horizontal loop of 52 m-long stainless steel pipe with an inner diameter of 25.7 mm. The five flow patterns observed in the test include air mass flow, stratified flow, stratified wavy flow, slug flow and wave flow. In the case that calculated speed for the gas is same with that of the liquid, along with the increase of liquid viscosity, the long bubbles in air mass flow become longer, the height of liquid film of stratified flow and slug flow decreases, the slug frequency increases, the average liquid level and amplitude of flow wave increases and the speed and frequency of the wave are reduced. The gas-liquid two-phase flow pattern map under different liquid viscosities is plotted. There is no stratified wavy flow found when the liquid viscosity is not less than 20 mPa·s, and with the increase in liquid viscosity, the area of stratified flow is gradually decreased, the transition boundary from air mass flow into slug flow is drifted to the direction of small gas speed, the boundary for generating wave flow is drifted to the direction of liquid speed and high gas speed, easily forming a slug flow. Comparison verification with T-D model is performed, which is not suitable for flow pattern calculation under the experimental condition when the liquid viscosity is relatively large.

     

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