Research on Low Liquid Holdup Two Phase Flow in Horizontal Pipe

Authors

  • Xinhai Zhang
  • Tong Li
  • Yuxin Zhang
  • Yuanjie Liu

DOI:

https://doi.org/10.62051/ijepes.v2n3.11

Keywords:

Gas-liquid Stratified Flow, Mechanistic Model, Liquid Holdup, Pressure Gradient

Abstract

Low liquid content gas-liquid two-phase flow is widely present in wet natural gas pipelines and is one of the typical phenomena of gas-liquid two-phase flow. Liquid hydrocarbons and free water are consistently produced during the natural gas extraction and transportation processes due to factors such as pressure differentials and temperature fluctuations, leading to a low liquid-holdup pipe flow. Previous research has shown that this reduced liquid retention significantly increases pressure loss compared to single-phase gas flow. Accurately predicting pressure drop is crucial for the selection of pipeline size, pipe material, and pressurization equipment. At the same time, the liquid holdup rate is also an important parameter that determines the frequency of natural gas pipeline cleaning and the design of downstream equipment. Therefore, this article mainly focuses on the characteristics of gas-liquid two-phase flow with low liquid content during wet natural gas transportation. This article studies the gas-liquid two-phase flow patterns and different gas-liquid interface models in the literature. This article mainly compares and analyzes three low liquid content gas-liquid two-phase flow models in the literature.

References

[1] Birvalski, M., Koren, G.B., Henkes, R.A.W.M., 2014. Experiments and modelling of liquid accumulation in the low elbow of a gas/liquid pipeline. //BHR Group-9th North American Conference on Multiphase Technology. 41-55.

[2] Banafi, A., Talaie, M.R., 2014. A New Mechanistic Model to Predict Gas-Liquid Interface Shape of Gas-Liquid Flow Through Pipes with Low Liquid Loading. AIChE J. https://doi.org/10.1002/aic.14696.

[3] Zou, C., Pan, S., Zhao, Q., 2020. On the connotation, challenge and significance of China’s “energy independence” strategy. Petorl. Explor. Dev+. 47(2), 416-426. https://doi.org/10.11698/PED.2020.02.21.

[4] Chen, X.T., Cal, X.D & Brill, J.P., 1997. Gas-liquid stratified-wavy flow in horizontal pipelines. J. Energy Resour. Technol. 119(4), 209-216. https://doi.org/10.1115/1.2794992.

[5] Das, R., Pattanayak, S., 1996. Detection and analysis of transition from annular to intermittent flow in vertical tubes. Can. J. Chem. Eng. 74, 49-57. https://doi.org/10.1002/cjce.5450740107.

[6] Grolman, E., Fortuin, J.M.H., 1997. Gas-liquid flow in slightly inclined pipes. Chem. Eng. Sci. 52(24), 4461- 4471. https://doi.org/10.1016/S0009-2509(97)00291-1.

[7] Hart, J., Hamersma, P.J., 1989. Fortuin JMH. Correlations predicting frictional pressure drop and liquid holdup during horizontal gas-liquid pipe flow with a small liquid holdup. Int. J. Multiphas. Flow. 15, 947-964. https://doi.org/10.1016/0301-9322(89)90023-2.

[8] Zhang, H.-Q., Sarica, C., 2011. Low liquid loading gas/liquid pipe flow. J. Nat. Gas. Sci. Eng.. 3(2), 413-422. https://doi.org/10.1016/j.jngse.2011.03.001.

[9] Hudaya, A.Z., Widyatama, A., Dinaryanto, O., Juwana, W.E., Indarto, Deendarlianto, 2019. The liquid wave characteristics during the transportation of air-water stratified co-current two-phase flow in a horizontal pipe. Exp. Therm. Fluid. Sci. 103, 304-317. https://doi.org/10.1016/j.expthermflusci.2019.01.021.

[10] Sun, L., Zou, C., Jia, A., Wei, Y., Zhu, R., Wu, S., Guo, Z., 2019. Development characteristics and orientation of tight oil and gas in China. Petorl. Explor. Dev+. 46(6). https://doi.org/10.11698/PED.2019.06.01.

[11] Meng, W., Chen, X.T., Kouba, G.E., Sarica, C., Brill, J.P., 2001. Experimental study of low-liquid-loading gas-liquid flow in near-horizontal pipes. SPE Prod. Facil. 16(4), 240-249. https://doi.org/10.2118/74687-PA.

[12] Oliemans, R., 1987. Modeling of gas-condensate flow in horizontal and inclined pipes. //Pipeline Engineering Symposium-ETCE. Dallas: ASME.

[13] Pan, M.L., He, H., Ju, P., Hibiki, T., Ishii, M., 2015. Experimental study and modeling of disturbance wave height of vertical annular flow. Int. J. Heat. Mass. Tran. 89, 165-175. https://doi.org/10.1016/S1876-3804(21)60104-010.1016/j.ijheatmasstransfer.2015.05.073.

Downloads

Published

03-09-2024

Issue

Section

Articles

How to Cite

Zhang, X., Li, T., Zhang, Y., & Liu, Y. (2024). Research on Low Liquid Holdup Two Phase Flow in Horizontal Pipe. International Journal of Electric Power and Energy Studies, 2(3), 72-78. https://doi.org/10.62051/ijepes.v2n3.11