The undersea separation was widely used in the petroleum industry to improve the efficiency and keep the well pressure. High gas?liquid ratio condition exists in offshore gas field frequently and for this condition, a novel two-stage gas and liquid cylindrical cyclone was designed. In order to increase the separation efficiency, some parts had been added in the separator. The size parameters of the separator were designed by using effective volume transformation methods, and a method for diameter determination was also proposed based on the characteristics of liquid drop breaking in swirl field. This determination described the liquid drop’s changing shape and breaking in the gas cyclone field and the critical relative velocity of the gas phase and liquid phase when the liquid drops started to break had also been calculated. The model based on the pressure field by the solution of Navier?Stocks equation and had also been verified by the experiments which had measured the liquid drops diameters by using Malvern laser particle size analyzer and the data from model and experiments kept high consistency. Different turbulence models, different meshing schemes and different discrete formats had been compared in order to choose the best numerical simulation plan and this plan also had been validated by existing experimental data. The characteristics of asymmetry were analyzed by CFD about the internal flow field of the simplified model and the influence of structural parameters and operational parameters were also obtained. The results of the models showed that it was very diffcult for oil drops in different diameters to break in the gas cyclone fields. The results of the numerical simulation showed that the length of the separator had little effect on the asymmetry characteristics of the internal flow field and the inlet velocity and the ratio of the length and width of inlet would not make the internal flow field become unstable.
Zhaoming YANG Jianlei CHEN Yunrui HAN Limin HE Xiaoming LUO
. Design of two-stage swirling gas?liquid separator and simulation of flow field characteristics[J]. The Chinese Journal of Process Engineering, 2018
, 18(6)
: 1198
-1209
.
DOI: 10.12034/j.issn.1009-606X.218124
[1] Erdal F.M., Shirazi S. A. Effect of Inlet Configuration on Flow Behavior in a Cylindrical Cyclone Separator[C]. ASME. 2002: 521-529. [2] Kouba G.E., Wang S., Gomez L.E., et al. Review of the State-of-the-Art Gas/Liquid Cylindrical [3]Cyclone(GLCC) Technology -Field Applications[C].SPE 104256, 2006. [4] Wang S., Mohan R., Shoham O., et al. Optimal Control Strategy and Experimental Investigation of [5]Gas-Liquid Compact Separators[C].SPE 78270, 2002. [6] Wang S., Kouba G.E., Marrelli J., et al. The State-of-the-Art of Gas-Liquid Cylindrical Cyclone Control [7]Technology: From Laboratory to Field[J].Journal of Energy Resources Technology. 2010, 132(3). [8] Erdal F.M., Shirazi S.A., Mantilla I. et al. Computational Fluid Dynamics (CFD) Study of Bubble Carry-Under in Gas-Liquid Cylindrical Cyclone Separators[C]. SPE, 66500 2000. [9] Arpandi I.A., Joshi A. R., Shoham O., et al. Hydrodynamics of Two-Phase Flow in Gas-Liquid [10]Cylindrical Cyclone Separators[C].SPE 30683, 1996. [11] Earni S., Marrelli J. D., Wang S., et al. Slug Detection as a Tool for Predictive Control of GLCC [12]Compact Separators[J].Journal of Energy Resources Technology. 2003, 125(2): 145-153. [13] Wang S., Kouba G. E., Gomez L. E., et al. Gas-Liquid Cylindrical Cyclone (GLCC) Compact Separators For Wet Gas Applications[J]. Journal of Energy Resources Technology. 2003, 125(1): 43-50. [14]薄启炜, 张琪, 林博, 等.螺旋式井下油气分离器设计与分析[J].石油机械, 2003, 31(1):8-10 [15]王尊策, 崔航, 李森, 等.井下螺旋式气液分离器分离性能的数值模拟[J].科学技术与工程, 2010, 10(6):1358-1361 [16] 金向红, 金有海, 王建军, 等.气液旋流器的分离性能[J]. 中国石油大学学报(自然科学版). 2009, 33(5): 124-129. [17] 金向红, 金有海, 王建军, 等.气—液旋流分离技术应用的研究进展[J]. 化工机械. 2007, 34(6): 351-355. [18] 静玉晓.轴流导叶式旋流分离器的研制[D]. 青岛: 中国石油大学(华东), 2010. [19] Peixoto G.A., Ribeiro G. A. S., Barros P. R. A., et al. VASPS Prototype in Marimba Field–Workover and Re-Start[C]. SPE 95039, 2005. [20]Fischer P A.Subsea production systems progressing quickly[J].World Oil, 2004, 25(11):30-32 [21] Lim D., Gruehagen H. Subsea Separation and Boosting-An Overview of Ongoing Projects[C]. SPE 123159, 2009. [22] Ju G.T., Littell H. S., Cook T. B., et al. Perdido Development: Subsea and Flowline Systems[C]. OTC 20882, 2010. [23] Iyer S., Lang P., Schoppa W., et al. Subsea Processing at Parque das Conchas(BC-10): Taking Flow Assurance to the Next Level[C]. OTC, 2010. [24] Mogseth G.Functional Verification of the Worlds First Full Field Subsea Separation [25]System-TIORA[C].OTC 19328, 2008. [26] Vu V.K., Fantoft R., Shaw C, et al. Comparison of Subsea Separation Systems[C]. OTC 20080, 2009. [27] Zhao B.Prediction of gas-particle separation ef?ciency for cyclones: A time-of-?ight model[J]. [28]Separation and Puri?cation Technology.2011, 85(2): 171–177. [29]金向红, 金有海, 王建军, 等.气液旋流器的分离性能[J].中国石油大学学报:自然科学版, 2009, 33(5):124-129 [30]Hsiang L P, Faeth G M.Near-limit drop deformation and secondary breakup[J].International Journal of Multiphase Flow, 1992, 18(5):635-652 [31]Wang L, Feng J, Gao X, et al.Investigation on the oil–gas separation efficiency considering oil droplets breakup and collision in a swirling flow[J]. Chemical Engineering Research & Design, 2017, 117:394-400. [32] Wang A, Marashdeh Q, Fan L S.ECVT imaging and model analysis of the liquid distribution inside a horizontally installed passive cyclonic gas–liquid separator[J]. Chemical Engineering Science, 2016, 141:231-239. [33] Yoshidaa H., Kwan-Sikb Y, Fukuib K., et al. Effect of apex cone height on particle classification performance of a cyclone separator[J]. 2003, 14(3): 263-278. [34]陈建磊, 何利民, 罗小明, 等.旋流分离器流场模拟研究方法优化选择[J].过程工程学报, 2013, 13(5):721-727 [35]M.D. Slack,Prasad R O,Bakker A,et alAdvances in Cyclone Modelling Using Unstructured Grids[J].Chemical Engineering Research & Design, 2000, 78(8):1098-1104 [36] 魏耀东, 张静, 宋健斐, 等.旋风分离器自然旋风长的试验研究. 热能动力工程. 2010, 25(2): 206-210. [37] 宋健斐, 魏耀东, 时铭显.蜗壳式旋风分离器内气相流场非轴对称特性分析[J]. 化工学报. 2007(58): 1091-1096.