TY - GEN
T1 - Design and simulation of supersonic swirling separator
AU - Zhang, Yu Peng
AU - Wang, Shu Zhong
AU - Jing, Ze Feng
AU - Lv, Ming Ming
AU - Luo, Xiang Rong
PY - 2014
Y1 - 2014
N2 - Supersonic swirling separator has been developed for natural gas dehydration in recent years. Compared to Twister-I supersonic swirling separator, Twister-II type overcomes the disadvantage of uncontrolled shock and the steady swirling flow field contributes to high efficiency of gas-liquid separation. The design method is discussed. For the Laval nozzle, the contraction section is designed by double cubic curve method, while the method for expansion section is tapered tube method the same as the divergent tube, throat is smooth circular arc; the length of straight swirling pipe section for separation is 3-8 times of the diameter. The paper simulates the applicability of the supersonic swirling separator by Fluent. Studies have shown that the lower environmental temperature, the lower the outlet temperature, the easier water to cool, and the higher the separation efficiency. If the volume flow rate rises, the inlet velocity and the mass flow rate can be effectively improved. We can control the shock location by adjusting the pressure at the outlet of divergent pipe. The shock appears at the inlet in the working condition designed. When the outlet pressure is lower, the shock occurs in divergent tube; on the opposite, it moves forward. Beyond a certain degree, shock occurs at the Laval nozzle, the device fails to work.
AB - Supersonic swirling separator has been developed for natural gas dehydration in recent years. Compared to Twister-I supersonic swirling separator, Twister-II type overcomes the disadvantage of uncontrolled shock and the steady swirling flow field contributes to high efficiency of gas-liquid separation. The design method is discussed. For the Laval nozzle, the contraction section is designed by double cubic curve method, while the method for expansion section is tapered tube method the same as the divergent tube, throat is smooth circular arc; the length of straight swirling pipe section for separation is 3-8 times of the diameter. The paper simulates the applicability of the supersonic swirling separator by Fluent. Studies have shown that the lower environmental temperature, the lower the outlet temperature, the easier water to cool, and the higher the separation efficiency. If the volume flow rate rises, the inlet velocity and the mass flow rate can be effectively improved. We can control the shock location by adjusting the pressure at the outlet of divergent pipe. The shock appears at the inlet in the working condition designed. When the outlet pressure is lower, the shock occurs in divergent tube; on the opposite, it moves forward. Beyond a certain degree, shock occurs at the Laval nozzle, the device fails to work.
KW - Dehydration
KW - Laval nozzle
KW - Numerical simulation
KW - Shock
KW - Supersonic swirling separator
UR - https://www.scopus.com/pages/publications/84906699314
U2 - 10.4028/www.scientific.net/AMR.1008-1009.1148
DO - 10.4028/www.scientific.net/AMR.1008-1009.1148
M3 - 会议稿件
AN - SCOPUS:84906699314
SN - 9783038352082
T3 - Advanced Materials Research
SP - 1148
EP - 1153
BT - Applied Power and Energy Technology II
PB - Trans Tech Publications Ltd
T2 - 2nd International Conference on Advances in Energy and Environmental Science, ICAEES 2014
Y2 - 21 June 2014 through 22 June 2014
ER -