Wax Deposition Prediction and Control in Waxy Crude Oil Tieback Flowlines for South China Sea Deepwater Oil Development

Author(s):  
Xichong Yu ◽  
Chunsheng Wang ◽  
Qingping Li ◽  
Yan Li ◽  
Xiaosong Zhu ◽  
...  

Crude oils are generally very complex chemical systems consisting predominantly of hundreds to thousands of hydrocarbon compounds from simple low-molecular-weight paraffin to high-molecular-weight waxes. There are many factors effecting wax deposition such as the fluid composition, pressure and temperature and so on. Wax deposition is complex dynamic process related to transient heat and mass transfer, therefore it is very difficult to predict wax deposition velocity accumulation amounts on the wall in waxy crude oil tieback flowlines. There exist many waxy crude oil tieback flowlines for South China Sea deepwater oil development, which can cause many flow assurance problems. It is very important to carry out wax deposition prediction calculation and effective measures are adopted to solve flow assurance problems. In this study, based on certain waxy crude oil tieback flowlines for South China Sea deepwater oil development, OLGA software is used to simulate transient flow characteristics in waxy crude oil tieback flowlines such as wax precipitation rate, thickness of wax layer deposited at wall, pigging frequency and so on. OLGA software simulation results is coincident with field pigging operation results, finally obtaining a good simulation methods to predict transient flow characteristics in waxy crude oil tieback flowlines and giving good suggestions to determine pigging periods and frequency. The study results show two 10 inch non-insulation steel flowlines are recommended to develop deepwater waxy crude oil field and pigging periods should comprehensive consider thickness of wax layer deposited at wall and the increase of pressure caused by wax deposition. It is reasonable to 35 days pigging periods during 2 year after put into production, 60 days pigging periods after 2 years. The results show maximum liquid flow rate for a 10 inch flowline is 7000m3/d, and it is reasonable that one flowline is used to transport when flow rate is lower than 7000m3/d, and two flowlines are used to transport when flow rate is more than 7000m3/d. The pump pressure at FPSO is kept at 6000kPaA, and required maximum liquid flow rate of pigging at FPSO is 4200m3/d (175m3/h).

1996 ◽  
Author(s):  
W.R. Low ◽  
E.J. Gerber ◽  
L.A. Simek ◽  
John Brown

2018 ◽  
Vol 32 (10) ◽  
pp. 10605-10615 ◽  
Author(s):  
Haoran Zhu ◽  
Chuanxian Li ◽  
Fei Yang ◽  
Hongye Liu ◽  
Dinghong Liu ◽  
...  

2017 ◽  
Vol 35 (18) ◽  
pp. 1831-1838 ◽  
Author(s):  
Ashish Dewangan ◽  
Ashok Kumar Yadav

1993 ◽  
Author(s):  
Guohua Zheng ◽  
J.A. Holbrook ◽  
Alvaro Bernal ◽  
M.M. Santamaria ◽  
T.M. Williams ◽  
...  

2013 ◽  
Vol 401-403 ◽  
pp. 891-894 ◽  
Author(s):  
Qing Lin Cheng ◽  
Xu Xu Wang ◽  
Xian Li Li ◽  
Wei Sun ◽  
Ling De Meng

In waxy crude oil transportation process, wax crystals start to precipitate as the oil temperature drops to wax appearance point, and then form a network structure gradually which attaches to the wall. The problem of wax deposition seriously affects the normal operation of pipeline. Based on the wax deposition tendency coefficient method, combined with experimental data, the parameters related to wax deposition tendency coefficient is fitted, and the wax deposition rate equation of crude oil is determined finally. The variation law of wax deposition rate along the pipeline is analyzed, and the influence of different seasons and different throughput the on wax deposition rate is discussed subsequently.


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