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Document Type : Short Communication

Authors

1 international Petro offshore niam kish

2 AmirKabir University Of Technology

3 NISOC

Abstract

One of the most controversial usages of coiled tubing in stimulation operation is the calculation of the optimum pumping rate and coiled tubing depth. Considering the investigations conducted in one of the Iranian offshore oilfields, the simulation and optimization of coiled tubing operation can be accomplished by two phase flow simulator (OLGA) and MATLAB curve fitting Simmons model to obtain the optimum rate and the depth of operation with regard to the limitations imposed by the amount of nitrogen and the operation time. Simulation and field results are compared with good agreement. The simulation and optimization comprise of both theoretical and experimental aspects on the basis of multiphase considerations. The result of simulation and comparisons are done on the basis of the nitrogen amount limitation. In this paper, it is attempted to state the necessity of coiled tubing dominant variable optimization by representing an economic equation, based on simulation results of a real operation with perception of two-phase flow realities.

Keywords

[1] Dale M. Dusterhoft, Kelly L. Falk, J.G. Misselbrook, Journal of Canadian Petroleum Technology,32 09, (1993).
[2] A. Hernandez, Fundamentals of Gas Lift Engineering 1st Edition,Gulf Professional Publishing, (2016).
[3] Cazarez-Candia, O., Vásquez-Cruz, M. A, Journal of Petroleum Science and Engineering, 46 195-208, (2005).
[4] Y. Arjmand, drilling fluid flow simulation using OLGA Software, B.Sc. thesis, Amir Kabir University of Technology, Tehran, Iran (2018).
[5] P.K. Currie, J. D. J. a., Modelling and Optimization of Oil and Gas Production Systems, TU Delft,Version 5c,The Netherlands, March (2004).
[6] Economides M. J., Hill A. D., Ehlig-Economides C., Petroleum Production Systems, Prentice Hall 2nd edition, (October 5, 2012).
[7] Eduardo Camponogara, Paulo H.R. Nakashima, European journal of operational research,74 1220–1246, (2005).
[8] Gomez L. E., Shoham, O., Taitel, Y., International Journal of Multiphase Flow, 26-517-521, (2000).
[9]Mohammadreza Kamyab, Vamegh Rasouli,Journal of Natural Gas Science and Engineering 29 284-302,(2016).
[10] J.N.M. de Souza, J.L. de Medeiros, A.L.H. Costa, G.C. Nunes, Journal of Petroleum Science and Engineering 72 277–289, (2010).
[11] Florent Di Meglioa, Nicolas Petit, Vidar Alstad, Glenn-Ole Kaasa, Journal of Process Control, 22 809– 822, (2012).
[12] R. Zhang, Z. W., Shen Guan, M. Fang, X. Zhang, Natural Gas Science and Engineering, 24, (2015).
[13] B.G.M. van Wachem, A.E. Almstedt, Chemical Engineering Journal 96 81–98,(2003).
[14] Faravar Amir, Mehrdad Manteghian, International Journal of New Chemistry, 6 (1), (2019).
[15] Yingfeng Meng, Chaoyang Xu, Na Wei, Gao Li, Hongtao Li, Mubai Duan, Journal of Natural Gas Science and Engineering, 22 646-655, (2015).
[16] N. Zand, acquire the operational economical rate and depth for coil tubing nitrogen lift operation with two methods of multiphase flow simulator software and particle swarm optimization algorithm, M.Sc. thesis, Amir Kabir University of Technology, Tehran, Iran (2015).
[17] Hu L., Gao D., Journal of Natural Gas Science and Engineering,22 656-660, (2015).
[18] Camponogara, E., Nakashima, P., Eur. J. Oper. Res. 174, 1220–1246, (2006).
[19] Ray, T., Sarker, R., Journal of petroleum science and engineering, 59 84–96, (2007).
[20] Guerrero-Sarabia I., Fairuzo, Y. V., Journal of Petroleum Science and Engineering,108 162-171, (2013).
[21] Alex Crabtree, Journal of Petroleum Technology, 71 06, (2019).
[22] M. Sussman, P. Smereka, S. Osher, J. Comput. Phys.,114 146, (1994).
[23] D. Gueyffier, J. Li, R. Scardovelli, S. Zaleski, J. Comp. Phys., 152 423–456, (1999).
[24] Noormohammadi Mohammad, Molood Barmala, International Journal of New Chemistry, 6 (4), (2019).
[25] Hamedi, H. R. F., Khamechi, E., Petroleum Science and Technology, 1 418-427, (2011).
[26] Clegg, J. D., Bucaram, S. M., Hein N. W., Journal of Petroleum Technology, (1993).
[27] Mahdiani M. R., Khamehchi E., Journal of Natural Gas Science and Engineering, 26 18-27, (2015).
[28] Begs D. H., Brill J. P.,Journal of Petroleum technology, (1973).
[29] Takács, G., Gas Lift Manual PennWell,PennWell Corp., (July 31, 2005).
[30] noormohammadi Mohammad, International Journal of New Chemistry, 6, (2019).
[31] Kanu E. P., Mach, J., Brown K. E., journal of Petroleum Technology, (1981).