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Development an Easy-to-Use Simulator to Thermodynamic Design of Gas Condensate Reservoir’s Separators

DOI: 10.4236/mnsms.2018.81001, PP. 1-19

Keywords: Separator Design, Matlab Software, Simultaneous Algorithm, Optimum Condition, Gas Condensate Reservoir

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Abstract:

Separator design in petroleum engineering is so important because of its important role in the evaluation of optimum parameters and also to achieve to maximum stock tank liquid. However, no simulator exists that simultaneously and directly optimizes the parameters “pressure”, “temperature”, and so on. On the other hands, Commercial simulators fix one parameter and vary another parameter to achieve the optimum conditions. So, they need long-time simulation. Moreover, gas condensate reservoirs, like another reservoirs, have this problem as well. In present paper, a self-developed simulator applied in the optimized design of gas condensate reservoir’s separators by determining optimized pressure, temperature, and number of separators in order to obtain maximized tank liquid volume and minimized tank liquid density utilizing Matlab software and other commercial simulators such as Aspen-Plus, Aspen-Hysys, and PVTi to do a comparison. Also, each software was separately tested with one, two, and three separators to obtain the optimum number of separators. Additionally, Peng-Robinson equation of state (PR EOS) has been applied in the simulation. For simulation input, a set of field data of gas condensate reservoir has been utilized, as well. The results show a good compatibility of this simulator with other simulators but in so little runtime (this simulator calculates the optimum pressure and temperature in a wide range of pressures and temperatures with the help of a simultaneous optimization algorithm in one stage) and the highest stock tank liquid is calculated with this simulator in comparison to other simulators. Also, with the help of this simulator, we are able to obtain the optimum pressure, temperature, and the number of separators in the gas condensate reservoir’s separators with any desired properties. Finally, this simulator optimizes the temperatures for each separator and obtains very good results despite the other simulators that fix temperatures for all separators in most times.

References

[1]  Ahmed, T. (2010) Reservoir Engineering Handbook. 4th Edition, Gulf Professional Publishing, Texas.
[2]  Danesh, A. (1998) PVT and Phase Behavior of Petroleum Reservoir Fluids. Elsevier, Amsterdam.
[3]  Firoozabadi, A. (1999) Thermodynamics of Hydrocarbon Reservoirs. McGraw-Hill, Pennsylvania Plaza, New York.
[4]  Arnold, K. and Stewart, M. (2008) Surface Production Operations. 3rd Edition, Gulf Professional Publishing, Texas.
[5]  Assael, M.J., Trusler, M. and Tsolakis, T.F. (1996) Thermo Physical Properties of Fluids: An Introduction to Their Prediction. Imperial College Press, London.
https://doi.org/10.1142/p007
[6]  Adjiman, C.S., Dallwig, S., Floudas, C.A. and Neumaier, A. (1998) A Global Optimization Method, Alfa BB, for General Twice-Differentiable Constrained NLPs Theoretical Advances. Computers & Chemical Engineering, 22, 1137-1158.
https://doi.org/10.1016/S0098-1354(98)00027-1
[7]  Harding, S.T. and Floudas, C.A. (2000) Phase Stability with Cubic Equations of State: Global Optimization Approach. American Institute of Chemical Engineers Journal, 46, 1422-1440.
https://doi.org/10.1002/aic.690460715
[8]  Zhu, Y., Wen. H. and Xu, Z. (2000) Global Stability Analysis and Phase Equilibrium Calculations at High Pressures Using the Enhanced Simulated Annealing Algorithm. Chemical Engineering Science, 55, 3451-3459.
https://doi.org/10.1016/S0009-2509(00)00015-4
[9]  Vázquez-Román, R., García-Sánchez, F., Salas-Padrón, A., Hernández-Garduza, O. and Eliosa-Jiménez, G. (2000) An Efficient Flash Procedure Using Cubic Equations of State. Chemical Engineering Journal, 84, 201-205.
https://doi.org/10.1016/S1385-8947(00)00276-X
[10]  Nichita, D.V., Gomez, S. and Luna, E. (2002) Multiphase Equilibria Calculation by Direct Minimization of Gibbs Free Energy with a Global Optimization Method. Computers & Chemical Engineering, 26, 1703-1724.
https://doi.org/10.1016/S0098-1354(02)00144-8
[11]  Chaikunchuensakun, S., Stiel, L.I. and Baker, E.L. (2002) A Combined Algorithm for Stability and Phase Equilibrium by Gibbs Free Energy Minimization. Industrial & Engineering Chemistry Research, 41, 4132-4140.
https://doi.org/10.1021/ie011030t
[12]  Zhou, H., Sun, W.M. and Xia, N. (2004) Application of CFD in the Modification of an Oil-Gas Separator Design. Journal of Hydrodynamic (Ser. A), 19, 926-929.
[13]  Zhang, L.H., Xiao, H., Zhang, H.T., Xu, L.J. and Zhang, D. (2007) Optimal Design of a Novel Oil-Water Separator for Raw Oil Produced from ASP Flooding. Journal of Petroleum Science and Engineering, 59, 213-218.
https://doi.org/10.1016/j.petrol.2007.04.002
[14]  Bahadori, A., Vuthaluru, H.B. and Mokhatab, S. (2008) Optimizing Separator Pressures in the Multistage Crude Oil Production Unit. Asia-Pacific Journal of Chemical Engineering, 3, 380-386.
https://doi.org/10.1002/apj.159
[15]  Rossi, C.C., Cardozo-Filho, L. and Guirardello, R. (2009) Gibbs Free Energy Next Term Minimization for the Calculation of Chemical and Phase Equilibrium using Linear Programming. Fluid Phase Equilibria, 278, 117-128.
https://doi.org/10.1016/j.fluid.2009.01.007
[16]  Carroll, J. (2014) Natural Gas Hydrates: A Guide for Engineers. Gulf Professional Publishing, Houston.
[17]  Ejraei Bakyani, A., Sahebi, H., Ghiasi, M.M., Mirjordavi, N., Esmaeilzadeh, F., Lee, M. and Bahadori, A. (2016) Prediction of CO2-Oil Molecular Diffusion using Adaptive Neuro-Fuzzy Inference System and Particle Swarm Optimization Technique. Fuel, 181, 178-187.
https://doi.org/10.1016/j.fuel.2016.04.097
[18]  Peng, D.Y. and Robinson, D.B. (1976) A New Two-Constant Equation of State. Industrial & Engineering Chemistry Fundamentals, 15, 59-64.
https://doi.org/10.1021/i160057a011
[19]  Soave, G. (1972) Equilibrium Constants from a Modified Redlich-Kwong Equation of State. Chemical Engineering Science, 27, 1197-1203.
https://doi.org/10.1016/0009-2509(72)80096-4
[20]  Wilson, G. (1968) A Modified Redlich-Kwong EOS, Application to General Physical Data Calculations. American Institute of Chemical Engineers 65th National Meeting, Paper No. 15C.

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