Numerical simulation study of offshore heavy oil desanding by hydrocyclones

2021 ◽  
Vol 258 ◽  
pp. 118051
Author(s):  
Jiaqiang Jing ◽  
Shijian Zhang ◽  
Min Qin ◽  
Jiaqi Luo ◽  
Yuting Shan ◽  
...  
Energies ◽  
2017 ◽  
Vol 10 (12) ◽  
pp. 1999 ◽  
Author(s):  
Jun Ni ◽  
Xiang Zhou ◽  
Qingwang Yuan ◽  
Xinqian Lu ◽  
Fanhua Zeng ◽  
...  

Fuel ◽  
2020 ◽  
Vol 262 ◽  
pp. 116559 ◽  
Author(s):  
Xinqian Lu ◽  
Xiaolong Peng ◽  
Zeyu Lin ◽  
Xiang Zhou ◽  
Fanhua Zeng

Geofluids ◽  
2021 ◽  
Vol 2021 ◽  
pp. 1-12
Author(s):  
Fan Liu ◽  
Qingdong Ni ◽  
Chunguang Zhang ◽  
Wensheng Zhou ◽  
Jingqi Lin ◽  
...  

The heavy-oil flow in porous media is characterized by non-Darcy law with variable threshold pressure gradient (TPG) due to the large fluid viscosity. However, available analytical and numerical models hardly consider this effect, which can lead to erroneous results. This paper is aimed at presenting an innovative approach and establishing a numerical simulator to analyze the heavy-oil flow behavior with waterflooding. The apparent viscosity of the oil phase and flow correction coefficient characterized by the TPG were applied to describe the viscosity anomaly of heavy oil. Considering the formation heterogeneity, the TPG was processed into a variable related to mobility and the directionality. The discretization and linearization of the mathematical model were conducted to establish a fully implicit numerical model; the TPG value on each grid node was obtained through oil phase mobility interpolation, and then, the Jacobi matrix was reassembled and calculated to solve pressure and saturation equations. The corresponding simulator was thus developed. The pre-/postprocessing module of the simulator is connected to ECLIPSE; then, an efficient algorithm is introduced to realize a fast solution. Results show that considering the TPG will not only reduce the waterflooding area but also reduce the oil displacement efficiency because of aggravating the nonpiston phenomenon and interlayer conflict. The numerical simulation study on the TPG of heavy oil provides theoretical and technical support for the rational development and adjustment of water-driven heavy oil.


2020 ◽  
pp. 1-23
Author(s):  
Xinqian Lu ◽  
Zeyu Lin ◽  
Xiang Zhou ◽  
Fanhua Zeng

Abstract Heavy oil resources, as a non-renewable energy resource, often requires extra enhanced oil recovery techniques such as solvent-based processes. Many kinds of solvents including pure and mixed solvent have been tested in the solvent-based applications. Compared with pure solvent, the solvent mixture has an advantage of relatively higher dew point pressure while maintaining desirable solubility in heavy oil. The characterization of foamy oil behavior in pure solvent system is different from the solvent mixture system despite their similarities. Thus, an additional numerical simulation study is necessary for solvent mixture system. This work conducted simulation studies to investigate foamy oil behavior in a heavy oil-mixture solvent (C1+C3) system from pressure depletion tests. A better understanding of foamy oil characterization and mechanism in a heavy oil-mixture solvent system is obtained. A reliable non-equilibrium model is developed to perform simulation studies. Since previous experiments suggest the behavior of foamy oil in the solvent mixture system share similarities with the heavy oil-methane system, this investigation first conducted simulation study with consideration of two reactions in the model and achieved good agreements between the simulated calculation results and experimentally measurement. Then four reactions are considered in the model for simulation study and obtained better history match results. The simulation results suggest methane has more impact on the foamy oil behaviors than propane in the heavy oil-mixture solvent system. This work also discussed effect of model parameters involved in the history matching process and conducted sensitivity analysis.


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