Performance Evaluation of Demulsifier Using the Optimum Formulation HLD Concept: A Practical Case Using Heavy Crude Oil Diluted in Naphtha or in Synthetic Aromatic Oil

被引:10
作者
Meza, L. [1 ]
Alvarado, J. G. [1 ]
Marquez, R. [1 ,2 ]
Forgiarini, A. [1 ]
机构
[1] Univ Los Andes, FIRP Lab, Bogota, Colombia
[2] Pole Etud & Rech Lacq, TotalEnergies SE, Lacq, France
来源
SPE JOURNAL | 2022年 / 27卷 / 04期
关键词
INTERFACIAL-TENSION; ASPHALTENE AGGREGATION; EMULSION STABILITY; PHASE-BEHAVIOR; WATER SYSTEMS; RESINS; BREAKING; ASSOCIATION; SEPARATION; SOLVENCY;
D O I
10.2118/209577-PA
中图分类号
TE [石油、天然气工业];
学科分类号
0820 ;
摘要
Asphaltene-stabilized water-in-oil (W/O) emulsions can cause severe problems during oil production and transportation. These emulsions are broken by adding a demulsifying agent at a suitable concentration (C-D*) to obtain the optimal formulation, with minimal emulsion stability (stability*). Herein, we studied, from a phenomenological point of view, the perfonnance of two demulsifiers on W/O emulsion breaking with high asphaltene content A very simple polyethoxylated nonylphenol demulsifier (6E0) and a complex commercial demulsifier (COD) were studied. The influence of the chemical nature of the oil phase on the performance of the demulsifiers was evaluated. The emulsion stability* and C-D* values of W/O systems of heavy crude oil diluted in cyclohexane (Systems A and B) were compared to W/O emulsions composed by a heavy crude oil diluted in heavy naphtha or in an aromatic synthetic crude oil as the oil phase (Systems C and D). The results show that demulsifier performance improves significantly when the crude oil is diluted in heavy naphtha and in aromatic synthetic crude oil, obtaining unstable W/O emulsions (rupture time of 10(-2)-10(-1) minutes). In the latter cases, the C-D* value is significantly lower and with a wide area of low emulsion stability compared to systems formulated with crude oil diluted in cyclohexane. The mechanisms that generate this type of behavior are discussed and strategies to increase performance and robustness analyzed.
引用
收藏
页码:1856 / 1868
页数:13
相关论文
共 82 条
[61]   How to Attain Ultralow Interfacial Tension and Three-Phase Behavior with Surfactant Formulation for Enhanced Oil Recovery: A Review. Part 4: Robustness of the Optimum Formulation Zone Through the Insensibility to Some Variables and the Occurrence of Complex Artifacts [J].
Salager, Jean-Louis ;
Anton, Raquel E. ;
Arandia, Maria A. ;
Forgiarini, Ana M. .
JOURNAL OF SURFACTANTS AND DETERGENTS, 2017, 20 (05) :987-1018
[62]   SURFACTANT-OIL-WATER SYSTEMS NEAR THE AFFINITY INVERSION .1. RELATIONSHIP BETWEEN EQUILIBRIUM PHASE-BEHAVIOR AND EMULSION TYPE AND STABILITY [J].
SALAGER, JL ;
LOAIZAMALDONADO, I ;
MINANAPEREZ, M ;
SILVA, F .
JOURNAL OF DISPERSION SCIENCE AND TECHNOLOGY, 1982, 3 (03) :279-292
[63]   Apparent equilibration time required for a surfactant-oil-water system to emulsify into the morphology imposed by the formulation [J].
Salager, JL ;
Moreno, N ;
Antón, R ;
Marfisi, S .
LANGMUIR, 2002, 18 (03) :607-611
[64]   Partitioning of ethoxylated octylphenol surfactants in microemulsion-oil-water systems: Influence of temperature and relation between partitioning coefficient and physicochemical formulation [J].
Salager, JL ;
Marquez, N ;
Graciaa, A ;
Lachaise, J .
LANGMUIR, 2000, 16 (13) :5534-5539
[65]  
Salager JL., 2000, PHARM EMULSIONS SUSP, P19, DOI [10.1201/b14005-3, DOI 10.1201/B14005-3, 10.1201/b14005-3.]
[66]  
Salager JL, 1990, Int Chem Eng, V30, P103
[67]  
SCHRAMM LL, 1992, ADV CHEM SER, V231, P1
[68]   Overview of Asphaltene Nanostructures and Thermodynamic Applications [J].
Schuler, Bruno ;
Zhang, Yunlong ;
Liu, Fang ;
Pomerantz, Andrew E. ;
Andrews, A. Ballard ;
Gross, Leo ;
Pauchard, Vincent ;
Banerjee, Sanjoy ;
Mullins, Oliver C. .
ENERGY & FUELS, 2020, 34 (12) :15082-15105
[69]   Effect of Asphaltene Structure on Association and Aggregation Using Molecular Dynamics [J].
Sedghi, Mohammad ;
Goual, Lamia ;
Welch, William ;
Kubelka, Jan .
JOURNAL OF PHYSICAL CHEMISTRY B, 2013, 117 (18) :5765-5776
[70]  
Shutang G., 2010, SPE EOR Conference at Oil and Gas West Asia