SiO2-Based Nanofluids for the Inhibition of Wax Precipitation in Production Pipelines

被引:2
|
作者
Lopez, Daniel [1 ]
Rios, As A. [1 ]
Marin, Juan D. [2 ]
Zabala, Richard D. [3 ]
Rincon, Jaime A. [4 ]
Lopera, Sergio H. [5 ]
Franco, Camilo A. [1 ]
Cortes, Farid B. [1 ]
机构
[1] Univ Nacl Colombia, Fac Minas, Dept Proc & Energia, Grp Invest Fenoomenos Superficie Michael Polanyi, Medellin 050034, Colombia
[2] Ecopetrol SA CPF Florena, Dept Ingn Gerencia Desarrollo & Prod, Vicepresidencia Piedemonte, Piedecuesta 681011, Colombia
[3] Ecopetrol SA, Gerencia Ctr Tecn Desarrollo, Dept Tecnol Prod, Gerencia Gen Desarrollo, Bogota 1021, Colombia
[4] Ctr Innovac & Tecnol ECOPETROL ICP, Km 7 Via Piedecuesta, Bogota 1021, Colombia
[5] Univ Nacl Colombia, Fac Minas, Dept Proc & Energia, Grp Invest Yacimientos Hidrocarburos, Medellin 050034, Colombia
来源
ACS OMEGA | 2023年 / 8卷 / 37期
关键词
POLY(ETHYLENE-CO-VINYL ACETATE) EVA; POUR POINT DEPRESSANT; CRUDE-OIL; PARAFFIN DEPOSITION; FLOW; NANOPARTICLES; CRYSTALLIZATION; PERFORMANCE; VISCOSITY;
D O I
10.1021/acsomega.3c00802
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Wax deposition in high-wax (waxy) crude oil has been an important challenge in the oil and gas industry due to the repercussions in flow assurance during oil extraction and transportation. However, the nanotechnology has emerged as a potential solution for the optimization of conventional wax removal and/or inhibition processes due to its exceptional performance in the alteration of wax morphology and co-crystallization behavior. In this sense, this study aims to study the performance of two commercial wax inhibitor treatments (WT1 and WT2) on the wax formation and crystallization due to the addition of SiO2 nanoparticles. Differential scanning calorimetry experiments and cold finger tests were carried out to study the effect of the WT on wax appearance temperature (WAT) and the wax inhibition efficiency (WIE) in a scenario with an initial temperature difference. In the first stage, the behavior of both WT in the inhibition of wax deposition was achieved, ranging in the concentration of the WT in the waxy crude (WC) oil from 5000 to 50,000 mg center dot L-1. Then, NanoWT was prepared by the addition of SiO2 nanoparticles on WT1 and WT2 for concentrations between 1000 and 500 mg center dot L-1, and the performance of the prepared NanoWT was studied at the best concentration of WIT in the absence of nanoparticles. Finally, the role of the nanofluid concentration in wax inhibition was accomplished for the best NanoWT. Selected NanoWT with nanoparticle dosage of 100 mg center dot L-1 added to WC oil at 5000 mg center dot L-1 displays reductions in WAT and WIE of 15.3 and 71.6 for NanoWT1 and -2.2 and 42.5% for NanoWT2. In flow loop experiments for the crude oil at temperatures above (30 degrees C) and below (16 degrees C), the WAT value indicates an increase of 8.3 times the pressure drops when the crude oil is flowing at a temperature below the WAT value. Therefore, when NanoWT1 is added to the crude oil, a reduction of 31.8% was found in the pressure drop in comparison with the scenario below the WAT value, ensuring the flow assurance in the pipeline in an unfavorable environment. Based on the pressure-drop method, a reduction greater than 5% in the wax deposit thickness confirms the wax deposition inhibitory character of the designed NanoWT.
引用
收藏
页码:33289 / 33298
页数:10
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