Articles Information
Chemistry Journal, Vol.4, No.3, Sep. 2018, Pub. Date: Aug. 31, 2018
Investigation of Viscosity Variations for Heavy, Light and Medium Crude Oil as Basic Fluid of Well
Pages: 60-64 Views: 1547 Downloads: 474
Authors
[01]
Sina Moradi Shalali, Department of Petroleum Engineering, Omidieh Branch, Islamic Azad University, Omidieh, Iran.
[02]
Farshad Farahbod, Department of Chemical Engineering, Firoozabad Branch, Islamic Azad University, Firoozabad, Iran.
Abstract
Finding the properties of crude oil after addition of nano particle is considered in this work. The experiments are held to investigate the effect of nano particles on the physical properties of two kinds of heavy crude oil (API =21.45), medium crude oil (API=27.9) and light crude oil (API= 32.95). The ferric oxide nano particle decreases the viscosity of oil sample B about 11.4%, averagely comparing with the viscosity of oil sample B without the nano. Also, the empirical results illustrate the variation of temperature from 50°C to 90°C for medium crude oil (Sample C). The experimental results show, the decreasing in viscosity values for nano and simple medium oil. The obtained results show the trend of viscosity for nano oil is severely than simple oil. The average decreasing in the viscosity values are measured as 12.9% comparing with the viscosity of simple oil. All of the obtained results show the nano particles can improve the heat transfer rate in the text of crude oil. So, the trends of all of the experimental graphs are decreasing.
Keywords
Heavy Hydrocarbons, Crude Oil, Temperature, Nano, Viscosity, Well
References
[01]
Storm D. A., McKeon R. J., McKinzie H. L., Redus C. L., Drag Reduction in Heavy Oil, J. Energy Resour. Technol. 1999; 121 (3): 145-148.
[02]
Wang Lidong, Wu Siyu, Liu Shuang, Cui Shuai, Liu Jie, Zhang Shihan, Cobalt impregnated porous catalyst promoting ammonium sulfate recovery in an ammonia-based desulfurization process, Chemical Engineering Journal, Volume 331, 1 January 2018, Pages 416-424.
[03]
Rached Ben-Mansour, Pervez Ahmed, Habib M. A., Simulation of Oxy-fuel combustion of heavy oil fuelin a model furnace, J. Energy Resour. Technol. 2015, 137: 032206.
[04]
Shadi WH, Mamdouh TG, Nabil E. Heavy crude oil viscosity reduction and rheology for pipeline transportation. Fuel 2010; 89: 1095–100.
[05]
Martnez-Palou R, Mosqueira ML, Zapata-Rendon B, Mar-Jugrez E, Bernal-Huicochea C, Clavel-Lopez J. C., Transportation of heavy and extra-heavy crude oil by pipeline: a review. J. Pet. Sci. Eng. 2011; 75: 274–82.
[06]
Elphingstone G. M., Greenhill K. L., Hsu J. J. C., Modeling of Multiphase Wax Deposition, J. Energy Resour. Technol. 1999; 121 (2), 81-85.
[07]
Weissman J. G. Review of processes for downhole catalytic upgrading of heavy crude oil. Fuel Proc. Technol. 1997; 50: 199–213.
[08]
Rana MS, Sلmano V, Ancheyta J, Diaz JAI. A review of recent advances on process technologies for upgrading of heavy oils and residua. Fuel 2007; 86: 1216–31.
[09]
Naseri A, Nikazar M, Mousavi DSA. A correlation approach for prediction of crude oil viscosities. J. Pet. Sci. Eng. 2005; 47: 163–74.
[10]
Hossain MS, Sarica C, Zhang HQ. Assessment and development of heavy-oil viscosity correlations. In: SPE International Thermal Operations and Heavy Oil Symposium, Kalgary, 1–3 November 2005. p. 1–9.
[11]
Liang-pei Hou Rong-xiang Zhao Xiu-ping Li Xiao-han Gao, Preparation of MoO2/g-C3N4 composites with a high surface area and its application in deep desulfurization from model oil, Applied Surface Science, Volume 434, 15 March 2018, Pages 1200-1209
[12]
Alomair O, Elsharkawy A, Alkandari H. Viscosity predictions of Kuwaiti heavy crudes at elevated temperatures. In: SPE Heavy Oil Conference and Exhibition, Kuwait, 12–14 December 2011. p. 1–18.
[13]
Yigit Ahmet S., Christoforou Andreas P., Stick-Slip and Bit-Bounce Interaction in oil-well Drillstrings, J. Energy Resour. Technol. 2006; 128 (4): 268-274.
[14]
Barrufet MA, Setiadarma A. Reliable heavy oil-solvent viscosity mixing rules for viscosities up to 450 K, oil-solvent viscosity ratios up to 4 _ 105, and any solvent proportion. Fluid Phase Equilib. 2003; 213: 65–79.
[15]
Luis F. Ayala, Doruk Alp, Evaluation of “Marching Algorithms” in the Analysis of Multiphase Flow in Natural Gas Pipelines, J. Energy Resour. Technol. 2008; 130 (4), 043003.
[16]
Fu Hailu, Jia Caiyun, Chen Qiaoshan, Cao Xueting, Zhang Xiaomin, Effect of particle size on the transformation kinetics of flue gas desulfurization gypsum to α-calcium sulfate hemihydrate under hydrothermal conditions, Particuology, Available online 1 February 2018, In Press, Corrected Proof.
[17]
Yilin Wang John, Well Completion for Effective Deliquification of Natural Gas wells, J. Energy Resour. Technol. 2011; 134 (1): 013102.
[18]
Chuan Lu, Huiqing Liu, Qiang Zheng, Qingbang Meng, Experimental Study of Reasonable Drawdown Pressure of Horizontal Wells in Oil Reservoir With Bottom Water, J. Energy Resour. Technol. 2014; 136 (3): 034502.
[19]
Junlai Wu; Yuetian Liu; Haining Yang, New Method of Productivity Equation for Multibranch Horizontal Well in Three-Dimensional Anisotropic Oil Reservoirs, J. Energy Resour. Technol. 2012; 134 (3): 032801-032801-5.
[20]
Anuj Gupta, Performance Optimization of Abrasive Fluid Jet for Completion and Stimulation of Oil and Gas Wells, J. Energy Resour. Technol. 2012; 134 (2): 021001.
[21]
Ji Haiyan, Sun Jia, Wu Peiwen, Wu Yingcheng, He Jing, Chao Yanhong, Zhu Wenshuai, Li Huaming, Silicotungstic acid immobilized on lamellar hexagonal boron nitride for oxidative desulfurization of fuel components, Fuel, Volume 213, 1 February 2018, Pages 12-21.
[22]
Lupianez C, Guedea I, Bolea I, Diez LI, Romeo LM. Experimental study of SO2 and NOx emissions in fluidized bed oxy-fuel combustion. Fuel Process Technol 2013; 106: 587–94.
[23]
de las Obras-Loscertales M, Rufas A, de Diego LF, García-Labiano F, Gayán P, Abad A, et al. Effects of temperature and flue gas recycle on the SO2 and NOX emissions in an oxy-fuel fluidized bed combustor. Energy Procedia 2013; 37: 1275–82.
[24]
Kaewboonsong W, Kuprianov VI, Chovichien N. Minimizing fuel and environmental costs for a variable-load power plant (co-)firing fuel oil and natural gas: Part 1. Modeling of gaseous emissions from boiler units. Fuel Process Technol 2006; 87: 1085–94.
[25]
Taheri-Shakib Jaber, Shekarifard Ali, Naderi Hassan, The influence of electromagnetic waves on the gas condensate characterisation: Experimental evaluation, Journal of Petroleum Science and Engineering, Volume 166, July 2018, Pages 568-576.