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Investigation of the Effect of Temperature and Grain Size on the Kinetic of Hydrochloric Acid and Calcium Carbonate Reaction as a Simulation of Wellbore Acidizing | ||
| Journal of Chemical and Petroleum Engineering | ||
| دوره 57، شماره 2، اسفند 2023، صفحه 391-399 اصل مقاله (658.15 K) | ||
| نوع مقاله: Research Paper | ||
| شناسه دیجیتال (DOI): 10.22059/jchpe.2023.357815.1429 | ||
| نویسندگان | ||
| Kaveh Paydar1؛ Ali Ebadi2؛ Amin Ahmadi1؛ Mehrdad Manteghian* 1 | ||
| 1Department of Petroleum Engineering, Faculty of Chemical Engineering, Tarbiat Modares University of Tehran, Iran. | ||
| 2Department of Chemical Engineering, Faculty of Chemical Engineering, Tarbiat Modares University of Tehran, Tehran, Iran. | ||
| چکیده | ||
| In this study, the significance of temperature within the range of 25 to 70 degrees Celsius and the particle size of calcium carbonate at 237 μm, 348.5 μm, and 497.5 μm on the hydrochloric acid reaction rate with calcium carbonate stone was deliberated. The slow reaction rate helps a retarded action, and therefore, HCl penetrates deeper, and the zones farther from the wellbore will be affected by the acidizing. Therefore, the exploration of variables influencing the reaction rate holds considerable significance. The reaction rate is controlled by influential factors such as temperature and particle size, where the effect of these two factors is discussed in detail. According to the empirical findings, the reaction rate exhibits an upward trend as temperature rises and as the size of calcium carbonate particles decreases. It is worth mentioning that the highest and lowest reaction rates were observed at temperatures of 70 and 25 degrees Celsius, and with calcium carbonate particle sizes of 237 and 497.5 micrometers, respectively. Consequently, this research, considering the examined parameters and the obtained results, contributes to a better understanding and more efficient design of the acidizing process. | ||
| کلیدواژهها | ||
| Acidizing؛ Stimulation؛ HCl؛ Calcium Carbonate؛ Grain Size | ||
| مراجع | ||
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[1] Ali M, Ziauddin M. Carbonate acidizing: a mechanistic model for wormhole growth in linear and radial flow. Journal of Petroleum Science and Engineering. 2020;186:106776. https://doi.org/10.1016/j.petrol.2019.10677 [2] Assem A, Kumar H, Nasr-El-Din H, De Wolf C. Location and magnitude of formation damage due to iron precipitation during acidizing carbonate rocks. Journal of Petroleum Science and Engineering. 2019;179:337-54. https://doi.org/10.1016/j.petrol.2019.04.073 [3] Karimi M, Shirazi MM, Ayatollahi S. Investigating the effects of rock and fluid properties in Iranian carbonate matrix acidizing during pre-flush stage. Journal of Petroleum Science and Engineering. 2018;166:121-30. https://doi.org/10.1016/j.petrol.2018.03.002 [4] Ahmadi A, Paydar K, Ebadi A, Manteghian M. Study and Optimization of the Effect of Temperature, Acid Concentration, and Rock Grain Size on the pH of Carbonate Reservoir Acidizing. Journal of Chemical and Petroleum Engineering. 2022;56(2):331-9. https://doi.org/10.22059/jchpe.2022.342154.1391 [5] Economides MJ, Nolte KG. Reservoir stimulation: Prentice Hall Englewood Cliffs, NJ; 1989. [6] Da Motta EP, Hill A, Sepehrnoori K. Selective matrix acidizing of horizontal wells. SPE Production & Facilities. 1995;10(03):157-64. https://doi.org/10.2118/27399-PA [7] Kalfayan L. Production enhancement with acid stimulation: Pennwell Books; 2008. [8] Medeiros Jr F, Trevisan O. Thermal analysis in matrix acidization. Journal of Petroleum Science and Engineering. 2006;51(1-2):85-96. https://doi.org/10.1016/j.petrol.2005.11.011 [9] Lyons J, Nasrabadi H, Nasr-El-Din HA. A novel pore-scale thermal-fracture-acidizing model with heterogeneous rock properties. SPE Journal. 2016;21(01):280-92. https://doi.org/10.2118/167158-PA [10] Chang FF, Nasr-El-Din HA, Lindvig T, Qui X, editors. Matrix acidizing of carbonate reservoirs using organic acids and mixture of HCl and organic acids. SPE Annual Technical Conference and Exhibition; 2008: OnePetro. [11] Schembre J, Kovscek A. Mechanism of formation damage at elevated temperature. 2005. https://doi.org/10.1115/1.1924398 [12] Yoo H, Kim Y, Lee W, Lee J. An experimental study on acid-rock reaction kinetics using dolomite in carbonate acidizing. Journal of Petroleum Science and Engineering. 2018;168:478-94. https://doi.org/10.1016/j.petrol.2018.05.041 [13] Bazin B, Roque C, Bouteca M. A Laboratory Evaluation of Acid Propagation in Relation to Acid Fracturing: Results and Interpretation. SPE European Formation Damage Conference and Exhibition. 1995:SPE-30085-MS. https://doi.org/10.2118/30085-MS [14] Taylor K, Al-Ghamdi A, Nasr-El-Din H. Measurement of acid reaction rates of a deep dolomitic gas reservoir. Journal of Canadian Petroleum Technology. 2004;43(10). https://doi.org/10.2118/04-10-05 [15] Kalia N, Glasbergen G. Fluid temperature as a design parameter in carbonate matrix acidizing. SPE International Production and Operations Conference and Exhibition. 2010:SPE-135654-MS. https://doi.org/10.2118/135654-MS [16] Young PR. Dilution of Concentrated Solutions. University of Illinois at Chicago 2020. https://chem.libretexts.org/@go/page/79575 [17] Udonne JD, Folami N, Patinvoh R. TREATMENT OF INDUSTRIAL WASTE EFFLUENT USING TREATED BAGASSE. International Journal of Scientific & Engineering Research. 2016;7(3):389-97 | ||
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