研究领域
油气藏流体的高压物性及相态模型
油气藏数值模拟
深水流动保障
科研项目
[1] 中国石油大学（北京）引进人才科研启动基金，油气水系统高温高压相平衡实验及PVT相态模型开发，2015.11-2018.12，负责(Science Foundation of China University of Petroleum, Beijing (Grant No.2462015YJRC028), Experimental Investigation and Model Development of the Phase Behavior in CO2-Hydrocarbon-Brine System Under Reservoir Pressures and Temperatures, PI: H. Zhao)
[2] 国家自然科学基金青年基金，CO2-烃-水体系多相平衡和相稳定性研究：揭示水和CO2对油气烃类体系相态的影响规律，2017.1-2019.12，负责(National Science Foundation for Young Scientists of China (Grant No. 51604284), Multiphase Equilibrium Modeling and Stability Analysis for the CO2-Hydrocarbon-H2O System: The Effects of Water and Carbon Dioxide on Phase Behavior of Hydrocarbon System, PI: H. Zhao)
[3] 中国石油化工股份有限公司华东油气分公司，黄桥高含CO2油田产出液处理工艺技术，2016.5-2016.12，参与(SINOPEC East China Oil & Gas Co., Ltd. (Contract No. 34600297-16-ZC0607-0001), Huangqiao Oilfield High CO2 Content Wellstream Processing Technology, Participant)
代表性研究成果
[1] Zhao, H., Fedkin, M., Dilmore, R. and Lvov, S. N. Carbon dioxide solubility in aqueous solutions of sodium chloride at geological conditions: Experimental results at 323.15, 373.15, 423.15K and 150 bar and modeling up to 573.15K and 2000 bar, Geochimica et Cosmochimica Acta, 2015, 149, 165-189. http://dx.doi.org/10.1016/j.gca.2014.11.004
[2] Zhao, H., Dilmore, R. D., Allen, E., Hedges, S. W., Soong, Y. and Lvov, S. N. Measurement and modeling of CO2 solubility in natural and synthetic formation brines for CO2 sequestration, Environmental Science & Technology, 2015, 49, 1972-1980. http://dx.doi.org/10.1021/es505550a
[3] Zhao, H., Dilmore, R. and Lvov, S. N. Experimental studies and modeling of CO2 solubility in high temperature aqueous CaCl2, MgCl2, Na2SO4, and KCl solutions, AIChE Journal, 2015, 61, 2286-2297.http://dx.doi.org/10.1002/aic.14825
[4] Zhao, H. and Lvov, S. N. Phase behavior of the CO2–H2O system at temperatures of 273–623 K and pressures of 0.1–200 MPa using Peng-Robinson-Stryjek-Vera equation of state with a modified Wong-Sandler mixing rule: An extension to the CO2–CH4–H2O system, Fluid Phase Equilibria, 2016, 417, 96-108. http://dx.doi.org/10.1016/j.fluid.2016.02.027
[5] Zhao, H. Modeling vapor-liquid phase equilibria of methane-water and methane-carbon dioxide-water systems at 274K to 573K and 0.1 to 150 MPa using PRSV equation of state and Wong-Sandler mixing rule, Fluid Phase Equilibria, 2017, 447, 12-26. http://dx.doi.org/10.1016/j.fluid.2017.05.015
[6] Sengupta, A., Beck, J., Zhao, H., Schatz, R.S., Ziomek-Moroz, M. and Lvov, S.N. Corrosion Behavior of 13Cr Casing in Cement Synthetic Pore Solution, ECS Transactions, 2015, 66(17), 37-50.227th ECS Meeting, 24-28 May 2015, Chicago, Illinois, USA. http://dx.doi.org/10.1149/06617.0037ecst
[7] Zhao, H. Flash Calculation and Phase Stability Analysis of Reservoir Gas-Water System—Implication for Extracting Dissolved CH4 by CO2 Injection. SPE Annual Technical Conference and Exhibition, Dubai, UAE, 26–28 September 2016 (SPE 181349 Full Presentation) http://dx.doi.org/10.2118/181349-MS
Publications
[1] 吴木旺，梁豪，崔书姮，赵海宁*，熊秋昊. 高温高压天然气PVT物性计算模型对比研究. 石油钻采工艺，2022，已录用.
[2] 任魁杰, 孟良, 赵海宁, 王博弘, 王博弘, 鲁岑, 梁永图*. 黄桥高含CO2气田产出液单井集输工艺, 油气储运, 2020, 39(6): 650-661.
[3] 宋传真*, 赵海宁, 张慧. 氮气对塔河油田原油轻质组分抽提作用实验与评价, 石油学报，2021, 42(3), 341-349.
[4] Zhao, H.*, Song, C., Zhang, H., Di, C., Tian, Z. Improved fluid characterization and phase behavior approaches for gas flooding and application on Tahe light crude oil system, Journal of Petroleum Science and Engineering, 2022, 208: 109653.
[5] Zhao, H.*, Jing, H., Fang, Z., and Yu. H. Flash calculation using successive substitution accelerated by GDEM in reduced-variable space: comparison and new insights. SPE Journal, 2020. 25(06): 3332-3348. SPE-202472-PA.
[6] Zhao, H.*, Fang, Z. Improved multiple-mixing-cell method for accelerating minimum miscibility pressure calculations. SPE Journal. 2020, 25(04): 1681-1696. SPE-199360-PA.