利用冰冻石英砂模拟冻土水合物的赋存条件,研究了压力对二氧化碳水合物生成特性的影响,在300 mL高压水合物反应釜中于271 K下进行了多组CO2液化压力以上及以下的霰状冰粉包裹的石英砂中水合物生成实验。结果表明,充入的CO2未液化时,初始压力越大,水合反应速率越快,压力越早达稳定状态;充入压力达液化压力后,注入的CO2越多,水合反应速率越快。压力作为水合反应的驱动力,压力越高水合物生成越多,冰的最终转化率越高。采用CO2置换冻土区中甲烷水合物时,控制压力低于液化压力或注入过量的CO2,置换效果更好。
The permafrost region contains a large amount of natural gas hydrate resources. Carbon dioxide replaces methane to recover gas hydrates in the frozen soil, can not only obtain a large amount of natural gas resources, but also can save carbon dioxide gas and reduce the greenhouse effect caused by carbon dioxide emissions. It is a very promising gas hydrate extraction methods. At present, there are few studies on the carbon dioxide replacement of natural gas hydrates by methane production in the permafrost region, and the formation and decomposition characteristics of methane hydrate and carbon dioxide hydrate in the permafrost region have not yet been revealed. In this work, the occurrence condition of frozen quartz sands sleet shape to simulate permafrost gas hydrate, experimental study on effect of stress on carbon dioxide hydrate formation characteristics, several experimental groups were carried out respectively in 271 K, which the generated pressure of carbon dioxide above or below liquefaction pressure in 300 mL high pressure hydration reactor. The results showed that carbon dioxide below freezing temperatures in quartz sand pressure without liquefaction, the higher the initial pressure, the faster the hydration reaction rate and the earlier the pressure will reach the stable state. But above liquefaction pressure, the more the amount of carbon dioxide was filled, the faster the hydration reaction rate was. From the overall trend, the pressure acted as a driving force of the hydration reaction. The higher the pressure, the more formation of carbon dioxide hydrate was, and the higher the final conversion rate was. Therefore, when carbon dioxide was used to replace methane hydrate in the permafrost region, it was necessary to control the pressure below the liquefaction pressure or to inject excess carbon dioxide, and the final conversion rate will increase dramatically.
[1]Makogon Y F, Holditch S A, Makogon T Y.Natural gas-hydrates—A potential energy source for the 21st Century[J].Journal of Petroleum Science & Engineering, 2007, 56(1):14-31
[2]张光学, 梁金强, 陆敬安, 等.南海东北部陆坡天然气水合物藏特征[J].天然气工业, 2014, 34(11):1-10
[3]徐学祖, 程国栋, 俞祁浩.青藏高原多年冻土区天然气水合物的研究前景和建议[J].地球科学进展, 1999, 14(2):201-204
[4]王平康, 祝有海, 卢振权, 等.祁连山冻土区天然气水合物岩性和分布特征[J].地质通报, 2011, 30(12):1839-1850
[5]王进寿, 郑有业, 黄朝晖, 等.陆域天然气水合物形成条件理论研究及其对青南多年冻土区水合物勘查的启示[J].地质科技情报, 2016, 4(05):139-147
[6]Kurihara M, Sato A, Ouchi H, et al.Prediction of Gas Productivity From Eastern Nankai Trough Methane Hydrate Reservoirs[J].Spe Reservoir Evaluation & Engineering, 2009, 12(3):477-499
[7]张旭辉, 鲁晓兵, 刘乐乐.天然气水合物开采方法研究进展[J].地球物理学进展, 2014, 29(2):858-869
[8] Sloan ED, Koh CA.Estimation techniques for phase equilibria of natural gas hydrates [C]. Proceedings of 3rd International Conference on Natural Gas Hydrates: New York, USA, 2008: 320–523.
[9]Zhao J, Xu K, Song Y, et al.A Review on Research on Replacement of CH4 in Natural Gas Hydrates by Use of CO2[J].Energies, 2012, 5(2):399-419
[10]徐纯刚, 李小森, 蔡晶, 等.二氧化碳置换法模拟开采天然气水合物的研究进展[J].化工学报, 2013, 64(7):2309-2315
[11]Ota M, Abe Y, Watanabe M, et al.Methane recovery from methane hydrate using pressurized CO2[J].Fluid Phase Equilibria, 2005, s228–229(3):553-559
[12]李遵照, 郭绪强, 陈光进, 等.置换水合物中的实验和动力学[J].化工学报, 2007, 58(5):1197-1203
[13]张学民, 李金平, 吴青柏, 等.置换天然气水合物中的研究进展[J].过程工程学报, 2014, 14(4):715-720
[14]宋光春, 李玉星, 王武昌.温度和压力对置换甲烷水合物的影响[J].油气储运, 2016, 35(3):295-301
[15]Deusner C, Bigalke N, Kossel E, et al.Methane Production from Gas Hydrate Deposits through Injection of Supercritical CO2[J].Energies, 2012, 5(7):2112-2140
[16] 陈云飞.冻土区天然气水合物沉积物强度特性研究[D]. 大连理工大学, 2014.
[17] 陈晓庆.置换结合降压法开采天然气水合物的实验研究[D]. 大连理工大学, 2015.
[18]张郁, 李小森, 陈朝阳, 等.冰点下多孔介质中甲烷水合物的生成特性[J].现代地质, 2016, 30(04):922-928
[19]Zhang X, Li J, Wu Q, Wang C, Nan J.Experimental Study on the Formation Characteristic of CO2 Hydrate in Porous Media below the Freezing Point[J].Journal of China Petroleum Processing & Petrochemical Technology, 2015, 17(3):32-38
[20]Robinson D B.A New Two-Constant Equation of State[J].Industrial & Engineering Chemistry Fundamentals, 1976, 15(1):92-94
[21] 陈钟秀, 顾飞燕, 胡望月.化工热力学 [M]. 北京: 化学工业出版社, 2012
[22]M.J. Hwang, D.A. Wright, A Kapur, G.D. Holder.An experimental study of crystallization and crystal growth of methane hydrates from melting ice[J]. Journal of Inclusion Phenomena& Molecular Recognition in Chemistry, 1990, 8:103-116.[J].Journal of Inclusion Phenomena& Molecular Recognition in Chemistry, 1990, 8(1):103-116
[23]Sloan E D, Fleyfel F.A molecular mechanism for gas hydrate nucleation from ice[J].AIChE Journal, 1991, 37(9):1281-1292