Characterizing methane hydrate formation in the non-Newtonian fluid flowing system

被引:36
作者
Fu, Weiqi [1 ]
Wang, Zhiyuan [3 ]
Duan, Wenguang [1 ,2 ]
Zhang, Zhennan [3 ]
Zhang, Jianbo [1 ]
Sun, Baojiang [1 ]
机构
[1] China Univ Petr East China, Sch Petr Engn, Qingdao 266580, Shandong, Peoples R China
[2] CNPC XiBu Drilling Engn Co Ltd, Urumqi 830000, Peoples R China
[3] China Univ Petr East China, Inst Offshore Oil & Gas & Hydrate Res, Qingdao 266580, Shandong, Peoples R China
关键词
Gas hydrate development; Hydrate formation; Mass transfer; non-Newtonian fluid; Rheology; GAS-DOMINATED SYSTEMS; LIQUID MASS-TRANSFER; NATURAL-GAS; SHELL-MODEL; THEORETICAL PREDICTION; TURBULENT-FLOW; POROUS-MEDIA; KINETICS; DISSOCIATION; DEPOSITION;
D O I
10.1016/j.fuel.2019.05.052
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Developing natural gas hydrates in deep water faces serious well control problem and flow assurance problem, induced by the reformation of gas hydrate in the drilling fluid. In order to solve this problem, developing a hydrate formation predicting model becomes necessary. In this work, the methane hydrate formation experiments are performed in the xanthan gum (XG) aqueous solution under flow velocities from 1.8 to 1.5 m/s, XG concentrations from 0.1 to 0.3% and void fraction of 4.5%. The hydrate formation rates decrease with the XG concentration increasing and increases with the flow velocity increasing. The hydrate formation rate at the moment of the experiment onset will decrease sharply due to the formation of hydrate shell on gas bubbles and gas hydrates will form at the almost constant rate, because the second growth of hydrate shells on the fractures of gas bubbles and collisions between gas bubbles enhances the hydrate formation rates. The hydrate formation rate increases rapidly when the hydrate formation process is near the end of hydrate formation since the breakage rates of gas bubbles increase the hydrate formation rates. A mass transfer model is developed to describe the methane hydrate formation under the non-Newtonian fluid flowing condition. Since the volumetric mass transfer coefficient closely depends on the rheological properties of carrying fluid, the rheological experiments for the XG aqueous solution are conducted and an empirical rheology model is developed correspondingly. An integrated constant is proposed to improve the accuracy of the model which reflects influences of the hydrate shell formation, the second growth of hydrate shell and the bubble breakage on methane hydrate formation. The correlations of the integrated constant are functions of the XG concentration, the flow velocity and the subcooling temperature. Through validation, the proposed mass transfer model shows good agreements with experimental data and the maximum discrepancy is 11.64%.
引用
收藏
页码:474 / 487
页数:14
相关论文
共 55 条
[1]   Production of natural gas from methane hydrate by a constant downhole pressure well [J].
Ahmadi, Goodarz ;
Ji, Chuang ;
Smith, Duane H. .
ENERGY CONVERSION AND MANAGEMENT, 2007, 48 (07) :2053-2068
[2]   FORMATION OF HYDRATES DURING DEEP-WATER DRILLING OPERATIONS [J].
BARKER, JW ;
GOMEZ, RK .
JOURNAL OF PETROLEUM TECHNOLOGY, 1989, 41 (03) :297-301
[3]  
Boxall J.A., 2008, INT C GAS HYDR ICG H
[4]   Insights into methane hydrate formation, agglomeration, and dissociation in water plus diesel oil dispersed system [J].
Chen, Jun ;
Liu, Jun ;
Chen, Guangqin ;
Sun, Chang-Yu ;
Jia, Meng-Lei ;
Liu, Bei ;
Si, Si ;
Ren, Ning .
ENERGY CONVERSION AND MANAGEMENT, 2014, 86 :886-891
[5]   Methane Hydrate Formation and Dissociation on Suspended Gas Bubbles in Water [J].
Chen, Litao ;
Sloan, E. Dendy ;
Koh, Carolyn A. ;
Sum, Amadeu K. .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2014, 59 (04) :1045-1051
[6]  
[陈玉川 Chen Yuchuan], 2018, [化工进展, Chemical Industry and Engineering Progress], V37, P1726
[7]   Natural gas hydrate formation and inhibition in gas/crude oil/aqueous systems [J].
Daraboina, Nagu ;
Pachitsas, Stylianos ;
von Solms, Nicolas .
FUEL, 2015, 148 :186-190
[8]   Methane hydrates as potential energy resource: Part 1-Importance, resource and recovery facilities [J].
Demirbas, Ayhan .
ENERGY CONVERSION AND MANAGEMENT, 2010, 51 (07) :1547-1561
[9]  
Deng Z, 2016, CHEM ENG J, V160, P729
[10]   Underinhibited Hydrate Formation and Transport Investigated Using a Single-Pass Gas-Dominant Flow loop [J].
Di Lorenzo, Mauricio ;
Aman, Zachary M. ;
Kozielski, Karen ;
Norris, Bruce W. E. ;
Johns, Michael L. ;
May, Eric F. .
ENERGY & FUELS, 2014, 28 (11) :7274-7284