过程工程学报 ›› 2026, Vol. 26 ›› Issue (9): 1031-1041.DOI: 10.12034/j.issn.1009-606X.225304
李思阳(
), 朱玉洁, 陈瑜洲, 刘康, 肖朋(
), 孙长宇
收稿日期:2025-12-05
修回日期:2026-02-13
出版日期:2026-03-11
发布日期:2026-09-28
通讯作者:
肖朋 lisiyang15@163.com;xpmail@yeah.net
作者简介:李思阳,硕士研究生,化学工程与技术专业,E-mail: lisiyang15@163.com;基金资助:
Siyang LI(
), Yujie ZHU, Yuzhou CHEN, Kang LIU, Peng XIAO(
), Changyu SUN
Received:2025-12-05
Revised:2026-02-13
Online:2026-03-11
Published:2026-09-28
Contact:
Peng XIAO lisiyang15@163.com;xpmail@yeah.net
摘要:
降压开采是天然气水合物开采中最具前景的技术之一,但开采过程中水合物沉积层与井筒均面临水合物二次生成风险。本实验研究了分解水中气泡的产生、演变规律及对水合物再生成的影响。结果表明,水合物分解过程会伴随大量气泡生成;而未生成水合物的甲烷饱和水,经过同样的降压过程后并无气泡产生。分解压力较高时,分解水中气泡数量更多,且存在大量直径小于5 µm的微气泡。静置过程中,分解水中气泡发生聚并、尺寸增大,但总体数量较为稳定。气泡可为水合物生成提供成核位点和传质通道,对水合物再生有促进作用;在3 MPa分解条件下,水合物再生过程的水转化率较常压分解提升约12%。此外,再生成压力越高,体系达到平衡时的水转化率越高。水合物在气泡表面再次生成时,气泡逐渐发生凹陷变形,最终呈现半透明化状态,气泡内的气体完全转化为水合物。与纯水体系相比,在分解水中添加表面活性剂十二烷基硫酸钠(SDS),水合物的生成速率更快,且生成的水合物膜呈现出典型的蓬松多孔结构,这种结构减小了传质阻力。本研究结果证实,分解水中的微气泡是强化水合物再生成的重要因素,可为降压开采时水合物再生成行为的调控提供理论支撑。
中图分类号:
李思阳, 朱玉洁, 陈瑜洲, 刘康, 肖朋, 孙长宇. 分解水中气泡演变及其对水合物再生成的强化机理[J]. 过程工程学报, 2026, 26(9): 1031-1041.
Siyang LI, Yujie ZHU, Yuzhou CHEN, Kang LIU, Peng XIAO, Changyu SUN. Evolution of bubbles in dissociated water and their enhancement mechanism for hydrate reformation[J]. The Chinese Journal of Process Engineering, 2026, 26(9): 1031-1041.
| Runs | System | Dissociation pressure/MPa | Dissociation temperature/K |
|---|---|---|---|
| 1 | Pure water | 3.0 | 276.15 |
| 2 | Pure water | 1.5 | 276.15 |
| 3 | Pure water | 0.1 | 276.15 |
| 4 | 0.01wt% SDS solution | 3.0 | 276.15 |
表1 水合物分解实验条件
Table 1 Experimental conditions for hydrate dissociation
| Runs | System | Dissociation pressure/MPa | Dissociation temperature/K |
|---|---|---|---|
| 1 | Pure water | 3.0 | 276.15 |
| 2 | Pure water | 1.5 | 276.15 |
| 3 | Pure water | 0.1 | 276.15 |
| 4 | 0.01wt% SDS solution | 3.0 | 276.15 |
| Runs | System | Dissociation pressure/MPa | Dissociation temperature/K | Reformation pressure/MPa | Reformation temperature/K |
|---|---|---|---|---|---|
| 5 | Pure water | 3.0 | 276.15 | 4.0 | 273.15 |
| 6 | Pure water | 3.0 | 276.15 | 5.0 | 273.15 |
| 7 | Pure water | 3.0 | 276.15 | 7.3 | 273.15 |
| 8 | Pure water | 1.5 | 276.15 | 5.0 | 273.15 |
| 9 | Pure water | 0.1 | 276.15 | 5.0 | 273.15 |
| 10 | Pure water | - | - | 5.0 | 273.15 |
| 11 | 0.01wt% SDS solution | 3.0 | 276.15 | 5.0 | 273.15 |
| 12 | 0.005wt% SDS solution | 3.0 | 276.15 | 5.0 | 273.15 |
| 13 | 0.0025wt% SDS solution | 3.0 | 276.15 | 5.0 | 273.15 |
表2 水合物再生成实验条件
Table 2 Experimental conditions for hydrate reformation
| Runs | System | Dissociation pressure/MPa | Dissociation temperature/K | Reformation pressure/MPa | Reformation temperature/K |
|---|---|---|---|---|---|
| 5 | Pure water | 3.0 | 276.15 | 4.0 | 273.15 |
| 6 | Pure water | 3.0 | 276.15 | 5.0 | 273.15 |
| 7 | Pure water | 3.0 | 276.15 | 7.3 | 273.15 |
| 8 | Pure water | 1.5 | 276.15 | 5.0 | 273.15 |
| 9 | Pure water | 0.1 | 276.15 | 5.0 | 273.15 |
| 10 | Pure water | - | - | 5.0 | 273.15 |
| 11 | 0.01wt% SDS solution | 3.0 | 276.15 | 5.0 | 273.15 |
| 12 | 0.005wt% SDS solution | 3.0 | 276.15 | 5.0 | 273.15 |
| 13 | 0.0025wt% SDS solution | 3.0 | 276.15 | 5.0 | 273.15 |
图2 不同分解条件下液相中残留气泡的数量比较:(a) 分解压力3.0 MPa;(b) 分解压力1.5 MPa;(c) 分解压力0.1 MPa;(d) 甲烷饱和水溶液
Fig.2 Comparison of residual bubble population in the liquid phase under different dissociation conditions: (a) dissociation pressure of 3.0 MPa; (b) dissociation pressure of 1.5 MPa; (c) dissociation pressure of 0.1 MPa; (d) methane-saturated aqueous solution
图3 3.0 MPa分解压力下液相中不同位置的气泡在72 h前后的形态变化
Fig.3 Morphologies of bubbles at different locations in the liquid phase before and after 72 h under 3.0 MPa decomposition pressure
图5 高倍下不同分解压力分解水中的气泡形貌:(a) 3.0 MPa;(b) 0.1 MPa
Fig.5 Bubble morphologies in dissociated water under different dissociation pressures at high magnification: (a) 3.0 MPa; (b) 0.1 MPa
图6 纯水与SDS体系中残留气泡的数量对比:(a) 纯水;(b) SDS溶液
Fig.6 Comparison of the residual bubble population in pure water and SDS solution: (a) pure water; (b) SDS solution
图8 经不同压力分解后水合物再生成的形貌:(a) 3.0 MPa;(b) 0.1 MPa
Fig.8 Morphologies of hydrate reformation after hydrate dissociation under different pressures: (a) 3.0 MPa; (b) 0.1 MPa
图10 不同压力下再生成过程中水合物形貌随时间的变化过程:(a) 4.0 MPa;(b) 5.0 MPa;(c) 7.3 MPa
Fig.10 Changes in hydrate morphology with time during the reformation process at various pressures: (a) 4.0 MPa; (b) 5.0 MPa; (c) 7.3 MPa
图11 7.3 MPa下再生成过程中水合物的共聚焦显微图像及对应的拉曼谱图随时间的变化:(a) 30 min;(b) 1 h;(c) 2.5 h;(d) 5.3 h
Fig.11 Changes in confocal microscopic images and the corresponding Raman spectra of hydrates with time during reformation at 7.3 MPa: (a) 30 min; (b) 1 h; (c) 2.5 h; (d) 5.3 h
图13 不同浓度SDS溶液体系下水合物再生成过程中的形貌随时间的变化过程:(a) 0.0025wt% SDS溶液;(b) 0.005wt% SDS溶液;(c) 0.01wt% SDS溶液
Fig.13 Changes in hydrate morphology during the reformation process in SDS solutions: (a) 0.0025wt% SDS solution; (b) 0.005wt% SDS solution; (c) 0.01wt% SDS solution
图14 0.01wt% SDS溶液再生成过程中水合物的共聚焦显微图像及对应的拉曼谱图随时间的变化:(a) 5 min; (b) 2.2 h; (c) 5.2 h; (d) 25.3 h
Fig.14 Changes in confocal microscopic images and the corresponding Raman spectra of hydrates with time during reformation in 0.01wt% SDS solution: (a) 5 min; (b) 2.2 h; (c) 5.2 h; (d) 25.3 h
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