座舱增压
计算机模拟
水合物
天然气
叠加原理
离解(化学)
笼状水合物
环境科学
机械
体积热力学
生产效率
化学
石油工程
生产(经济)
材料科学
再分配(选举)
高压
逸度
不稳定性
地质学
流量(数学)
消散
化学物理
控制音量
作者
Xinglong Gao,Zhitao Wang,Shuhua Lin,Zheyuan Liu,Ni Liu,Yingming Xie,Binlin Dou,Liang Yang
出处
期刊:Energy & Fuels
[American Chemical Society]
日期:2026-09-09
卷期号:40 (37): 20470-20482
标识
DOI:10.1021/acs.energyfuels.6c02785
摘要
Abstract Well layout configuration is critical for gas hydrate production as it dictates pressure spreads and dissociation front propagation. This study conducted numerical simulations for single-well, two-well, and several multi-well layouts. Gas production rate, water production rate, and volume ratio of gas to water were calculated to describe production behavior based on the geological conditions of the SH7 site in the Shenhu Area, northern South China Sea, to investigate multi-well development dynamics. A synergistic effect coefficient (Sec) was introduced to quantify the production enhancement per well in multi-well systems. Results demonstrate that while increasing well count enhances total recovery, the gains are inherently nonproportional, revealing a distinct synergistic effect limitation. Well layout and spacing significantly control performance; specifically, the ring layout and larger well spacing outperforms others by establishing a more homogenized pressure distribution. Mechanistic analysis reveals that while inter-well pressure superposition expands the effective dissociation region, the increasing competition among flow pathways and phase redistribution progressively constrain further enhancement. These coupled processes govern the nonproportional evolution of synergistic effects. These findings provide a mechanistic basis for optimizing well spacing and architecture in large-scale hydrate commercialization.
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