This
study explored the fully coupled thermo-hydro-chemical response
of natural gas hydrate (NGH) recovery, where the factors considered
are that the hydrate decomposes from solid to methane and water, two-phase
flow, and heat transfer. The fully coupled numerical model developed
was verified by matching the data of gas production and temperature
that are collected from Masuda’s experiment and then applied
to simulate the NGH field trial. The simulation result showed that
both the model (H2–C) ignoring heat transfer and
the model (H1–C) ignoring two-phase flow overestimated
the production of NGH, and there were obvious interfaces in evolution
curves of reservoir properties. Sensitivity analysis showed that the
peak gas production rate and cumulative gas production increased with
the increase of the production pressure difference, initial absolute
permeability, and phase equilibrium parameter e
1 and decreased along with the increasing of the initial water
saturation. The hydrate phase equilibrium conditions and the wellhole
pressure enhanced the decomposition rate of the hydrate by changing
the difference between equilibrium pressure and reservoir pressure.
The initial absolute permeability and water saturation affected the
hydrate depressurization by changing the gas flow capacity in the
reservoir. Therefore, the gas production will be effective in the
future NGH commercial exploitation if the proper enhancement of pressure
difference and that of the gas flow capacity can be combined.