| G 1 | thermal gradient within the frozen layer (°C/m) |
| G 2 | thermal gradient below the frozen layer (°C/m) |
| H | permafrost thickness (m) |
| k | intrinsic permeability (m2) |
| k rA | aqueous relative permeability (m2) |
| k rG | gas relative permeability (m2) |
| k ΘC | thermal conductivity (W/(m·K)) |
| k ΘRD | thermal conductivity of dry porous medium (W/(m·K)) |
| k ΘRW | thermal conductivity of fully saturated porous medium (W(m·K)) |
| k ΘI | thermal conductivity of ice (W/(m·K)) |
| M W | cumulative mass of produced water (kg) |
| P | pressure (Pa) |
| P B | initial pressure at base of HBL (Pa) |
| P W | pressure at the well (Pa) |
| Q | total amount of injected heat (J) |
| q | heat injection rate (W/m of well) |
| Q P | gas production rate (ST m3/day/m of well) |
| Q W | water production rate (kg/day/m of well) |
| r | radius (m) |
| r W | wellbore radius (m) |
| R GW | gas-to-water ratio (ST m3 of CH4/m3 of H2O) |
| S | phase saturation |
| t | time (days) |
| T | temperature (°C) |
| T 0 | permafrost ground temperature (°C) |
| T B | initial temperature at the base of HBL (°C) |
| V P | cumulative volume of produced CH4 (ST m3) |
| W | pump work (J) |
| x,y,z | cartesian coordinates (m) |
| ΔHC | combustion enthalpy of produced methane (J) |
| ΔlI-P | horizontal distance between injector and producer (m) |
| ΔlP-P | vertical distance between two producers (m) |
| Φ | porosity |
| η | energy ratio |
| χ | hydrate dissociation percentage |
| λ | van Genuchten exponent—Table 1 |
| Subscripts and Superscripts | |
| 0 | denotes initial state |
| A | aqueous phase |
| B | base of HBL |
| cap | capillary |
| G | gas phase |
| H | solid hydrate phase |
| I | solid ice phase |
| irA | irreducible aqueous phase |
| irG | irreducible gas |
| n | permeability reduction exponent—Table 1 |
| n G | gas permeability reduction exponent—Table 1 |
| W | well |