Modelling facility for field-average formation pressure p(t) at any time moment t as response to production flowrates history:
(1) | A_e \, h_e \int_{p_i}^p \phi_e(p) \, c_t(p) \, dp = \Delta Q (t) = Q^{\downarrow}_t(t) - Q^{\uparrow}_t(t) + Q^{\downarrow}_{GC}(t) + Q^{\downarrow}_{AQ}(t) |
where
p_i = p(0) | \Delta Q (t) | full-field cumulative reservoir fluid balance | |
A_e | Q^{\uparrow}_t(t) | full-field cumulative offtakes by the time moment t | |
h_e | effective formation thickness averaged over drainage area | Q^{\downarrow}_t(t) | full-field cumulative intakes by the time moment t |
\phi_e(p) | effective porosity as function of formation pressure p(t) | Q^{\downarrow}_{GC}(t) | cumulative gas influx from Gas Cap Expansion |
c_t(p) | total compressibility as function of formation pressure p(t) | Q^{\downarrow}_{AQ}(t) | cumulative water influx from Aquifer Expansion |
The MatBal equation (1) is often complemented by constant PI model of Bottom-Hole Pressure ( p^{\uparrow}_{wf}(t) for producers and p^{\downarrow}_{wf}(t) for injectors):
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where | where | ||||||
p^{\uparrow}_{wf, \, k}(t) | p^{\downarrow}_{wf, \, j}(t) | ||||||
Q^{\uparrow}_k(t) | cumulative offtakes from k-th producer by the time moment t | Q^{\downarrow}_j(t) | cumulative intakes to j-th injector by the time moment t | ||||
J^{\uparrow}_k | productivity index of k-th producer | J^{\downarrow}_j | injectivity Index of j-th injector |
In practice there is no way to measure the external influx Q^{\downarrow}_{GC}(t) and Q^{\downarrow}_{AQ}(t) so that one need to model them and calibrate model parameters to fit available data on production flowrates history and formation pressure data records.
There is a list of various analytical Aquifer Drive and Gas Cap Drive models which are normally related to pressure dynamics p(t):
Gas Cap Drive @model | Aquifer Drive @model | ||||
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which closes equation (1) for the pressure p(t).
Variations
In some specific cases equation (1) can be explicitly integrated:
Low pressure dry gas | |||||
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\{ \phi_e = {\rm const}, \ c_t = {\rm const} \} | c_t = c_r + \frac{1}{p} \sim \frac{1}{p} | ||||
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where
V_e = A_e \, h_e \, \phi_e | drainage volume |
See Also
Petroleum Industry / Upstream / Production / Subsurface Production / Field Study & Modelling / Production Analysis / Flowing Material Balance Analysis (FMB)
[ Material Balance Pressure Plot ][ Material Balance Pressure @model ]