p_e \ (t) = p_{nr} \ (0) + \gamma_n^{-1} \cdot  \sum_m \left(  Q^{\uparrow}_{nm} +  Q^{\downarrow}_{nm} \ \right)
p_{{\rm wf}, n} \ \ \ (t) = p_e \ (t) + J_n^{-1}  \cdot  q_n(t)
Q^{\uparrow}_{nm} \ =  

\ - \ f^{\uparrow}_{O,nm} \ \cdot B_{ob} \cdot  \, Q^{\uparrow}_O   

\ - \ f^{\uparrow}_{G,nm} \ \cdot B_{go} \cdot Q^{\uparrow}_G 

\ - \ f^{\uparrow}_{W,nm} \ \cdot B_w \cdot Q^{\uparrow}_W 

Q^{\downarrow}_{nm} \ = 

f^{\downarrow}_{G,nm} \ \cdot B_{go} \cdot Q^{\downarrow}_G 

\ + \ f^{\downarrow}_{W,nm} \ \cdot B_w \cdot Q^{\downarrow}_W

\ + \ B_{go} \cdot Q^{\downarrow}_{GCAP} \    

\ + \ B_w \cdot Q^{\downarrow}_{WAQ} 
Q_m(t) =  \int_0^t q_m(t) \, dt
B_{og} = \frac{B_o - R_s \, B_g}{1- R_s \, R_v}
B_{go} = \frac{ B_g - R_v \, B_o}{1- R_s \, R_v}

The value of  can be linked to drainable volume  as:

\gamma_n = c_{t,n} \cdot V_{\phi, n} = (c_r + s_{w,n} \cdot c_w + s_{o,n} \cdot c_o + s_{g,n} \cdot c_g) \cdot  \phi_n \cdot V_n
s_{w,n} + s_{o,n} + s_{g,n} = 1

In case of Water Injector .

In case of Gas Injector: .


The objective function is:

E[ \ \tau_n, \gamma_n, f_{nm} \ ] = \sum_k \sum_n \left[ {\rm w}_e \cdot \left( p_{e,n} \ \ (t_k) - \tilde p_{e,n} \ \ (t_k) \right)^2  

+ {\rm w}_{\rm wf} \ \ \cdot \left( p_{{\rm wf},n} \ \ (t_k) - \tilde p_{{\rm wf},n} \ \ (t_k) \right)^2  \right]   \rightarrow \min 


The constraints are:

J_n \geq  0 ,  \quad \gamma_n \geq 0,  \quad f_{nm} \ \geq  0 , \quad \sum_m f^{\uparrow}_{O, nm} \ \leq 1 , \quad \sum_m f^{\uparrow}_{G, nm} \ \leq 1, \quad \sum_m f^{\downarrow}_{W, nm} \ \leq 1, \quad \sum_m f^{\downarrow}_{G, nm} \ \leq 1


In regular case , the initial formation pressure at datum is the same for all wells: 


See Also


Petroleum Industry / Upstream /  Production / Subsurface Production / Field Study & Modelling / Production Analysis / Capacitance Resistance Model (CRM) / Capacitance-Resistivity Model (CRM) @model

Production – Injection Pairing @ model

[ Slightly compressible Material Balance Pressure @model ]