PNG 301
Introduction to Petroleum and Natural Gas Engineering

5.4.1.2: Stabilized Flow of Gas to a Vertical Production Well in Terms of Pressure-Squared

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To develop the inflow performance relationship in terms of pressure, we assumed that the group, p μ g  Z , was relatively constant in the pressure range of interest, and we removed the entire group from the pressure integral in Equation 5.10. In the pressure-squared formulation, we assume that the product μ g  Z is relatively constant with pressure and remove it from Equation 5.10, leaving:

r w r e 1 r dr= 0.001127( 2π )( 5.615 ) T SC   k g   h q g   T r   p SC   μ g   Z p wf p e p dp
Equation 5.16

Again, we will see that the μ g  Z product can be safely assumed to be relatively constant over a particular pressure range. Performing both integrations in Equation 5.16 results in:

[ lo g e ( r ) ] r w r e = 0.001127( 2π )( 5.615 ) T SC   k g   h q g   T r   p SC   μ g   Z [ p 2 2 ] p wf p e
Equation 5.17

Rearranging Equation 5.17 results in:

q g = 0.001127( 2π )( 5.615 ) T SC   k g   h 2   T r   p SC   μ g   Z ( p e 2 p wf 2 ) log e ( r e r w )
Equation 5.18a

or,

q g = 0.01988   T SC   k g   h T r   p SC   μ g   Z ( p e 2 p wf 2 ) log e ( r e r w )
Equation 5.18b

or, after substituting the normal U.S. definitions of p SC and T SC :

q g = 0.70325   k g   h T r   μ g   Z ( p e 2 p wf 2 ) log e ( r e r w )
Equation 5.18c

In this equation, we evaluate μ g and Z at the arithmetic mean average pressure, Equation 5.15. Again, we can add a skin factor to account for well damage or stimulation and write similar equations in terms of average pressure p ¯ 2 for the pseudo-steady state flow regime. Equation 5.18c is the Inflow Performance Relationship for Gas in Terms of Pressure-Squared.