| THEORY & FORMULAE |
It is a common and economic engineering practice to make surface measurements of gas pressure (and flowrate), and from thence predict the static and flowing pressure at the subsurface sand face.
The widely-used equation for estimating both static and flowing bottomhole pressure for a single-phase vertical gas flow in a tubing is given as:
Where:
Q = gas rate at surface, Mcf/d, i.e. 1000cf/d
+ = gas production
− = gas injection
Ps = flowing sandface pressure, psia
Pw = wellhead pressure, psia
Ta = average temperature, °R
G = mean gas relative density (air = 1)
Za= mean gas compressibility factor
d = inside diameter of pipe, inches
h = tubing length/well depth, ft
ƒ = Moody friction factor
Z depends on both T & P and, T & P vary across the length of the tubing, and P is the primary unknown. Thus the equation can only be solved in an stepwise iterative fashion. The method of successive substitution is used here to solve the equation. The tubing is discretized into 10 equal sections, such that the Pw of one section is set equal to the Ps of the one above it, and so on. Z is computed via the Yarborough & Hall correlations.