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Dynamic Data Analysis – v5.12.01 - © KAPPA 1988-2017

Chapte

r 2 – T heory

- p20/743

2.C

Line Source Solution in a homogeneous infinite reservoir

We now consider the simplest problem we can find: the diffusion in a homogeneous infinite

reservoir, starting at initial uniform pressure p

i

, produced by a vertical line source well. The

introduction to dimensionless terms and the derivations for this model are shown in the

Chapter ‘Analytical models - 13.B - Dimensionless problems’.

2.C.1

The Line Source Solution

The solution in dimensionless terms is given in the paragraph ‘13.B - Dimensionless problems’.

To get the physical solution, the dimensionless parameters are replaced by their real values.

The solution at any point and time, for a Line Source well producing a homogeneous infinite

reservoir, is then given by the following:

Line Source Solution:

 

 

 

kt

rc

E

kh

qB

p trp

t

i

i

2

1. 948

6.70

,

A typical line source response is displayed in the figures below, on a loglog scale (with the

Bourdet derivative) and a semilog scale. For first readers, the notions of loglog and semilog

plots are described in the PTA methodology chapter.

Fig. 2.C.1 – Line source loglog plot

Fig. 2.C.2 – Line source semilog plot

The line source equation shows that the pressure change is a unique function of the parameter

group r

2

/t, or more conveniently r/√t. This has an important implication on the physical

understanding of the diffusion process. If one considers, for example, the time it requires for

the pressure change to reach a certain value (for example 1 psi), it will amount to a certain

value of r/√t that we will calculate from the Line Source Solution, and therefore the relation:

Radius of investigation:

ta r

inv

In the chapter on boundary models we recommend at one does not use the notion of radius of

investigation, as it may be misleading when one considers how such result is used afterwards.

However, it is an interesting means of understanding the diffusion process. To extend this

notion to cases where the flow geometry may not be strictly radial, we may consider that the

area of investigation is proportional to r², and we therefore have: