Foam
fluid is widely used in petroleum industry, so the behavior
of the foam fluid flow in porous media directly affects the application
effect of foam. However, the foam flow pattern in porous media is
difficult to be established because of its dynamic change of interface
structure and unpredictable boundary condition. In this work, the
transient structural changes of the foam fluid in porous media are
quantitatively characterized, and the flow behavior is analyzed based
on fractal theory and visual experiments. First, the foam fractal
characteristics are verified, and the fractal dimension is calculated.
Results show that the foam fractal dimension is between 1.5 and 2.0,
and the foam flow can be divided into three stages: gas–liquid
two-phase flow, foam unstable flow stage, and foam stable flow stage.
In addition, the evaluation indices of foam performance in porous
media are proposed to evaluate the influencing factors, namely, the
fractal dimension in stable stage D
foam‑s and the time needed to reach stability T
s. The analysis shows that the larger concentration of the surfactant
and the lower permeability correspond to smaller D
foam‑s and the larger temperature corresponds to
larger D
foam‑s, and D
foam‑s of the nitrogen foam is smaller than that
of the carbon dioxide foam. T
s is the
opposite. Last, the relationship between fractal dimension, pressure,
and gas saturation is discussed. Qualitative analysis shows that the
larger the displacement pressure, the smaller the foam fractal dimension
and the higher the gas saturation, the smaller the foam fractal dimension.
This paper provides a new method to explore the flow behavior of foam
flow in formation, which has a certain significance for guiding the
field application of the foam fluid.