The
gas–liquid two-phase flow is widely encountered in many
industrial applications, and its online and nonseparation flow rate
measurement has plagued the industry for many years. Based on the
thermal diffusion measurement, which was proposed to measure the velocities
and lengths of the Taylor bubble and liquid slug in our previous study,
a method for further measuring the flow rate of gas–liquid
two-phase flow under a slug flow pattern is presented in this paper.
The pipe wall temperature is monitored to capture the passages of
each Taylor bubble and liquid slug and measure their velocities (U
TB and U
LS) and
lengths (L
TB and L
LS), based on which the liquid film thickness around the Taylor
bubble (η) is derived. A good linear relationship was found
between the average descending slope of the temperature curve (k̅), the liquid slug velocity (U
LS), and the void fraction in the liquid slug (αLS), and the void fraction is acquired based on this relationship.
In accordance with the flow law and distribution of gas and liquid
phases, a new flow rate calculation model is established to predict
the flow rate of each phase using the measured slug flow characteristics
(U
TB, U
LS, L
TB, L
LS, η,
and αLS). Experimental tests on air–water
two-phase flow show that the average relative errors in the gas and
liquid flow rates are 3.45% and 5.51%, with maximum values of 9.98%
and 10.47%, respectively.