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The cylinder with outer diameter 10 mm and heated length 10 mm was designed for high temperature uniformity.
The monoblock has a 180.0 mm heated length, has a 10.0 mm inside diameter, and has a square cross-section with 30.0 mm nominal outside surfaces.
In the present work, the axial streamwise profile of the fluid and wall temperature for air water (i) isolated single Taylor bubble and, (ii) a train of Taylor bubbles, in a horizontal square channel of size 3.3 mm × 3.3 mm × 350 mm, heated from the bottom (heated length = 175 mm), with the other three sides kept insulated, are reported at different gas volume flow ratios.
The gap of the annular flow channel was 6.0 mm with an effective heated length on the inner heated rod of 1400 mm.
The variation in the heat transfer coefficient due to differences in the heated length may also influence the performance of the existing microscale heat transfer correlations.
Heat transfer coefficients were measured at six cross sections along the heated length, with 60 azimuthal positions being monitored at each section.
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The channel hydraulic diameters covered the range 16 26.7 mm, and the heated length-to-hydraulic-diameter ratio varied in the range from 23.3 to 51.
The results suggested that RDS was not correlated to heating length but positively correlated to temperature and moisture content.
The heating length determined the start point of heating; the heating power determined how long the wellbore temperature remained above the inflection point temperature.
However, heating length of 2,000 m is not able to meet the requirement that crude oil temperature is higher than the inflection point temperature.
Quadrature is used to obtain numerical results for the local and average Nusselt number for various flow velocities, heating lengths, wall thicknesses, and wall conductivities.
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