Heat transfer for flow boiling of water and critical heat flux in a half‐heated round tube under low‐pressure conditions

Abstract

Heat transfer for flow boiling of water and critical heat flux (CHF) experiments in a half-circumferentially heated round tube under low-pressure conditions were carried out. To clarify the flow patterns in the heated section, experiments in the round tube under the same conditions were also carried out, and their results were compared. The experiments were conducted with atmospheric-pressure water in test sections with inner diameter D = 6 mm, heated length L = 360 mm, inlet water subcooling ∆T in = 80 K, and mass velocity G from 0 to 2000 kg/(m 2 ⋅s) for the half-circumferentially heated round tube and from 0 to 7000 kg/(m 2 ⋅s) for the full-circumferentially heated tube. The experimental data demonstrated that the wall temperature near the outlet of the half-circumferentially heated tube remained almost the same until CHF. It was found that burnout occurred when the flow regime changed from churn flow to annular flow, and the liquid film on the heated wall dried out although liquid film on the unheated wall remained.