2013
DOI: 10.1063/1.4816892
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Flow regimes of adiabatic gas-liquid two-phase under rolling conditions

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“…The mixture of N 2 and inhibitor-water mist in the mixing chamber of the nozzle forms a gas-liquid two-phase flow, and it is discharged from the outlet of the mixing chamber to the environment. The local resistance loss produced by the gas-liquid two-phase flow at the outlet of the mixing chamber can be calculated as the local resistance of the two-phase flow sudden expansion joint proposed by Romie[19]. Where Δ P E is the local resistance loss of the mixing chamber outlet ( Pa ); P a is the pressure of the environment ( Pa ); ρ gh is the density at the mixing chamber ( kg / m 3 ); B is the area ratio between the upstream and downstream sections of the sudden expansion outlet, and for the two-phase flow in the mixing chamber, B = 0; χ is the mass gas content, i.e., dryness, χ = G g / G w ; and v mh is mass velocity of the two-phase, , kg /( m 2 ∙ s ).…”
Section: Niwm Equipment Design and Operationmentioning
confidence: 99%
“…The mixture of N 2 and inhibitor-water mist in the mixing chamber of the nozzle forms a gas-liquid two-phase flow, and it is discharged from the outlet of the mixing chamber to the environment. The local resistance loss produced by the gas-liquid two-phase flow at the outlet of the mixing chamber can be calculated as the local resistance of the two-phase flow sudden expansion joint proposed by Romie[19]. Where Δ P E is the local resistance loss of the mixing chamber outlet ( Pa ); P a is the pressure of the environment ( Pa ); ρ gh is the density at the mixing chamber ( kg / m 3 ); B is the area ratio between the upstream and downstream sections of the sudden expansion outlet, and for the two-phase flow in the mixing chamber, B = 0; χ is the mass gas content, i.e., dryness, χ = G g / G w ; and v mh is mass velocity of the two-phase, , kg /( m 2 ∙ s ).…”
Section: Niwm Equipment Design and Operationmentioning
confidence: 99%