carbatpy.models.components.two_phase_correlations
Submodules
Classes
Condensation heat-transfer coefficient – Deng et al. (2019). |
|
Frictional pressure drop for evaporation – Moreno-Quibén & Thome (2007), |
|
Macdonald et al. two-phase frictional pressure-drop correlation. |
|
DISCLAIMER: ERROR IN PAPER? RESULTS IN INPLAUSIBLE PRESSURE LOSSES. CONTACTED AUTHORS. |
Package Contents
- class carbatpy.models.components.two_phase_correlations.DengHTC(D, G, T_wall, CT_type, state, fluid)[source]
Bases:
HeatTransferBaseCondensation heat-transfer coefficient – Deng et al. (2019).
Extends TwoPhaseBase with: - Log-mean void fraction (α) and Rouhani–Axelsson void fraction (α_ra) - Bell–Ghaly mixture correction - HTC for annular and stratified-wavy regimes
- Parameters:
D (float – inner tube diameter [m])
G (float – mass flux [kg/(m² s)])
T_wall (float – wall temperature [K])
CT_type (str – "HC" (hydrocarbon) or other (affects J_G^T constant))
state (
FluidState)fluid (carbatpy Fluid object)
- T_wall
- CT_type
- class carbatpy.models.components.two_phase_correlations.MQTPressureDrop(D, G, state, fluid, heat_transfer_rate=None)[source]
Bases:
PressureLossBaseFrictional pressure drop for evaporation – Moreno-Quibén & Thome (2007), with Wojtan–Ursenbacher–Thome (2005) flow map.
- Parameters:
D (float – inner tube diameter [m])
G (float – mass flux [kg/(m² s)])
state (
FluidState)fluid (carbatpy Fluid object)
- heat_transfer_rate = None
- class carbatpy.models.components.two_phase_correlations.MacdonaldPressureDrop(D, G, state, fluid)[source]
Bases:
PressureLossBaseMacdonald et al. two-phase frictional pressure-drop correlation.
- Parameters:
D (float – inner tube diameter [m])
G (float – mass flux [kg/(m² s)])
state (
FluidState)fluid (carbatpy Fluid object)
- class carbatpy.models.components.two_phase_correlations.FangPressureDrop(state, fluid, mdot, D, eps=0.0)[source]
Bases:
PressureLossBaseDISCLAIMER: ERROR IN PAPER? RESULTS IN INPLAUSIBLE PRESSURE LOSSES. CONTACTED AUTHORS. Frictional pressure drop for condensation – Fang et al. (2025), Int. J. Refrigeration 170, 214–223.
- Parameters:
state (
FluidState)fluid (carbatpy Fluid object)
mdot (float – mass flow rate [kg/s])
D (float – inner tube diameter [m])
- mdot
- eps = 0.0