Source code for RCAIDE.Library.Attributes.Coolants.Glycol_Water

# RCAIDE/Library/Attributes/Coolants/Glycol_Water.py
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# Created:  Mar 2024, M. Clarke

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#  Imports
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from .Coolant import Coolant

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#  Glycol_Water
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[docs] class Glycol_Water(Coolant): """ Implementation of a 50-50 ethylene glycol-water mixture coolant properties. This class provides thermophysical properties and calculation methods for a standard ethylene glycol-water mixture commonly used in cooling systems. Attributes ---------- tag : str Identifier set to 'Glycol_Water' percent_glycol : float Mass fraction of glycol in the mixture (default: 0.5) density : float Mass per unit volume [kg/m³] specific_heat_capacity : float Heat capacity at constant pressure [J/kg·K] thermal_conductivity : float Heat conduction coefficient [W/m·K] dynamic_viscosity : float Absolute viscosity [Pa·s] Prandtl_number : float Dimensionless number for heat transfer characteristics kinematic_viscosity : float Ratio of dynamic viscosity to density [m²/s] Notes ----- All properties are currently implemented as constant values, though the method structure allows for future implementation of temperature and pressure dependence. **Major Assumptions** * Mixture is exactly 50% water and 50% ethylene glycol by mass * Standard atmospheric pressure conditions * Single-phase liquid mixture **Extra modules required** None References ---------- [1] The Engineering ToolBox (2003). Ethylene Glycol Heat-Transfer Fluid Properties. [online] Available at: https://www.engineeringtoolbox.com/ethylene-glycol-d_146.html [Accessed 8 January 2025]. [2] Microelectronics Heat Transfer Laboratory. (1997). Fluid Properties Calculator. Fluid properties calculator. http://www.mhtl.uwaterloo.ca/old/onlinetools/airprop/airprop.html See Also -------- RCAIDE.Library.Components.Thermal_Management : Thermal management system components """ def __defaults__(self): """This sets the default values. Assumptions: Mixture is 50% water-50% ethylene-glycol Source: Engineering Toolbox: https://www.engineeringtoolbox.com/ethylene-glycol-d_146.html University of Waterloo: http://www.mhtl.uwaterloo.ca/old/onlinetools/airprop/airprop.html """ self.tag = 'Glycol_Water' self.percent_glycol = 0.5 self.density = 1075 # kg/m^3 self.specific_heat_capacity = 3300 # J/kg.K self.thermal_conductivity = 0.387 # W/m.K self.dynamic_viscosity = 0.0019 # Pa.s self.Prandtl_number = self.specific_heat_capacity * self.dynamic_viscosity / self.thermal_conductivity self.kinematic_viscosity = self.dynamic_viscosity / self.density
[docs] def compute_cp(self,T=300): """ Calculate specific heat capacity of glycol-water mixture at given temperature. Parameters ---------- T : float, optional Temperature [K] (default: 300) Returns ------- cp : float Specific heat capacity [J/(kg·K)] Notes ----- Currently returns constant value of 3300 J/(kg·K), based on the default value, regardless of temperature. **Major Assumptions** * Temperature independence * 50-50 water-glycol mixture References ---------- [1] The Engineering ToolBox (2003). Ethylene Glycol Heat-Transfer Fluid Properties. [online] Available at: https://www.engineeringtoolbox.com/ethylene-glycol-d_146.html [Accessed 8 January 2025]. """ return self.specific_heat_capacity
[docs] def compute_absolute_viscosity(self,T=300.,p=101325.): """ Calculate dynamic viscosity of glycol-water mixture at given conditions. Parameters ---------- T : float, optional Temperature [K] (default: 300) p : float, optional Pressure [Pa] (default: 101325) Returns ------- mu : float Dynamic viscosity [kg/(m·s)] Notes ----- Currently returns constant value of 0.0019 Pa·s, based on the default value, regardless of conditions. **Major Assumptions** * Temperature and pressure independence * 50-50 water-glycol mixture References ---------- [1] The Engineering ToolBox (2003). Ethylene Glycol Heat-Transfer Fluid Properties. [online] Available at: https://www.engineeringtoolbox.com/ethylene-glycol-d_146.html [Accessed 8 January 2025]. """ return self.dynamic_viscosity
[docs] def compute_density(self,T=300.,p=101325.): """ Calculate density of glycol-water mixture at given conditions. Parameters ---------- T : float, optional Temperature [K] (default: 300) p : float, optional Pressure [Pa] (default: 101325) Returns ------- rho : float Density [kg/m³] Notes ----- Currently returns constant value of 1075 kg/m³ based on the default value. **Major Assumptions** * Temperature and pressure independence * 50-50 water-glycol mixture References ---------- [1] The Engineering ToolBox (2003). Ethylene Glycol Heat-Transfer Fluid Properties. [online] Available at: https://www.engineeringtoolbox.com/ethylene-glycol-d_146.html [Accessed 8 January 2025]. """ return self.density
[docs] def compute_thermal_conductivity(self,T=300.,p=101325.): """ Calculate thermal conductivity of glycol-water mixture at given conditions. Parameters ---------- T : float, optional Temperature [K] (default: 300) p : float, optional Pressure [Pa] (default: 101325) Returns ------- k : float Thermal conductivity [W/(m·K)] Notes ----- Currently returns constant value of 0.387 W/(m·K), based on the default values, regardless of conditions. **Major Assumptions** * Temperature and pressure independence * 50-50 water-glycol mixture References ---------- [1] Microelectronics Heat Transfer Laboratory. (1997). Fluid Properties Calculator. Fluid properties calculator. http://www.mhtl.uwaterloo.ca/old/onlinetools/airprop/airprop.html """ return self.thermal_conductivity
[docs] def compute_prandtl_number(self,T=300.): """ Calculate Prandtl number of glycol-water mixture at given temperature. Parameters ---------- T : float, optional Temperature [K] (default: 300) Returns ------- Pr : float Prandtl number [dimensionless] Notes ----- Calculated using the relationship: Pr = (μ·Cp)/k where: - μ is dynamic viscosity - Cp is specific heat capacity - k is thermal conductivity **Major Assumptions** * Temperature independence of constituent properties * 50-50 water-glycol mixture References ---------- [1] Microelectronics Heat Transfer Laboratory. (1997). Fluid Properties Calculator. Fluid properties calculator. http://www.mhtl.uwaterloo.ca/old/onlinetools/airprop/airprop.html """ Cp = self.compute_cp(T) mu = self.compute_absolute_viscosity(T) K = self.compute_thermal_conductivity(T) return mu*Cp/K