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Thermal Performances of Windows
Introduction
During the design of a building, environmental issues have gained considerable influence in the entire project. One of the first concerns is to improve thermal performances. In this process, simulation software provide key tools for modeling thermal losses and performances in the building.
The international standard ISO 10077-2:2012 (Ref. 1) deals with thermal performances of windows, doors, and shutters. It provides computed values of the thermal characteristics of frame profiles in order to validate a simulation software.
COMSOL Multiphysics successfully passes the entire benchmark. This document describes six frame profiles of ISO 10077-2:2012 related to windows only. Other test cases from this standard are available in the following applications:
Figure 1: Geometry of one of the windows and cross-section view.
Model Definition
On each test case, a window section separates a hot internal side from a cold external side. In these applications, the traditional glazing is replaced by an insulation panel. After solving a model, two quantities are calculated and compared to the normative values:
air cavities
A window frame contains many cavities. The purpose is to ensure thermal insulation. According to the standard, cavities are modeled in different ways depending on their shapes.
The heat flow rate in cavities is represented by an equivalent thermal conductivity keq, which includes the heat flow by conduction, convection, and radiation. It also depends on the geometry of the cavity and on the adjacent materials. The definition of keq is detailed in the next paragraphs.
Cavities are divided into three types:
unventilated cavities, completely closed or connected either to the exterior or to the interior by a slit with a width not exceeding 2 mm;
slightly ventilated cavities, connected either to the exterior or to the interior by a slit greater than 2 mm but not exceeding 10 mm;
well-ventilated cavities, corresponding to a configuration not covered by one of the two preceding types, it is assumed that the whole surface is exposed to the environment so that boundary conditions are applied to (see the Boundary conditions section below for more information).
Unventilated Rectangular Cavity
For an unventilated rectangular cavity, the equivalent thermal conductivity is defined by:
where d is the cavity dimension in the heat flow rate direction, and R is the cavity thermal resistance given by:
where ha is the convective heat transfer coefficient, and hr is the radiative heat transfer coefficient. These coefficients are defined by:
where:
C1 = 0.025 W/(m·K)
C2 = 0.73 W/(m2·K4/3)
ΔT is the maximum surface temperature difference in the cavity
σ = 5.67·10-8 W/(m2·K4) is the Stefan-Boltzmann constant
Tm is the average temperature on the boundaries of the cavity
E is the intersurface emittance, defined by:
ε1 and ε2 are the surface emissivities (both are equal to 0.90 in this model)
F is the view factor of the rectangular section, defined by:
d is the cavity dimension in the heat flow rate direction
b is the cavity dimension perpendicular to the heat flow rate direction
Slightly Ventilated Rectangular Cavities
For a slightly ventilated cavity, the equivalent thermal conductivity is twice that of an unventilated cavity of the same size.
Nonrectangular Cavities
Nonrectangular cavities are transformed into rectangular cavities of same area and aspect ratio according to defined rules in ISO 10077-2:2012 presented below. Then, keq is evaluated following one of the two previous rectangular cases.
Figure 2: Nonrectangular cavity transformation.
Figure 2 shows a nonrectangular cavity of area A. Then, d and b are the depth and the width (in accordance with the direction of the heat flow) of the smallest rectangle than can contain of the nonrectangular cavity. The equivalent rectangular cavity, of size b × d and area A must satisfy:
Hence, b and d are given by:
Boundary conditions
The heat flux conditions for internal and external sides are given by Newton’s law of cooling:
where Text is the exterior temperature (Text = Ti = 20°C for the internal side and Text = Te = 0°C for the external side). The standard defines thermal surface resistance, Rs, which is related to the heat transfer coefficient, h, by:
Internal and external thermal surface resistances are not equal. Moreover, on boundaries linked to the internal side, an increased thermal resistance is used in edges. Figure 3 explains how to determine boundaries where it should be applied.
Figure 3: Protected boundaries.
If d is greater than 30 mm, b is set to 30 mm. Otherwise, b = d is chosen. Furthermore, two boundaries are considered as adiabatic: the boundary in contact with the wall and the end of the insulation panel.
Description of the six Applications
Figure 4 to Figure 9 depict the geometry of each application but only a part of the insulation panel is represented. Unventilated cavities are red-numbered while slightly ventilated cavities are green-numbered. Boundaries with an increased thermal resistance are represented with bold black lines. Adiabatic boundaries in contact with the wall are represented with a striped rectangle.
Application 1: Aluminum Frame with Thermal Break
The first application studies the heat conduction in an aluminum frame section with thermal break. The frame structure is made of aluminum with a high thermal conductivity k of 160 W/(m·K). Four barriers made of polyamide 6.6 with 25% of glass fiber compose the thermal break. They have a low thermal conductivity of 0.30 W/(m·K). Ethylene propylene diene monomer (EPDM) rubber gaskets are also used to waterproof the window. EPDM rubber has a thermal conductivity of 0.25 W/(m·K). The insulation panel has a very low thermal conductivity of 0.035 W/(m·K).
This frame is divided into many cavities: most of them are considered as unventilated cavities because they are not connected to the exterior. One cavity is connected to the exterior. According to the standard, this cavity is cut into two “subcavities” due to its internal 2 mm width slit. The first cavity (labeled 1 on Figure 4) is considered as unventilated cavity and the second cavity (labeled 10 on Figure 4) are considered as a slightly ventilated cavity.
Figure 4: Geometry of the first window.
Application 2: Aluminum Clad Wood Frame
The second application studies the heat conduction in an aluminum clad wood frame section. The frame is made of two wood blocks with a thermal conductivity of 0.13 W/(m·K). On the external side, a wood block is covered by an aluminum structure which has a high thermal conductivity. This application includes EPDM gaskets too.
All cavities is considered as an unventilated cavities because they are either closed or connected to the exterior by a 2 mm width slit.
Figure 5: Geometry of the second window.
Application 3: PVC Frame with Steel Reinforcement
The third application studies the heat conduction in a PVC frame section with steel reinforcement. The main structure of the frame is made of PVC, which has a thermal conductivity of 0.17 W/(m·K). Two reinforcements made of steel are also present. Steel has a high thermal conductivity of 50 W/(m·K). EPDM gaskets are used.
Air cavities are all completely closed or connected to the exterior by a slit with a width not exceeding 2 mm. Thus they are considered as unventilated cavities.
Figure 6: Geometry of the third window.
Application 4: Roof Window
The fourth application studies the heat conduction in a roof window frame section. The main part of the frame is made of two soft wood blocks. The interior part is aluminum clad and there are also EPDM gaskets.
Three air cavities are not connected to the exterior or only by a slit with a width smaller than 2 mm. They are considered as unventilated. Four others air cavities are considered as slightly ventilated cavities.
Figure 7: Geometry of the fourth window.
Application 5: Sliding Window
The fifth application studies the heat conduction in a sliding window frame section. The frame has an aluminum structure with a high thermal conductivity. There are some thermal breaks made of rigid polyurethane (PU), polyamide, and polyester mohair. Their thermal conductivities are 0.25 W/(m·K), 0.25 W/(m·K), and 0.14 W/(m·K), respectively. There are also some EPDM gaskets to waterproof the window.
Four air cavities are completely closed, and two others are connected to the exterior by a 2 mm width slit. According to the standard, they are considered as unventilated cavities. One cavity is considered as a slightly ventilated cavity because it is connected to the exterior by a larger slit of 6 mm. In addition, one last cavity is considered as well ventilated because it is connected to the exterior with a 15 mm width slit.
Figure 8: Geometry of the fifth window.
Application 6: PVC Frame
The sixth application studies the heat conduction in a fixed PVC frame section. Polyamide with a thermal conductivity of 0.25 W/(m·K) is used. There are also some EPDM gaskets to waterproof the window.
In this application, there are seven closed cavities. There are considered as unventilated. In addition, one cavity is connected to the exterior by a 3 mm width slit so it is considered as slightly ventilated.
Figure 9: Geometry of the sixth window.
Results and Discussion
Temperature profiles
The temperature profiles for each application are shown in Figure 10 to Figure 15.
Figure 10: Temperature distribution in the aluminum frame with thermal break.
Figure 11: Temperature distribution in the aluminum clad wood frame.
Figure 12: Temperature distribution in the PVC frame with steel reinforcement.
Figure 13: Temperature distribution in the roof window.
Figure 14: Temperature distribution in the sliding window.
Figure 15: Temperature distribution in the PVC frame.
Quantities of interest
The quantities of interest are the following:
where is the heat flow rate through the window (in W/m), Te = 0°C is the external temperature and Ti = 20°C is the internal temperature
where bp is the visible width of the panel expressed in meters, bf is the projected width of the frame section expressed in meters, and Up is the thermal transmittance of the central area of the panel expressed in W/(m2·K).
Table 1 to Table 6 compare the numerical results of COMSOL Multiphysics with the expected values provided by ISO 10077-2:2012.
Table 1: comparison between expected and computed values of quantities in Application 1.
L2D (W/(m·K))
Uf (W/(m2·K))
Table 2: comparison between expected and computed values of quantities in Application 2.
L2D (W/(m·K))
Uf (W/(m2·K))
Table 3: comparison between expected and computed values of quantities in Application 3.
L2D (W/(m·K))
Uf (W/(m2·K))
Table 4: comparison between expected and computed values of quantities in Application 4.
L2D (W/(m·K))
Uf (W/(m2·K))
Table 5: comparison between expected and computed values of quantities in Application 5.
L2D (W/(m·K))
Uf (W/(m2·K))
Table 6: comparison between expected and computed values of quantities in Application 6.
L2D (W/(m·K))
Uf (W/(m2·K))
The maximum permissible differences to pass this test case are 3% for the thermal conductance and 5% for the thermal transmittance. The measured values are completely coherent and meet the validation criteria.
Reference
1. European Committee for Standardization, ISO 10077-2:2012, Thermal performance of windows, doors and shutters – Calculation of thermal transmittance – Part 2: Numerical method for frames, 2012.
Application Library path: Heat_Transfer_Module/Buildings_and_Constructions/windows_thermal_performances
Modeling Instructions
Root
Start by opening the following prepared file. It already contains global definitions, geometries, local variables, selections, operators and material properties.
1
From the File menu, choose Open.
2
First Window (comp1)
Click the  Zoom Extents button in the Graphics toolbar.
First Window
First Window (comp1)
In the Model Builder window, expand the First Window (comp1) node.
Definitions (comp1)
Variables 1
Define the thermal conductance of the section for the postprocessing part as follows.
1
In the Model Builder window, expand the First Window (comp1)>Definitions node, then click Variables 1.
2
In the Settings window for Variables, locate the Variables section.
3
Note that because boundaries linked to the wall and the end of the insulation panel are considered adiabatic, the heat flow rates through the internal and external boundaries are equal (in absolute values).
4
In the Model Builder window, collapse the First Window (comp1)>Definitions node.
Heat Transfer in Solids and Fluids (ht)
Fluid 1
1
In the Model Builder window, expand the Heat Transfer in Solids and Fluids (ht) node, then click Fluid 1.
2
Heat Flux 1
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Exterior Side.
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rse.
6
In the Text text field, type Te.
Heat Flux 2
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Flat Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_n.
6
In the Text text field, type Ti.
Heat Flux 3
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Corner Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_p.
6
In the Text text field, type Ti.
Open Boundary 1
1
In the Physics toolbar, click  Boundaries and choose Open Boundary.
2
3
In the Settings window for Open Boundary, locate the Upstream Properties section.
4
In the Tustr text field, type Te.
5
In the Model Builder window, collapse the Heat Transfer in Solids and Fluids (ht) node.
Study 1
The heat flow rate through the interior (or exterior) side of the section needs to be determined to calculate the thermal conductance of the section. In order to have enough precision in this value, the default relative tolerance of the solver has already been modified to 106. To access to this value, expand the Solver 1 node and click on the Stationary Solver 1 node. In the Stationary Solver settings window, locate the General section.
1
In the Home toolbar, click  Compute.
Results
Temperature (ht)
A Global Evaluation node is added in order to calculate the thermal conductance of the section and the thermal transmittance of the frame.
Thermal Conductance of the Section (L2D) 1
1
In the Model Builder window, expand the Results>Derived Values node.
2
Right-click Derived Values and choose Global Evaluation.
3
In the Settings window for Global Evaluation, type Thermal Conductance of the Section (L2D) 1 in the Label text field.
4
Locate the Expressions section. In the table, enter the following settings:
5
Click  Evaluate.
Table
1
Go to the Table window.
The results should be close to the expected values in Table 1.
Results
Surface
1
In the Model Builder window, expand the Results>Temperature (ht) node, then click Surface.
2
In the Settings window for Surface, locate the Expression section.
3
From the Unit list, choose degC.
4
In the Temperature (ht) toolbar, click  Plot.
The current plot group shows the temperature distribution; compare with Figure 10.
The same simulation method is applied on five other benchmarks. The instructions below describe the steps to achieve the calculations.
First Window (comp1)
In the Model Builder window, collapse the First Window (comp1) node.
Second Window
Second Window (comp2)
In the Model Builder window, expand the Second Window (comp2) node.
Definitions (comp2)
Variables 2
1
In the Model Builder window, expand the Second Window (comp2)>Definitions node, then click Variables 2.
2
In the Settings window for Variables, locate the Variables section.
3
4
In the Model Builder window, collapse the Second Window (comp2)>Definitions node.
Heat Transfer in Solids and Fluids 2 (ht2)
Fluid 1
1
In the Model Builder window, expand the Heat Transfer in Solids and Fluids 2 (ht2) node, then click Fluid 1.
2
Heat Flux 1
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Exterior Side.
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rse.
6
In the Text text field, type Te.
Heat Flux 2
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Flat Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_n.
6
In the Text text field, type Ti.
Heat Flux 3
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Corner Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_p.
6
In the Text text field, type Ti.
Open Boundary 1
1
In the Physics toolbar, click  Boundaries and choose Open Boundary.
2
3
In the Settings window for Open Boundary, locate the Upstream Properties section.
4
In the Tustr text field, type Te.
5
In the Model Builder window, collapse the Heat Transfer in Solids and Fluids 2 (ht2) node.
Study 2
In the Home toolbar, click  Compute.
Results
A Global Evaluation node is added in order to calculate the thermal conductance of the section and the thermal transmittance of the frame.
Thermal Conductance of the Section (L2D) 2
1
In the Results toolbar, click  Global Evaluation.
2
In the Settings window for Global Evaluation, type Thermal Conductance of the Section (L2D) 2 in the Label text field.
3
Locate the Data section. From the Dataset list, choose Study 2/Solution 2 (8) (sol2).
4
Locate the Expressions section. In the table, enter the following settings:
5
Click  Evaluate.
Table
1
Go to the Table window.
The results should be close to the expected values in Table 2.
Results
Surface
1
In the Model Builder window, expand the Results>Temperature (ht2) node, then click Surface.
2
In the Settings window for Surface, locate the Expression section.
3
From the Unit list, choose degC.
4
In the Temperature (ht2) toolbar, click  Plot.
The current plot group shows the temperature distribution; compare with Figure 11.
Second Window (comp2)
In the Model Builder window, collapse the Second Window (comp2) node.
Third Window
Third Window (comp3)
In the Model Builder window, expand the Third Window (comp3) node.
Definitions (comp3)
Variables 3
1
In the Model Builder window, expand the Third Window (comp3)>Definitions node, then click Variables 3.
2
In the Settings window for Variables, locate the Variables section.
3
4
In the Model Builder window, collapse the Third Window (comp3)>Definitions node.
Heat Transfer in Solids and Fluids 3 (ht3)
Fluid 1
1
In the Model Builder window, expand the Heat Transfer in Solids and Fluids 3 (ht3) node, then click Fluid 1.
2
Heat Flux 1
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Exterior Side.
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rse.
6
In the Text text field, type Te.
Heat Flux 2
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Flat Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_n.
6
In the Text text field, type Ti.
Heat Flux 3
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Corner Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_p.
6
In the Text text field, type Ti.
Open Boundary 1
1
In the Physics toolbar, click  Boundaries and choose Open Boundary.
2
3
In the Settings window for Open Boundary, locate the Upstream Properties section.
4
In the Tustr text field, type Te.
5
In the Model Builder window, collapse the Heat Transfer in Solids and Fluids 3 (ht3) node.
Edit the default mesh settings to improve the mesh resolution of narrow regions.
Mesh 3
Size
1
In the Model Builder window, under Third Window (comp3) right-click Mesh 3 and choose Edit Physics-Induced Sequence.
2
In the Settings window for Size, click to expand the Element Size Parameters section.
3
In the Resolution of narrow regions text field, type 2.
4
In the Model Builder window, collapse the Mesh 3 node.
Study 3
In the Home toolbar, click  Compute.
Results
A Global Evaluation node is added in order to calculate the thermal conductance of the section and the thermal transmittance of the frame.
Thermal Conductance of the Section (L2D) 3
1
In the Results toolbar, click  Global Evaluation.
2
In the Settings window for Global Evaluation, type Thermal Conductance of the Section (L2D) 3 in the Label text field.
3
Locate the Data section. From the Dataset list, choose Study 3/Solution 3 (15) (sol3).
4
Locate the Expressions section. In the table, enter the following settings:
5
Click  Evaluate.
Table
1
Go to the Table window.
The results should be close to the expected values in Table 3.
Results
Surface
1
In the Model Builder window, expand the Results>Temperature (ht3) node, then click Surface.
2
In the Settings window for Surface, locate the Expression section.
3
From the Unit list, choose degC.
4
In the Temperature (ht3) toolbar, click  Plot.
The current plot group shows the temperature distribution; compare with Figure 12.
Third Window (comp3)
In the Model Builder window, collapse the Third Window (comp3) node.
Fourth Window
Fourth Window (comp4)
In the Model Builder window, expand the Fourth Window (comp4) node.
Definitions (comp4)
Variables 4
1
In the Model Builder window, expand the Fourth Window (comp4)>Definitions node, then click Variables 4.
2
In the Settings window for Variables, locate the Variables section.
3
4
In the Model Builder window, collapse the Fourth Window (comp4)>Definitions node.
Another mean to improve the accuracy of the solution is to use second order elements for the discretization of the temperature field. Second order elements are particularly efficient for purely conductive models as the ones studied here.
Heat Transfer in Solids and Fluids 4 (ht4)
1
In the Model Builder window, under Fourth Window (comp4) click Heat Transfer in Solids and Fluids 4 (ht4).
2
In the Settings window for Heat Transfer in Solids and Fluids, click to expand the Discretization section.
3
From the Temperature list, choose Quadratic Lagrange.
Fluid 1
1
In the Model Builder window, expand the Heat Transfer in Solids and Fluids 4 (ht4) node, then click Fluid 1.
2
Heat Flux 1
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Exterior Side.
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rse.
6
In the Text text field, type Te.
Heat Flux 2
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Flat Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_n.
6
In the Text text field, type Ti.
Heat Flux 3
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Corner Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_p.
6
In the Text text field, type Ti.
Open Boundary 1
1
In the Physics toolbar, click  Boundaries and choose Open Boundary.
2
3
In the Settings window for Open Boundary, locate the Upstream Properties section.
4
In the Tustr text field, type Te.
Open Boundary 2
1
In the Physics toolbar, click  Boundaries and choose Open Boundary.
2
3
In the Settings window for Open Boundary, locate the Upstream Properties section.
4
In the Tustr text field, type Ti.
5
In the Model Builder window, collapse the Heat Transfer in Solids and Fluids 4 (ht4) node.
Edit the default mesh settings to improve the mesh resolution of narrow regions.
Mesh 4
Size
1
In the Model Builder window, under Fourth Window (comp4) right-click Mesh 4 and choose Edit Physics-Induced Sequence.
2
In the Settings window for Size, click to expand the Element Size Parameters section.
3
In the Resolution of narrow regions text field, type 2.
4
In the Model Builder window, collapse the Mesh 4 node.
Study 4
In the Home toolbar, click  Compute.
Results
A Global Evaluation node is added in order to calculate the thermal conductance of the section and the thermal transmittance of the frame.
Thermal Conductance of the Section (L2D) 4
1
In the Results toolbar, click  Global Evaluation.
2
In the Settings window for Global Evaluation, type Thermal Conductance of the Section (L2D) 4 in the Label text field.
3
Locate the Data section. From the Dataset list, choose Study 4/Solution 4 (22) (sol4).
4
Locate the Expressions section. In the table, enter the following settings:
5
Click  Evaluate.
Table
1
Go to the Table window.
The results should be close to the expected values in Table 4.
Results
Surface
1
In the Model Builder window, expand the Results>Temperature (ht4) node, then click Surface.
2
In the Settings window for Surface, locate the Expression section.
3
From the Unit list, choose degC.
4
In the Temperature (ht4) toolbar, click  Plot.
The current plot group shows the temperature distribution; compare with Figure 13.
Fourth Window (comp4)
In the Model Builder window, collapse the Fourth Window (comp4) node.
Fifth Window
Fifth Window (comp5)
In the Model Builder window, expand the Fifth Window (comp5) node.
Definitions (comp5)
Variables 5
1
In the Model Builder window, expand the Fifth Window (comp5)>Definitions node, then click Variables 5.
2
In the Settings window for Variables, locate the Variables section.
3
4
In the Model Builder window, collapse the Fifth Window (comp5)>Definitions node.
Heat Transfer in Solids and Fluids 5 (ht5)
Fluid 1
1
In the Model Builder window, expand the Heat Transfer in Solids and Fluids 5 (ht5) node, then click Fluid 1.
2
Heat Flux 1
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Exterior Side.
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rse.
6
In the Text text field, type Te.
Heat Flux 2
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Flat Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_n.
6
In the Text text field, type Ti.
Heat Flux 3
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Corner Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_p.
6
In the Text text field, type Ti.
Open Boundary 1
1
In the Physics toolbar, click  Boundaries and choose Open Boundary.
2
3
In the Settings window for Open Boundary, locate the Upstream Properties section.
4
In the Tustr text field, type Te.
Open Boundary 2
1
In the Physics toolbar, click  Boundaries and choose Open Boundary.
2
3
In the Settings window for Open Boundary, locate the Upstream Properties section.
4
In the Tustr text field, type Ti.
5
In the Model Builder window, collapse the Heat Transfer in Solids and Fluids 5 (ht5) node.
Study 5
In the Home toolbar, click  Compute.
Results
A Global Evaluation node is added in order to calculate the thermal conductance of the section and the thermal transmittance of the frame.
Thermal Conductance of the Section (L2D) 5
1
In the Results toolbar, click  Global Evaluation.
2
In the Settings window for Global Evaluation, type Thermal Conductance of the Section (L2D) 5 in the Label text field.
3
Locate the Data section. From the Dataset list, choose Study 5/Solution 5 (29) (sol5).
4
Locate the Expressions section. In the table, enter the following settings:
5
Click  Evaluate.
Table
1
Go to the Table window.
The results should be close to the expected values in Table 5.
Results
Surface
1
In the Model Builder window, expand the Results>Temperature (ht5) node, then click Surface.
2
In the Settings window for Surface, locate the Expression section.
3
From the Unit list, choose degC.
4
In the Temperature (ht5) toolbar, click  Plot.
The current plot group shows the temperature distribution; compare with Figure 14.
Fifth Window (comp5)
In the Model Builder window, collapse the Fifth Window (comp5) node.
Sixth Window
Sixth Window (comp6)
In the Model Builder window, expand the Sixth Window (comp6) node.
Definitions (comp6)
Variables 6
1
In the Model Builder window, expand the Sixth Window (comp6)>Definitions node, then click Variables 6.
2
In the Settings window for Variables, locate the Variables section.
3
4
In the Model Builder window, collapse the Sixth Window (comp6)>Definitions node.
Heat Transfer in Solids and Fluids 6 (ht6)
Fluid 1
1
In the Model Builder window, expand the Heat Transfer in Solids and Fluids 6 (ht6) node, then click Fluid 1.
2
Heat Flux 1
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Exterior Side.
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rse.
6
In the Text text field, type Te.
Heat Flux 2
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Interior Side (Flat Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_n.
6
In the Text text field, type Ti.
Heat Flux 3
1
In the Physics toolbar, click  Boundaries and choose Heat Flux.
2
In the Settings window for Heat Flux, locate the Boundary Selection section.
3
From the Selection list, choose Internal (Corner Area).
4
Locate the Heat Flux section. Click the Convective heat flux button.
5
In the h text field, type 1/Rsi_p.
6
In the Text text field, type Ti.
Open Boundary 1
1
In the Physics toolbar, click  Boundaries and choose Open Boundary.
2
3
In the Settings window for Open Boundary, locate the Upstream Properties section.
4
In the Tustr text field, type Te.
5
In the Model Builder window, collapse the Heat Transfer in Solids and Fluids 6 (ht6) node.
Study 6
In the Home toolbar, click  Compute.
Results
A Global Evaluation node is added in order to calculate the thermal conductance of the section and the thermal transmittance of the frame.
Thermal Conductance of the Section (L2D) 6
1
In the Results toolbar, click  Global Evaluation.
2
In the Settings window for Global Evaluation, type Thermal Conductance of the Section (L2D) 6 in the Label text field.
3
Locate the Data section. From the Dataset list, choose Study 6/Solution 6 (36) (sol6).
4
Locate the Expressions section. In the table, enter the following settings:
5
Click  Evaluate.
Table
1
Go to the Table window.
The results should be close to the expected values in Table 6.
Results
Surface
1
In the Model Builder window, expand the Results>Temperature (ht6) node, then click Surface.
2
In the Settings window for Surface, locate the Expression section.
3
From the Unit list, choose degC.
4
In the Temperature (ht6) toolbar, click  Plot.
The current plot group shows the temperature distribution; compare with Figure 15.