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Lecture Objectives: Analysis of unsteady state heat transfer HW3
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Unsteady-state heat transfer (Explicit – Implicit methods)
Example: To - known and changes in time Tw - unknown Ti - unknown Ai=Ao=6 m2 (mcp)i=648 J/K (mcp)w=9720 J/K Initial conditions: To = Tw = Ti = 20oC Boundary conditions: hi=ho=1.5 W/m2 Tw Ti To Ao=Ai Conservation of energy: Time [h] 0.1 0.2 0.3 0.4 0.5 0.6 0.7 To 20 30 35 32 10 15 Time step Dt=0.1 hour = 360 s
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Implicit methods - example
After rearranging: 2 Equations with 2 unknowns! = To Tw Ti =36 system of equation Tw Ti =72 system of equation Tw Ti
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Explicit methods - example
=360 sec = To Tw Ti =360 To Tw Ti =720 To Tw Ti Time There is NO system of equations! UNSTABILE
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Problems with stability !!! Often requires very small time steps
Explicit method Problems with stability !!! Often requires very small time steps
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Explicit methods - example
= To Tw Ti =36 To Tw Ti =72 To Tw Ti Stable solution obtained by time step reduction 10 times smaller time step Time =36 sec
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Explicit methods information progressing during the calculation
Tw Ti To
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Unsteady-state conduction - Wall
q Dx Nodes for numerical calculation
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Discretization of a non-homogeneous wall structure
Section considered in the following discussion Discretization in space Discretization in time
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Internal node Finite volume method
Boundaries of control volume For node “I” - integration through the control volume
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Internal node finite volume method
After some math work: Explicit method Implicit method
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Internal node finite volume method
Explicit method Rearranging: Implicit method Rearranging:
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Unsteady-state conduction Implicit method
b1T1 + +c1T2+=f(Tair,T1,T2) a2T1 + b2T2 + +c2T3+=f(T1 ,T2, T3) Air 1 2 3 4 5 6 Air a3T2 + b3T3+ +c3T4+=f(T2 ,T3 , T4) ……………………………….. a6T5 + b6T6+ =f(T5 ,T6 , Tair) Matrix equation M × T = F for each time step M × T = F
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Announcement Help with solving system of equation for HW 3
Next Tuesday at 6:00 pm Computer lab in the 2nd floor in ECJ
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Homework 3 (Similar to HW2, but unsteady, and more realistic)
Top view Surface radiation Tinter_surf ≠ Tair Te_i Te_o 2.5 m Tair_in Idif 8 m 8 m IDIR Glass South East Insulation Ts Tair_out Concrete Surface radiation IDIR IDIR
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HW3
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Explicit method Accuracy when compared to explicit ?
- simple for calculation - but unstable Problem with stability can be fixed with appropriate time step: Accuracy when compared to explicit ?
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Linearization of radiation equations Surface to surface radiation
Equations for internal surfaces - closed envelope Ti Tj Linearized equations: Calculate h based on temperatures from previous time step Or for your HW3
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Linearized radiation means linear system of equations
Calculated based on temperature values from previous time step B0 C0 T0 F0 A1 B1 C1 T1 F1 A2 B2 C2 T2 F2 These coefficient will have Some radiation convection coefficients x = A3 B3 C3 T3 F3 A4 B4 C4 T4 F4 A5 B5 C5 T5 F5 A6 B6 T6 F6
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Energy balance for air unsteady-state heat transfer
QHVAC
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System of equation for more than one element
Roof air Left wall Right wall Floor Elements are connected by: Convection – air node Radiation – surface nodes
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Example Tair is unknown and it is solved by system of equation :
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System of equations (matrix) for single zone (room)
8 elements Three diagonal matrix for each element x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x x Air equation
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System of equations for a building
Matrix for the whole building 4 rooms Rom matrixes Connected by common wall elements and airflow in-between room – Airflow simulation program (for example CONTAM) Energy Simulation program “meet” Airflow simulation program
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