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October 27, 2021, 16:34
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Post Process Heat Conservation Equation
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New Member
Sameed Akber
Join Date: Nov 2020
Posts: 7
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Hi,
I am running a a very simple transient simulation: turbulent flow through a rectangular channel; all walls are insulated; constant T,U inlet; buoyantPimpleFoam with sensibleEnthalpy I cannot satisfy the intregral energy equation in manual post processing. I've attached geometry and integral equation. Since all walls are insulated, AT EACH TIME STEP: Net energy coming into the domain = rate of change of Energy in control volume But net energy coming into domain is higher than rate of change of internal energy. I would appreciate any help. Thank you. |
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| Tags |
| buoyantpimplefoam, control volume, energy balance, heat transfer balance |
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