StraightPipe |
Mean heat transfer coefficient of straight pipe | uniform wall temperature or uniform heat flux | hydrodynamically developed or undeveloped laminar flow regime |
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Mean heat transfer coefficient of straight pipe | uniform wall temperature or uniform heat flux | hydrodynamically developed or undeveloped laminar flow regime |
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Input record for function kc_laminar and kc_laminar_KC |
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Input record for function kc_laminar and kc_laminar_KC |
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Mean heat transfer coefficient of straight pipe | uniform wall temperature or uniform heat flux | hydrodynamically developed or undeveloped overall flow regime| pressure loss dependence |
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Mean heat transfer coefficient of straight pipe | uniform wall temperature or uniform heat flux | hydrodynamically developed or undeveloped overall flow regime| pressure loss dependence |
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Input record for function kc_overall and kc_overall_KC |
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Input record for function kc_overall and kc_overall_KC |
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Mean heat transfer coefficient of straight pipe | hydrodynamically developed turbulent flow regime | pressure loss dependence |
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Mean heat transfer coefficient of straight pipe | hydrodynamically developed turbulent flow regime | pressure loss dependence |
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Input record for function kc_turbulent and kc_turbulent_KC |
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Input record for function kc_turbulent and kc_turbulent_KC |
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Local two phase heat transfer coefficient of straight pipe | horizontal or vertical boiling | horizontal condensation |
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Input record for function kc_twoPhaseOverall_KC |
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Input record for function kc_twoPhaseOverall_KC |
This information is part of the Modelica Standard Library maintained by the Modelica Association.
Calculation of mean convective heat transfer coefficient kc of a straight pipe at an uniform wall temperature or uniform heat flux and for a hydrodynamically developed or undeveloped laminar fluid flow. See more information.
Calculation of mean convective heat transfer coefficient kc of a straight pipe for a hydrodynamically developed turbulent fluid flow at uniform wall temperature or See more information.