Fundamentals of Heat and Mass Transfer¶
Incropera, F. P., DeWitt, D. P., Bergman, T. L., & Lavine, A. S. (2007). Fundamentals of Heat and Mass Transfer. Wiley.
Cited by¶
3 citations across 3 artifacts.
Each citation links to the sentence it supports in the citing article.
Primes¶
- Asymmetric Flux
- The asymmetry can be directional, as in one-way valves, ratchets, charge traps, and optical diodes; spectral or compositional, as in greenhouse glazing that transmits visible-band radiation but absorbs infrared, semipermeable membranes, frequency filters, and capital-flow controls;
This sourceStandard treatment of transport across selective boundaries, including semipermeable membranes and directionally selective barriers.
- The asymmetry can be directional, as in one-way valves, ratchets, charge traps, and optical diodes; spectral or compositional, as in greenhouse glazing that transmits visible-band radiation but absorbs infrared, semipermeable membranes, frequency filters, and capital-flow controls;
- Counter-Current Exchange
- Heat-exchanger engineering: counter-flow shell-and-tube exchangers achieve higher effectiveness than parallel-flow designs of the same size; the choice is structural, not empirical.
This sourceDerives counter-flow versus parallel-flow heat-exchanger effectiveness, the temperature-difference profile along the contact, and the dependence on capacity ratio and NTU. (
- Heat-exchanger engineering: counter-flow shell-and-tube exchangers achieve higher effectiveness than parallel-flow designs of the same size; the choice is structural, not empirical.
Domain-specific¶
- Boundary Value Problem
- Consider heat conduction through a furnace or exterior building wall of thickness L: inside the wall the steady temperature obeys the (elliptic) conduction equation, the inner face is held at a known fixed temperature (a Dirichlet condition set by the interior), and the outer face loses heat to ambient air by convection — a Robin condition in which the surface flux is proportional to the temperature difference with the outside air (Newton's law of cooling)
This sourceGives the convective surface condition, with the heat flux proportional to the difference between the surface and fluid temperatures.
Supported in partVerified against the work's full text
“the direction of transfer, and it is {{{proportional}}} to the temperature gradient, dT/dx, in”
- Consider heat conduction through a furnace or exterior building wall of thickness L: inside the wall the steady temperature obeys the (elliptic) conduction equation, the inner face is held at a known fixed temperature (a Dirichlet condition set by the interior), and the outer face loses heat to ambient air by convection — a Robin condition in which the surface flux is proportional to the temperature difference with the outside air (Newton's law of cooling)
Verification¶
Does it exist? Not checked yet. This entry carries no identifier to resolve. It was extracted from the citation as written in the article, normalized, and deduplicated against the rest of the registry.
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