By Eric M. Smith
The first aim in any engineering layout strategy should be the removing of uncertainties. In thermal layout of warmth exchangers there are almost immediately many levels within which assumptions in mathematical answer of the layout challenge are being made. Accumulation of those assumptions may perhaps introduce adaptations in layout. The fashion designer must comprehend the place those inaccuracies could come up, and try to dispose of as many resources of mistakes as attainable via identifying layout configurations that stay away from such difficulties at resource.
In this intriguing textual content, the writer adopts a numerical method of the thermal layout of warmth exchangers, extending the idea of functionality overview to the purpose the place software program should be written. the 1st few chapters are meant to supply a improvement from undergraduate reviews concerning the basics of warmth exchanger thought and the recommendations of direct sizing. Later chapters on temporary reaction of warmth exchangers and at the similar single-blow approach to acquiring experimental effects must also curiosity the working towards engineer. concept is defined easily, making sure that readers can boost their very own method of the answer of specific problems.
This booklet is an critical reference textual content for larger point (post-graduate) scholars and practising engineers, researchers and teachers within the box of warmth exchangers.
- Includes a complete new bankruptcy on exergy and strain loss
- Provides within the first few chapters a improvement from undergraduate experiences concerning the basics of warmth exchanger concept, and keeps in later chapters to debate matters corresponding to the temporary reaction of warmth exchangers and the comparable single-blow approach to acquiring experimental effects which are additionally of curiosity to the training engineer.
- Adopts a numerical method of the thermal layout of warmth exchangers, extending the idea of functionality assessment to the purpose the place software program should be written
- Contributes to the advance of the direct ‘sizing’ technique in thermal layout of the exchanger surface
- Explains concept easily, with the target that the reader can boost their very own method of the answer of specific problems
Read or Download Advances in thermal design of heat exchangers : a numerical approach : direct-sizing, step-wise rating, and transients PDF
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Additional info for Advances in thermal design of heat exchangers : a numerical approach : direct-sizing, step-wise rating, and transients
M. (1995) Design and development of the WR-21 intercooled recuperated (ICR) marine gas turbine. ASME J. Engng Gas Turbines Power, 117, July, 557-562. M. (1960) The geometry of multi-start helical coil heat exchangers. Unpublished report. M. (1986) Design of helical-tube multi-start coil heat exchangers. In Advances in Heat Exchanger Design, ASME Winter Annual Meeting, Anaheim, California, 7-12 December 1986, ASME Publication HTD-Vol. 66, pp. 95-104. M. P. (1972) Thermal performance of cross-inclined tube bundles measured by a transient technique.
With two known terminal temperatures it is then possible to solve the heat balance equations for the unknown temperatures directly in five out of six possible cases. The remaining case arises when the pinch point is at the same end as the two known temperatures. When an exchanger of this type is required, there is usually a limiting temperature for one of the unknowns. g. 9) approximately. 12. 12 Optimum temperature profiles in contraflow The paper by Grassmann & Kopp (1957) presented an analysis based on minimizing exergy loss for temperatures below the dead state TO.
Define whichever is the greater, and assume (mcCc < m/,C/j)... then (Nc > AT/,). 17) may be written Solving for effectiveness Contraflow Parallel flow These equations may be expressed in alternative form by writing (it is necessary to have W < 1) and write Afc = Ntu, then Contraflow Parallel flow The exponentials are written with negative exponents so that limiting values for effectiveness may be obtained Fundamentals 29 A special case occurs with contraflow when the water equivalents of the two flui are equal.