Engineering Heat Transfer

Webb, R. L. Air-side heat exchanger in finned tube heat exchangers. Heat Transfer Engineering 1 (1980) 3, pp. 3.3-19. 

Figure 10-73. Shell-side pressure loss for 3 shell-side baffle configurations—RODbaffles . (Used by permission Small, W. M., and Young, R. K. Heat Transfer Engineering, V. 2, 1979. Taylor and Francis, Inc., Philadelphia, PA. All rights reserved.)...

Butterworth, D. (1977) Introduction to Heat Transfer, Engineering Design Guide No. 18 (Oxford U.P.). 

CHEN-CHIA, H. and Fair, J. R. (1989) Heat Transfer Engineering, 10 (2) 19. Direct-contact gas-liquid heat transfer in a packed column. 

For practical purposes, heat-transfer engineers often use empirical or semi-empirical correlations to predict h values. These formulations are usually based on the dimensionless numbers described before. In this case, the appropriate formulation should be used to prevent significant errors. If dimensionless correlations are applicable under conditions of gas extraction, then heat-transfer coefficients can be determined from these correlations and the influence of parameter variations may be derived also from them. 

Dimensionless numbers help in convection heat transfer engineering Used to compare relative values in the practice of engineering In convection, there is the Eckert number and the Prandtl number, There is also the Reynolds number, Peclet number and Nusselt number. 

S. Kandlikar. An extension of the flow boiling correlation to transition, laminar, and deep laminar flows in minichannels and microchannels . Heat Transfer Engineering, 25, 3, pp. 86-93 (2004). 

S. Kandlikar and W. Grande. Evolution of microchannel flow passages — thermohydraulic performance and fabrication technology . Heat Transfer Engineering, 25, pp. 3-17 (2003). 

D. Steiner and J. Taborek. Flow boiling heat transfer in vertical mbes correlated by an asymptotic model . Heat Transfer Engineering, 13, 2, pp. 43-69 (1992). 

Vasiliev, L.L., Zhuravlyov, A.S., Novikov, M.N., and Vasiliev L.L. Jr., (2000) Experimental Investigation of Propane Boiling in Porous Structures, Proceedings of The TV Minsk International Seminar Heat Pipes, Heat Pumps, Refrigerators , Minsk, Belarus, pp. 245-255. Vasiliev, L.L., Zhuravlyov, A.S., Novikov, M.N., Shapovalov, A.V., and Litvinenko, V.V. (2003) Heat Transfer at Propane Pool Boiling and Evaporation in Capillary-Porous Evaporators Proceedings of The 4th Baltic Heat Transfer Conference Advances in Heat Transfer Engineering", Kaunas, Lithuania, pp. 739-746. 

A great amount of proprietary research has been conducted by a few companies into the workings of helical baffled heat exchangers. The only known open literature method for estimating helical baffle performance has been Comparison of Correction Factors for Shell-and-Tube Heat Exchangers with Segmental or Helical Baffles by Stehlik, Nemcansky, Krai, and Swanson [Heat Transfer Engineering, 15(1), 55-65]. 

Steiner, D., andTaborek, J., Elow Boiling Heat Transfer in Vertical Tubes Correlated by an Asymptotic Model, Heat Transfer Engineering 13 (2), 43 (1992). 

Krai, D., Stehfik, P., Van der Ploeg, H. J., and Master, B. I., Helical Baffles in Shell-and-Tube Heat Exchangers, Part I Experimental Verification, Heat Transfer Engineering 17 (1), 93-101 (1996). American Petroleum Instimte, API Standard 662, Plate Heat Exchangers for General Refinery Services, API, Washington, DC, 2002. 

G. Croce, P. D Agaro, and A. Filippo, Compressibility and rarefaction effects on pressure drop in rough microchannels. Heat Transfer Engineering 28, 688-695 (2007). 

F.V. Castelloes, C.R. Cardoso, P. Couto, and R.M. Cotta, Transient Analysis of Slip Flow and Heat Transfer in Microchannels, Heat Transfer Engineering, Vol. 28, 549-558 (2007). 

Kandlikar, S. G., and Balasubramanian, P., An Extension of the Flow Boihng Correlation to Transition, Laminar, and Deep Laminar Flows in Mini-Channels and Micro-Chaimels, Heat Transfer Engineering, 25(3), 86—93 (2004). 

Revellin, R. and Thome, J.R., Critical Heat Flux during Flow Boiling in Microchaimels A Parametric Study, Heat Transfer Engineering, 30, 556-563, (2009). 

R. L. Webb, Performance, Cost Effectiveness and Water Side Fouling Considerations of Enhanced Tube Heat Exchangers for Boiling Service With Tube-Side Water Flow, Heat Transfer Engineering (3/3-4) 84-98,1982. 

D. C. Groeneveld, S. C. Cheng, and T. Doan, The CHF Look-Up Table, A Simple and Accurate Method for Predicting Critical Heat Flux, Heat Transfer Engineering (7) 46-62,1986. 

Song, T.-H. "Spectral Remote Sensing for Furnaces and Flames," Heat Transfer Engineering 29, no. 4 (2008) 417-28. 

In Advances in Heat Transfer Engineering, edited by B. Sunden and J. Vilemas, 143-58, New York Begell House, 2003. 

Although a study of liquid solidification in static systems is of interest, and gives some insight into the physical behaviour of freezing at a solid surface, the more complex situation that prevails in flowing systems is of more interest to the heat transfer engineer. 

Simple Formulas for thermophysical Properties of Liquid Water for Heat Transfer Calculations heat transfer engineering 19(1998)87-101. 

Overall conductance (overall heat-transfer coefficient) n. In heat-transfer engineering, the reciprocal of the total thermal resistance, for heat flow through plane walls or tube walls. It is defined by the equation U = q/AAT, where q is the rate of heat flow through (and normal to) the surface of area A, and AT is the fall in temperature through the layer in the direction of q. This is a modification of Fomier s law, invented to deal conveniently with heat flow through stagnant fluid films adjacent... 

U yii . (1) Chemical symbol for the element uranium. (2) In heat-transfer engineering symbol for overall conductance. 

Webb, R. L., "Nucleate Boiling On Porous Coated Surfaces", Heat Transfer Engineer-... 

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