Counterflow logarithmic mean temperature difference is actually the upper bound: A demonstration

Abstract The logarithmic mean temperature difference (ΔT LM or LMTD) is a corner stone concept used in the design and analysis of heat transfer equipment, such as heat exchangers. The LMTD methods are well established in the Chemical Engineering framework and, in general, apply a counterflow LMTD corrected by some factor to assess the “true” mean temperature difference between the fluids exchanging heat. The counterflow LMTD is used because it is undoubtedly believed that its value for two countercurrent streams is higher than when the same streams are arranged in concurrent flow. Although this principle may be supported by direct comparison between the counterflow and parallel flow LMTD’s for any given process conditions, a demonstration of its universal validity is not found in the literature. This article presents a proof founded in mathematical and physical arguments that this belief is indeed a fact.

[1]  A. O. Pittenger The Logarithmic Mean in n Variables , 1985 .

[2]  X. X. Zhu,et al.  Pressure drop considerations for heat exchanger network grassroots design , 2002 .

[3]  Frank Pettersson Heat exchanger network design using geometric mean temperature difference , 2008, Comput. Chem. Eng..

[4]  Ignacio E. Grossmann,et al.  Simultaneous optimization models for heat integration—II. Heat exchanger network synthesis , 1990 .

[5]  B. C. Carlson The Logarithmic Mean , 1972 .

[6]  K. Stolarsky,et al.  The Power and Generalized Logarithmic Means , 1980 .

[7]  R. A. Bowman Mean Temperature Difference Correction in Multipass Exchangers , 1936 .

[8]  John J.J. Chen Comments on improvements on a replacement for the logarithmic mean , 1987 .

[9]  Juan M. Zamora,et al.  A global MINLP optimization algorithm for the synthesis of heat exchanger networks with no stream splits , 1998 .

[10]  W. M. Nagle Mean Temperature Differences in Multipass Heat Exchangers , 1933 .

[11]  J. M. García,et al.  A hybrid methodology for detailed heat exchanger design in the optimal synthesis of heat exchanger networks , 2006 .

[12]  R. Mukherjee,et al.  Effectively design shell-and-tube heat exchangers , 1998 .

[13]  A. Colburn,et al.  Mean Temperature Difference and Heat Transfer Coefficient in Liquid Heat Exchangers , 1933 .

[14]  Donald Quentin Kern,et al.  Process heat transfer , 1950 .

[15]  Yusuf Ali Kara,et al.  A computer program for designing of shell-and-tube heat exchangers , 2004 .

[16]  Mauro A.S.S. Ravagnani,et al.  A MINLP Model for the Rigorous Design of Shell and Tube Heat Exchangers Using the Tema Standards , 2007 .

[17]  Tung-Po Lin,et al.  The Power Mean and the Logarithmic Mean , 1974 .

[18]  William R. Paterson,et al.  A replacement for the logarithmic mean , 1984 .

[19]  Ming-Tsun Ke,et al.  The log mean heat transfer rate method of heat exchanger considering the influence of heat radiation , 2009 .

[20]  E. B. Leach,et al.  Extended Mean Values , 1978 .