Shopping cart ITEMS
 modern scholarly publishers in the finest tradition
Login Register
Home
Books
Journals
References
A-Z Index
Author Index
For Our Authors
User Area
Shopping Cart
Contact
Electronic Data Center

Journal of Enhanced Heat Transfer

Theory and Application in High Performance Heat and Mass Transfer 

ISSN for PRINT: 1065-5131

Institutional price:

$577.00

Issues per year:

4

For Online Access

Best Paper Award Selection - Editorial Board Site

Add subscription to shopping cart

2003, Volume10

Issue 4

  116 pages  

DOI: 10.1615/JEnhHeatTransf.v10.i4   

click 'Save as...' here to save XML metadata

Issue price - $138.00  

Add to shopping cart

  • Alternative Approach for Determining Log Mean Temperature Difference Correction Factor and Number of Shells of Shell and Tube Heat Exchangers
  • Ahmad Fakheri
    Department of Mechanical Engineering, Bradley University, Peoria, Illinois, USA


    ABSTRACT

    The challenge of enhancing or optimizing the rate of heat transfer from heat exchangers is compounded by the lack of a simple and generally applicable approach for its analysis. Because the expressions for the log mean temperature difference (LMTD) correction factor, F, or those for heat exchanger effectiveness, e, are difficult to evaluate, the traditional analysis methods rely on heat exchanger specific charts. In addition to being applicable only to a particular heat exchanger, these charts are highly nonlinear and strongly dependent on the traditional parameters used for their evaluation. Expressed in terms of the nondimensional parameters P and R, the LMTD correction factor F charts are particularly difficult to read in the steep regions. These shortcomings also make the assessment of different heat transfer enhancement strategies tedious. In this study, an alternative approach for determining F in terms of two new nondimensional parameters, r and f, is presented. This new approach results in a single general algebraic equation for determining the LMTD correction factor of multipass shell and tube heat exchangers with any number of shell passes and an even number of tube passes per shell. This single expression can be used to devise and compare different enhancement strategies for shell and tube heat exchanger networks, including their arrangement, to optimize their rate of heat transfer. It is shown that the approach presented results in a novel expression for the determination of the number of shells needed to meet a predefined overall correction factor for multishell and tube heat exchangers.

    DOI: 10.1615/JEnhHeatTransf.v10.i4.50

    Download article, 407-420 pages

    Article price - $35.00  

    Add to shopping cart

    << Previous article   Next article >>

    Designed by offsiteteam Designed by offsiteteam Designed by offsiteteam
    Begell House Inc.
    50 Cross Highway,
    Redding, CT 06896
    TEL (203) 938 1300
    FAX (203) 938 1304
    orders@begellhouse.com