A new heat exchanger design procedure is presented. It can be used wit
h any existing state-of-the-art exchanger rating program. Rather than
systematically exploring the whole of the available range of exchanger
sizes (diameters and tube lengths), it determines the relationships b
etween duty and tube length, pressure drop and tube length, etc. for a
range of diameters. This information is then used to clearly indicate
the full range of geometries that are suitable for a given duty and g
iven constraints. As the example presented in the paper shows, this ca
n be achieved by undertaking very few rating calculations (typically f
our to six). Conventional design procedures can involve hundreds of su
ch calculations. The graphical representation provides the designer wi
th clear guidance regarding the influence of allowable pressure drop o
n required geometry. It can also be used to appraise rapidly the amoun
t of thermal over design introduced through the selection of a specifi
c geometry.