For planning the start-up procedure of a pipeline under realistic condition
s the cool-down or warm-up behaviour should be known in advance. The relati
on between the cool-down or warm-up time and the mass-flow rate in the pipe
line should be known in particular. Based on heat balances theoretical rela
tions had been derived to enable appropriate estimations. These derived the
oretical relations are also valid for the cool-down or warm-up of packed be
ds used as heat accumulators, e.g., in regenerators. A simple experimental
method is suggested to determine the heat transfer coefficient in a packed
bed using the theoretical relation for the gas temperature as a function of
time and length. As all variables in the formulae are dimensionless, norma
lized diagrams have been developed, which are valid for all the cases discu
ssed. (C) 2001 Elsevier Science Ltd. All rights reserved.