The importance of integration in process plant design has long been re
cognised. This is evidenced for example, by the existence of complex h
eat and power networks in modern production sites. These networks repr
esent site-wide integration. They usually allow process heating duties
in several processes to be effected at low cost by using turbine pass
-out steam after obtaining a credit for power generated in a central t
urbine. When looking for energy saving in retrofit projects, an instal
led heat and power network of this type usually introduces a counter-p
roductive element. a reduction in steam heating duties leads to a redu
ction in turbine pass-out steam which, In turn, leads to a reduction i
n power generation. This makes optimisation of the process slow and op
timisation of the process in the site context two rather different tas
ks. More complications are given through other more general reflectors
across a site. A modern processing plant such as ethylene, for instan
ce, is usually linked into the overall site and interacts with other p
lants through several utilities, not just back pressure steam. This ma
kes it necessary to not only understand the fundamental process demand
s but also to analyse these demands in the site context. Process licen
sors will usually prefer to consider standard designs for individual p
rocesses. The best project, on the other hand, will almost invariably
be site dependent. This article highlights the distinction between the
application of process integration techniques-in particular pinch tec
hnology-within an individual process and their wider application in th
e overall site context The ''counter productive'' aspect of heat savin
gs in the context of isntalled heat and power networks Is given attent
ion. In addition to energy, the article discusses yields, flexibility
and capital cost savings.