This paper addresses alternative control strategies for a supercritica
l fluid extraction (SFE) process. Alternative control strategies are g
enerated by applying different plant decompositions for the SFE proces
s to produce a decentralised controller for the whole process. Two tec
hniques of plant decomposition are introduced, based on physical unit
operations and based on process dynamics. Screening alternative plant
decompositions are then performed by observing two indicators: the gap
and the maximum stability margin b(max). These indicators are also us
eful for deciding a ''realistic'' performance specification for each s
ubsystem. This study shows that the performance of a control strategy
depends on how the SFE process is decomposed and how the performance s
pecifications are posed in each subsystem. Hence, the ''best'' control
strategy for the SFE process can be determined in a systematic manner
by combining the ''best'' plant decomposition with a ''realistic'' pe
rformance specification for each subsystem. As a result, two control s
chemes are selected as alternative control strategies for the SFE proc
ess rather than the use of a centralised controller.