This paper addresses the problem of melt index (MI) control in the pol
ymerisation of propylene in slurry reactors. Good MI control performan
ce is usually hampered by measurement delays and a low sampling freque
ncy. The traditional solution to the control problem is to control the
hydrogen concentration in the reactor (H-2 serves as the chain transf
er agent in the reaction and therefore has a good correlation with the
MI). The H-2 concentration in the gas cap of the reactor is relativel
y easy to measure and therefore chosen to close a SISO control loop. H
owever, this concentration is not always a good measure for the H-2 co
ncentration in the slurry phase where the reactions occur. Consequentl
y, MI variations can still be large at good control of H-2 in the gas
cap. In the present paper, the use of a soft sensor for the H-2 concen
tration in the slurry phase is investigated by means of simulation. Wh
en used in combination with a model predictive control method, it is s
hown that plant performance significantly improves both at disturbance
s and at grade changes.