The objective of the present work was to optimize the
operating
conditions (P, T cosolvent %) and to study the scale-up and the feasibility
of the supercritical fluid extraction (SFE) process for polyphenols
from grape pomace, the main solid byproduct of the wine industry.
Pilot-scale equipment (1 L extraction vessel) was used to study the
scale-up prediction for extraction vessels of 50, 100, 500, and 1000
L capacity. The adopted scale-up criteria consisted of maintaining
and keeping constant the solvent mass-to-feed mass ratio and the bed
geometry dimension. The results indicated an excellent predictive
level obtained by Sovová’s model and success of the
adopted scale-up criteria. At industrial scale, yields were close
to 2.3 g
GAE
/100 g
DM
, a value obtained using
the pilot-scale equipment. High concentrations of high-added-value
phenols such as
cis
-resveratrol glucoside,
cis
-coutaric acid,
trans
-
p
-coumaric acid, quercetin, and proanthocyanidins were found in the
extract. An economic evaluation of the process indicated the feasibility
of an industrial SFE plant with a capacity of 500 L for producing
in 60 min an extract with an expected phenolics’ concentration
of approximately 133 g
GAE
/kg
extract
at an estimated
67€ /kg
extract
cost of manufacturing. Notably, all
values are better than those currently reported in the literature.