ENZYME-ENGINEERING, MEDIUM-ENGINEERING, AND REACTION-ENGINEERING TO DESIGN A LOW-COST, SELECTIVE PRODUCTION METHOD FOR MONOOLEOYLGLYCEROLS AND DIOLEOYLGLYCEROLS
Ja. Arcos et C. Otero, ENZYME-ENGINEERING, MEDIUM-ENGINEERING, AND REACTION-ENGINEERING TO DESIGN A LOW-COST, SELECTIVE PRODUCTION METHOD FOR MONOOLEOYLGLYCEROLS AND DIOLEOYLGLYCEROLS, Journal of the American Oil Chemists' Society, 73(6), 1996, pp. 673-682
The selective enzymic production of mono- and diolein (MO, DO) was opt
imized at high yields. A comparative study of the following distinct e
nzymic reactions was conducted: ethyl oleate glycerolysis, triolein (T
O) glycerolysis, and direct esterification. Solvent-free systems were
compared with media that contained different solvents. Native, modifie
d (with polyethylene glycol), and immobilized lipases were used. Mecha
nical resistance, the support effect on enzyme and glycerol dispersion
and on process reproducibility, and hydrophilicity of the support wer
e considered in the process optimization. We report the use of an immo
bilized lipase on an inorganic support (Celite), which has high activi
ties in both solid-phase glycerolysis (99% reaction conversion) and es
terification (100% conversion). The optimum conditions for the distinc
t reactions were compared by considering their selectivities, conversi
ons, yields, and cost of the substrates. We found less costly and more
selective processes in the absence of solvents for glycerolysis of tr
iolein and direct esterification. Although glycerolysis was the most i
nteresting process to produce diolein, esterification was better for m
onoolein preparation with this biocatalyst. The esterification reactio
n yielded 93 wt% of MO, in the absence of either TO or oleic acid (OA)
, at low cost because of the 100% reaction conversion. Similar costs o
f the substrates (10.6 and 10.1 $/g) were necessary to obtain 67 and 8
0 wt% of DO in esterification and glycerolysis, respectively. The glyc
erolysis conversion was 96%. In esterification, the product mixture wa
s impure, with a high amount of residual OA due to the low conversion
(59%). The high activity of PSL-Celite in these solid-phase reactions
has an advantage over the reactions with non immobilized-lipases due t
o the ease of enzyme recovery. The absence of organic solvents reduces
the need for solvent removal from the reaction mixtures.