This study is on the efficient fermentation
of high glucose (G)
and xylose (X) levels (G/X ratio of 1.5:1), simulating the hydrolysate
of lignocellulosic wastes, via an innovative integrated two-stage
fermentation–pervaporation process. Immobilized Zymomonas
mobilis (Z) and Pichia stipitis (P) were
exploited in a sequential-co-immobilized culture (Z in the first stage
and Z and P in second stage) to simultaneously increase bioethanol
productivity and lessen the inhibitions. The threshold inhibition
was evaluated in 100 mL shake flasks by raising the initial total
sugar concentration from 50 to 200 g/L where complete inhibition was
observed at 200 g/L. Subsequently, fermentation (G: 120 g/L, X: 80
g/L) was examined in a sequential-co-immobilized two-sectional bioreactor
(ITB-2L) during 200 h. ITB resulted in 100% glucose and 16% xylose
conversion, showing ethanol productivity of 0.26 g/L·h and yield
of 0.4 ge/gs. To investigate the effect of reducing
inhibitions, a tubular superhydrophobic silicalite-1/PDMS pervaporative
(TSP) autoclavable membrane with antiswelling properties was fabricated.
The pervaporative sequential-co-immobilized two-sectional bioreactor
(PITB) using TSP enhanced xylose conversion (57%), ethanol productivity
(0.39 g/L·h), and yield (0.47 ge/gs). The
membrane surface was probed after 161 h of usage, and the limited
presence of only negative ions on its surface proved its superior
ultralow fouling–biofouling formation. PITB proved itself as
a robust integrated process for the second-generation bioethanol production.