Table 3.
Comparison of simultaneous saccharification and fermentation methods using SO2 pretreatment of softwoods with Saccharomyces cerevisiae strains
| Yeast straina | Wood type | Pretreatmentb | Solids, % dry weight/volume | Inoc, g/L | Cellulase, FPU/gram dry weight | Max EtOH, g/L | Time to maximum EtOH production, hours | % TM | Reference | ||
|---|---|---|---|---|---|---|---|---|---|---|---|
| SO2 conc. | Reaction temp, °C | Duration, min | |||||||||
| Tembec 1 | Lodgepole pine | 4.0 | 200 | 5 | 5% (washed) | 5 | 40 FPU/g cellulase, 20 CU/g cellobiase | 17.0 | 24 | 68c | Ewanick et al. [36] (note: 6 hours enzyme preincubation) |
| Tembec 1 | Douglas fir | 4.5 | 195 | 4.5d | 40 mL, WSF | 5 | No enzymes added | 13.8 | 24 | 87e | Keating et al. [37] |
| Y-1528 | Douglas fir | 14.7 | 24 | 92f | |||||||
| Baker's yeast | Spruce | 2.5 | 215 | 5 | 8% | 5 | 32 FPU/g cellulase, 28 IU/g cellobiase | Not stated | 72 | 60f | Alkasrawi et al. [25] |
| Baker's yeastg | 72 | 92f | |||||||||
| TMB 3000 | 48 | 89f | |||||||||
| Baker's yeast | Spruce | 3.0 | 215 | 5 | 5% | 5 | 15 FPU/g cellulose, 23 CU/g cellobiase | Not stated | 24 | 49f | Söderström et al. [35] |
| Baker's yeast | Spruce | 3.0 | 210 | 5 | 12% WIS | 5 | 15 FPU/g cellulose, 23 CU/g cellobiase | 20.0 (graph) | 72 | 37f | Hoyer et al. [38] |
| XR122N | Pine | 3.3 | 215 | 5 | 10% | 4 | 15 FPU/g cellulose, 60 CU cellobiase | 28.7 | 48 | 98c | This study |
| XR122N | Pine | 3.3 | 215 | 5 | 12% | 4 | 15 FPU/g cellulose, 60 CU cellobiase | 23.6 | 48 | 76c | This study |
Abbreviations: FPU, filter paper unit; Inoc, inoculation; CU, cellobiase unit; temp, temperature; WIS, water-insoluble solids; WSF, water-soluble fraction.
aSaccharomyces.
bAll biomass was pretreated with SO2 in a single step and was not delignified before pretreatment or fermentation.
cTheoretical yield based on cellulose and hemicellulose content derived from gravimetric and analytical analyses of pretreated material.
dSteam explosion output was diluted to 15% w/w and filtered, and the pH altered to 6.0. Suspended solids not filtered out.
eTheoretical yield was based on the content of glucose and mannose in the pretreated material.
fTheoretical yield was based on the content of glucose and mannose in the liquid and of glucan in the solid material.
gIn hydrolysate.