4.6 Article

Enhanced High-Solids Fed-Batch Enzymatic Hydrolysis of Sugar Cane Bagasse with Accessory Enzymes and Additives at Low Cellulase Loading

Journal

ACS SUSTAINABLE CHEMISTRY & ENGINEERING
Volume 6, Issue 10, Pages 12787-12796

Publisher

AMER CHEMICAL SOC
DOI: 10.1021/acssuschemeng.8b01972

Keywords

Atmospheric glycerol organosolv-pretreated; Sugar cane bagasse; High solids content; Enzymatic hydrolysis; Low enzyme loading; Additive and accessory enzyme

Funding

  1. National Natural Science Foundation of China [21776114, 21176106]
  2. Jiangsu Provincial Natural Science Foundation of China [BK20181347]
  3. Jiangsu Province Six Talent Peak [XNY-010]
  4. China Postdoctoral Science Foundation [2016T90419]
  5. National First-Class Discipline Program of Light Industry Technology and Engineering [LITE2018-01]
  6. 111 Project [111-2-06]
  7. Jiangsu Province Collaborative Innovation Center for Advanced Industrial Fermentation Industry Development Program

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High cellulase loading is still a major impediment in the production of fermentative sugars from high-solids enzymatic hydrolysis of lignocellulosic substrates in the enzyme-based biorefinery industry. This study attempted a high-solids (20%) enzymatic hydrolysis of lignocellulosic substrate at a very low cellulase loading with mixed use of additives and accessory enzymes by fed-batch mode. To avoid the high initial biomass viscosity, the high-solids enzymatic hydrolysis of lignocellulosic substrates was initiated with a solids content of 8%. Thereafter, 4% of the additional substrates were consecutively fed into the hydrolysis system after 6, 12, and 18 h to reach a final solids content of 20%. Some additive mixtures (40 mg/g substrateTween 80 + 10 mg/g substrate tea saponin +20 mg/g substrate BSA) were observed to enable this fed-batch hydrolysis to increase 30% of the glucose yield after the 48 h. The combination of these additives and accessory enzymes (2.4 mg/g substrate xylanase and g substrate AA9) in the high-solids hydrolysis system further boosted the sugar release. This allowed us to achieve an industrially relevant sugar yield (83% cellulose and 90% xylan hydrolysis) and fermentable sugar titer (similar to 160 g/L) after 72 h, with a low cellulase enzyme loading (3 FPU/g substrate). Our results indicate that the fed-batch substrate addition process is a favorable model for high-solids enzymatic hydrolysis of lignocellulosic substrates. Moreover, the synergism between the additives and accessory enzymes can greatly boost the high-solids enzymatic hydrolysis of lignocellulosic substrates.

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