4.3 Article

Encapsulated Yeast Cell-free System: A Strategy for Cost-effective and Sustainable Production of Bio-ethanol in Consecutive Batches

Journal

BIOTECHNOLOGY AND BIOPROCESS ENGINEERING
Volume 20, Issue 3, Pages 561-575

Publisher

KOREAN SOC BIOTECHNOLOGY & BIOENGINEERING
DOI: 10.1007/s12257-014-0855-1

Keywords

yeast cell-free system; encapsulation; sustainability; cofactor regeneration; cost-effectiveness

Funding

  1. Basic Science Research Program through National Research Foundation (NRF) of Korea - Ministry of Education, Science and Technology [2011-0016965]
  2. BK21 plus Korea [21A.2013-1800001]
  3. National Research Foundation of Korea [2011-0016965] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

Ask authors/readers for more resources

This study was intended to develop an encapsulated yeast cell-free system (EyCFS) by confining yeast cell-free lysate within a calcium alginate capsule. The system was evaluated for bio-ethanol production at elevated temperatures and was compared to a bare yeast cell-free system (ByCFS). Fermentation of 10 g/L glucose with shaking (150 rpm), using 2 mg/mL cell-free proteins in the ByCFS produced 3.31 g/L bio-ethanol, corresponding to 65% of the maximal theoretical yield, at 45 degrees C and pH 7.0. On the contrary, the EyCFS produced 4.12 g/L bio-ethanol, corresponding to 81% of the maximal theoretical yield, under the same experimental conditions. The EyCFS also retained 32% of its original activity after 15 consecutive batches. We observed an 11% increase in bio-ethanol production after replenishment of cofactors (ATP and NADH) and ATPase. The weight-based total turnover number (TTNw; 0.82 x 10(3)), cost ratio (R value; 1.22), and yield (80.4%) indicated the economic suitability of the EyCFS for large-scale production. Connecting the EyCFS with an encapsulated saccharification system through separate hydrolysis and fermentation (SHF) resulted in production of 4.87 g/L bio-ethanol, corresponding to 87.6% of the maximal theoretical yield. This system resolved serious limitations of conventional simultaneous saccharification and fermentation in bare cell-free systems. These data demonstrates the superiority of the proposed system in terms of thermal stability, yield, efficacy, and cost-effectiveness.

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.3
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available