4.4 Article

Bench-scale fermentation for second generation ethanol and hydrogen production byClostridium thermocellumDSMZ1313 from sugarcane bagasse

Journal

Publisher

WILEY
DOI: 10.1002/ep.13516

Keywords

fermentation; bioethanol; hydrogen fermentation; fibrous bed bioreactor; lignocellulosic biomass; sugarcane bagasse

Funding

  1. Macau Science and Technology Development Fund [FDCT044/2017/AFJ]
  2. University of Macau Multi-Year Research Grant [MYRG2018-00108-FST]

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The study focuses on converting low-cost lignocellulosic biomass waste, sugarcane bagasse, into bioethanol and biohydrogen using thermophilic cellulolytic bacterium Clostridium thermocellum. Optimization of fermentation factors resulted in efficient production of ethanol and hydrogen, demonstrating the sustainability of using agricultural waste for energy production.
Exploration of eco-friendly energy resources substituting conventional fossil fuels is the real challenge globally. Prospectively, current investigation accentuates the fermentative conversion of low-cost lignocellulosic biomass waste, sugarcane bagasse (SCB) into bioethanol and biohydrogen exploiting thermophilic cellulolytic bacteriumClostridium thermocellumDSMZ 1313. Initially, the optimization of some key fermentation factors for bioethanol and biohydrogen productions was done in 150 ml serum bottles employing Taguchi orthogonal array L27 (3 13) experimental design. Results elucidated that the most suitable factors for ethanologenesis were 70 g/L cellulose, 10 g/L corn-steep liquor (CSL), 15 mg/L ferrous sulfate (FeSO4 center dot 6H(2)O), 1 g/L magnesium chloride (MgCl2 center dot 6H(2)O), pH 7, and 5 days incubation whereas for hydrogen fermentation were 60 g/L cellulose, 30 g/L CSL, 5 mg/L FeSO4 center dot 6H(2)O, 2 g/L MgCl2 center dot 6H(2)O, pH 7, and 3 days incubation. Quantitatively, 7.422 g/L ethanol and 56.891/50 ml hydrogen were produced from cellulose while 6.352 g/L ethanol and 51.685/50 ml hydrogen with H2SO4-pretreated SCB (substituted with cellulose). Scaled-up suspended-cell fermentations in bench-scale stirred-tank bioreactor resulted in 11.77% increased ethanol yield (0.239 g ethanol/g of glucose) and twofold higher hydrogen volumes (106.88 ml hydrogen/g of glucose). The employment of SCB directly as substrate for biofuels production has appeared sustainable to meet the high global energy demands.

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