4.7 Article

Wastes recycling of non-sterile cellulosic ethanol production from low-temperature pilot-scale enzymatic saccharification of alkali-treated sugarcane bagasse

Journal

JOURNAL OF CLEANER PRODUCTION
Volume 374, Issue -, Pages -

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.jclepro.2022.134019

Keywords

Lignocellulose; Alkaline pretreatment; Black liquor; Saccharomyces cerevisiae; Mass balance; Energy flow

Funding

  1. National Key R&D Program of China, China [2019YFB1503802, 2019YFB1503801]
  2. Guangdong Basic and Applied Basic Research Foundation, China [2020A1515011012]
  3. National Natural Science Foundation of China, China [51976224, 52006227]
  4. Key Fundamental Research Project of Guangdong-Guangxi Joint Funding, China [2020B1515420005]
  5. Science and Technology Planning Project of Guangdong Province, China [2020A1010020024]
  6. Youth Innovation Promotion Association, CAS, China [2021351]
  7. Pearl River S&T Nova Program of Guangzhou, China [201806010052]

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High energy consumption is a major obstacle for the conversion of lignocellulose into biofuels and biochemicals. In this study, a self-designed pilot-scale device with recycling of black liquor and waste washing water was used for low-temperature pretreatment and high-solid enzymatic hydrolysis of sugarcane bagasse. The results showed that the enzymatic hydrolysis of the treated sugarcane bagasse achieved a high glucose concentration and glucan conversion. A low-energy strategy for cellulosic ethanol production with low emission was proposed.
High energy consumption has been one of bottlenecks for bioconversion of lignocellulose into biofuels and biochemicals. A self-designed pilot-scale device with recycling of black liquor (BL) and waste washing water (WWW) was constructed to conduct low-temperature pretreatment and high-solid enzymatic hydrolysis of sugarcane bagasse (SCB) at ordinary atmospheric pressure. Results showed that enzymatic hydrolysis of WWWwashed BL-WWW-NaOH-treated SCB at 30% solid concentration for 72 h achieved 91.59 g/L glucose with glucan conversion of 70.94%. The pretreatment unit shared only 19.68%-22.43% of total energy consumption and 8.32%-8.81% of total cost. The non-sterile enzymatic hydrolysate could be directly fermented by BL-adapted yeasts to maximally produce 44.82 g/L ethanol at 48 h, while the sterile hydrolysate could not be fermented. 2,3-dihydro-3,5-dihydroxy-6-methyl-4H-pyran-4-one, furancarboxaldehyde and 5-hydroxymethylfurfural might be the dominant inhibitors in the sterile enzymatic hydrolysate for ethanol production. Finally, a low-emission strategy for cellulosic ethanol production with low energy consumption was proposed.

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