Recent advances in process modifications of simultaneous saccharification and fermentation (SSF) of lignocellulosic biomass for bioethanol production

被引:20
作者
Afedzi, Alfred Elikem Kwami [1 ,2 ]
Parakulsuksatid, Pramuk [1 ,2 ]
机构
[1] Kasetsart Univ, Fac Agroind, Dept Biotechnol, 50 Ngamwongwan Rd, Bangkok 10900, Thailand
[2] Kasetsart Univ, Fac Agroind, Fermentat Technol Res Ctr, 50 Ngamwongwan Rd, Bangkok 10900, Thailand
关键词
Simultaneous saccharification and fermenta-; tion; 2G bioethanol production; SSF modification; Enzyme and yeast development; Techno-economic and life cycle assessment; BATCH SIMULTANEOUS SACCHARIFICATION; OIL PALM TRUNK; DILUTE-ACID PRETREATMENT; LIFE-CYCLE ASSESSMENT; LIQUID HOT-WATER; ETHANOL-PRODUCTION; ENZYMATIC-HYDROLYSIS; SUGARCANE BAGASSE; CO-FERMENTATION; RICE STRAW;
D O I
10.1016/j.bcab.2023.102961
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The utilization of lignocellulosic biomass for second-generation (2G) bioethanol promotes green energy. Simultaneous saccharification and fermentation (SSF) is the first integrated bioprocess for both hydrolysis and fermentation. It's designed to primarily tackle enzyme inhibition during ethanol production. However, certain limitations have led to modifications in the traditional or batch SSF process to improve overall performance and yield. Recent SSF modifications have shown significant progress, with improvements in both enzyme technology and tailored strains for SSF. This has led to more efficient hydrolysis and fermentation. Experimental work plays a crucial role in providing insights into techno-economic and life-cycle assessments. Improvements in SSF involve key factors like biomass pretreatment, enzyme characteristics, hydrolysis duration, yeast strain selection, fermentation duration, co-fermentation strategies, and the integration of multiple stages. Notably, incorporating fed-batch modes and pre-saccharification into SSF allows handling high solids loading with improved ethanol concentrations. Design principles, including the structural characterization and evaluation of a bioprocess plant, are integral to the successful modification of SSF. Plant design for ethanol production is focused on the plant configuration, equipment size, and number of units with regards to reducing the total capital investment cost. Performing techno-economic analysis and life cycle assessment shows that SSF modifications reduce the use of enzymes and chemicals, resulting in cost savings and environmental benefits. The SSF modifications hold the promise of more sustainable and economically viable biofuel production, aligning with the global transition to greener energy sources.
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页数:17
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共 126 条
[61]   Comparative life cycle assessment of first- and second-generation ethanol from sugarcane in Brazil [J].
Maga, Daniel ;
Thonemann, Nils ;
Hiebel, Markus ;
Sebastiao, Diogo ;
Lopes, Tiago F. ;
Fonseca, Cesar ;
Girio, Francisco .
INTERNATIONAL JOURNAL OF LIFE CYCLE ASSESSMENT, 2019, 24 (02) :266-280
[62]   Lignin-first biomass fractionation using a hybrid organosolv - Steam explosion pretreatment technology improves the saccharification and fermentability of spruce biomass [J].
Matsakas, Leonidas ;
Raghavendran, Vijayendran ;
Yakimenko, Olga ;
Persson, Gustav ;
Olsson, Eva ;
Rova, Ulrika ;
Olsson, Lisbeth ;
Christakopoulos, Paul .
BIORESOURCE TECHNOLOGY, 2019, 273 :521-528
[63]   Improved Cellulosic Ethanol Titres from Highly Lignified Cotton Trash Residues Using Various Batch and Fed-Batch Process Configurations [J].
McIntosh, S. ;
Palmer, J. ;
Egbuta, M. ;
Liu, L. ;
Vancov, Tony .
BIOENERGY RESEARCH, 2019, 12 (04) :1021-1032
[64]   Physicochemical Structural Changes of Poplar and Switchgrass during Biomass Pretreatment and Enzymatic Hydrolysis [J].
Meng, Xianzhi ;
Sun, Qining ;
Kosa, Matyas ;
Huang, Fang ;
Pu, Yunqiao ;
Ragauskas, Arthur J. .
ACS SUSTAINABLE CHEMISTRY & ENGINEERING, 2016, 4 (09) :4563-4572
[65]   Desirability function for optimization of Dilute Acid pretreatment of sugarcane straw for ethanol production and preliminary economic analysis based in three fermentation configurations [J].
Mesa, Leyanis ;
Martinez, Yenisleidy ;
Barrio, Edenny ;
Gonzalez, Erenio .
APPLIED ENERGY, 2017, 198 :299-311
[66]   Techno-economic evaluation of strategies based on two steps organosolv pretreatment and enzymatic hydrolysis of sugarcane bagasse for ethanol production [J].
Mesa, Leyanis ;
Lopez, Nancy ;
Cara, Cristobal ;
Castro, Eulogio ;
Gonzalez, Erenio ;
Mussatto, Solange I. .
RENEWABLE ENERGY, 2016, 86 :270-279
[67]   Repeated batches as a strategy for high 2G ethanol production from undetoxified hemicellulose hydrolysate using immobilized cells of recombinant Saccharomyces cerevisiae in a fixed-bed reactor [J].
Milessi, Thais S. ;
Perez, Caroline L. ;
Zangirolami, Teresa C. ;
Corradini, Felipe A. S. ;
Sandri, Juliana P. ;
Foulquie-Moreno, Maria R. ;
Giordano, Roberto C. ;
Thevelein, Johan M. ;
Giordano, Raquel L. C. .
BIOTECHNOLOGY FOR BIOFUELS, 2020, 13 (01)
[68]   Modelling of the Simultaneous Saccharification and Fermentation for a Pine Sawdust Biorefinery [J].
Monica Mendieta, Carolina ;
Kruyeniski, Julia ;
Esteban Felissia, Fernando ;
Cristina Area, Maria .
FERMENTATION-BASEL, 2022, 8 (03)
[69]   Optimal design of multiproduct batch plants considering duplication of units in series [J].
Moreno, Marta S. ;
Iribarren, Oscar A. ;
Montagna, Jorge M. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2009, 87 (11A) :1497-1508
[70]   Bioethanol production from rice husk under elevated temperature simultaneous saccharification and fermentation using Kluyveromyces marxianus CK8 [J].
Nachaiwieng, Woottichai ;
Lumyong, Saisamorn ;
Yoshioka, Koichi ;
Watanabe, Takashi ;
Khanongnuch, Chartchai .
BIOCATALYSIS AND AGRICULTURAL BIOTECHNOLOGY, 2015, 4 (04) :543-549