Statistical optimization, kinetic modeling, and techno-economic analysis for the production of high molecular mass dextran using sugarcane industrial waste-molasses

被引:5
作者
Rahman, Sameeha Syed Abdul [1 ]
Pasupathi, Saroja [1 ]
Karuppiah, Sugumaran [2 ]
机构
[1] SASTRA Deemed Univ, Sch Chem & Biotechnol, Bioproc Engn Lab, Thanjavur, India
[2] SASTRA Deemed Univ, Ctr Bioenergy, Sch Chem & Biotechnol, Bioproc Engn Lab, Thanjavur, India
关键词
Dextran; Central-Composite design; Kinetic models; Lab-scale; Techno-economic analysis; RESPONSE-SURFACE METHODOLOGY; LEUCONOSTOC-MESENTEROIDES; SCALE-UP; GLUCAN PRODUCTION; BATCH CULTURES; GUM PRODUCTION; FERMENTATION; AERATION; AGITATION; GROWTH;
D O I
10.1016/j.biteb.2024.101902
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
This study focuses on the transformation of industrial wastes to wealth by utilizing treated sugarcane molasses (TCM) to produce dextran. The fermentation conditions for maximum dextran production were initially optimized using central-composite design in shake-flasks. The highest titer of dextran (60.0 +/- 2.0 g/L) was obtained with optimized variables of 150 g/L substrate (TCM), 12.8 g/L yeast extract, 39.8 g/L K2HPO4, 2 HPO 4 , and 48 h fermentation time. Then, the profiles of dextran production, TCM consumption, and microbial growth were fitted by kinetic models to obtain the following kinetic parameters: 0.35 h-1 maximum specific growth rate (mu max), max ), 0.48 g dextran/g substrate yield coefficient (Yps), Y p s ), 0.07 maintenance coefficient (ms), m s ), and 10.73 g product/g cell growth-associated constant (alpha). For determining the scale-up factors, the fermentation conditions were replicated in a 3 L fermenter at various stirring speeds (50-250 rpm), and a scale-up strategy based on constant P/V was used to predict the power consumption (1.88-285.51 W) for a pilot-scale of 2000 L working volume fermenter at various stirring speeds (10.8-54 rpm). The dextran produced was characterized using gel permeation chromatography to determine the molecular mass variations (3-4000 kDa) with fermentation conditions. The rheological variations of fermentation broth at different stirring speeds were also studied and related to the molecular mass of the dextran produced. Techno-economic analysis for dextran production explored a gross margin of 22.65 %, a return on investment of 16.80 %, and a pay-back time of 5.95 years.
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页数:16
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