Naseeruddin Shaik, Desai Suseelendra, Venkateswar Rao L
Research Scholar and Professor Emeritus, Respectively, Department of Microbiology, Osmania University, Hyderabad, 500007 India.
Principal Scientist, ICAR-Central Research Institute for Dry Land Agriculture, Santoshnagar, Hyderabad, 500059 India.
3 Biotech. 2021 Jan;11(1):21. doi: 10.1007/s13205-020-02595-6. Epub 2021 Jan 3.
Biphasic acid hydrolysates and enzymatic hydrolysates from carbohydrate-rich , an invasive perennial deciduous shrub of semi-arid regions, were used for bioethanol production. and were used for fermentation of hexoses and pentoses. acid hydrolysate with an initial sugar concentration of 18.70 ± 0.16 g/L was concentrated to 33.59 ± 0.52 g/L by vacuum distillation. The concentrated hydrolysate was pretreated and fermented by mono- and co-culture methods either singly or in combination with enzyme hydrolysate and ethanol yields were compared. Monoculture with (VS3) and (NCIM3455) yielded maximum ethanol of 36.6 ± 1.83 g/L and 37.1 ± 1.86 g/L with a fermentation efficiency of 83.94 ± 4.20% and 84.20 ± 4.21%, respectively, after 36 h of fermentation. The ethanol yield obtained was 0.428 ± 0.02 g/g substrate and 0.429 ± 0.02 g/g substrate with a productivity of 1.017 ± 0.051 g/L/hand 1.031 ± 0.052 g/L/h, respectively. (NCIM3498) yielded maximum ethanol of 24 g/L with ethanol yield of 0.455 ± 0.02 g/g substrate and a productivity of 1.004 ± 0.050 g/L/h after 24 h of fermentation. With concentrated acid hydrolysate as substrate, (VS3) produced ethanol of 8.52 ± 0.43 g/L, whereas (NCIM3455) produced 5.96 ± 0.30 g/L of ethanol. (NCIM3498) produced 4.52 ± 0.23 g/L of ethanol by utilizing 14.66 ± 0.87 g/L of sugars. Co-culture with (VS3) addition after 18 h of addition of (NCIM3498) to the mixture of concentrated acid hydrolysate and enzyme hydrolysate produced 13.86 ± 0.47 g/L of ethanol with fermentation efficiency, ethanol yield and productivity of 87.54 ± 0.54%, 0.446 ± 2.36 g/g substrate and 0.385 ± 0.014 g/L/h, respectively. Hence, it is concluded that co-culture with and is feasible, further scaling up of fermentation of substrate for bioethanol production.
从一种半干旱地区的入侵性多年生落叶灌木(富含碳水化合物)中获得的双相酸水解产物和酶水解产物被用于生物乙醇生产。[具体微生物名称1]和[具体微生物名称2]被用于己糖和戊糖的发酵。初始糖浓度为18.70±0.16 g/L的酸水解产物通过真空蒸馏浓缩至33.59±0.52 g/L。将浓缩后的水解产物进行预处理,并通过单培养和共培养方法单独或与酶水解产物结合进行发酵,比较乙醇产量。用[具体微生物名称1](VS3)和[具体微生物名称2](NCIM3455)进行单培养,发酵36小时后,分别产生最大乙醇量36.6±1.83 g/L和37.1±1.86 g/L,发酵效率分别为83.94±4.20%和84.20±4.21%。获得的乙醇产量分别为0.428±0.02 g/g底物和0.429±0.02 g/g底物,生产率分别为1.017±0.051 g/L/h和1.031±0.052 g/L/h。[具体微生物名称3](NCIM3498)发酵24小时后产生最大乙醇量24 g/L,乙醇产量为0.455±0.02 g/g底物,生产率为1.004±0.050 g/L/h。以浓缩酸水解产物为底物,[具体微生物名称1](VS3)产生8.52±0.43 g/L乙醇,而[具体微生物名称2](NCIM3455)产生5.96±0.30 g/L乙醇。[具体微生物名称3](NCIM3498)利用14.66±0.87 g/L的糖产生4.52±0.23 g/L乙醇。在将[具体微生物名称3](NCIM3498)添加到浓缩酸水解产物和酶水解产物的混合物中18小时后添加[具体微生物名称1](VS3)进行共培养,产生13.86±0.47 g/L乙醇,发酵效率、乙醇产量和生产率分别为87.54±0.54%、0.446±2.36 g/g底物和0.385±0.014 g/L/h。因此,可以得出结论,[具体微生物名称1]和[具体微生物名称3]的共培养是可行的,可进一步扩大用于生物乙醇生产的[底物名称]发酵规模。