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本文引用的文献

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Enhanced ethanol production from sugarcane molasses by industrially engineered replacement of the gene.通过工业工程改造的基因替换提高甘蔗 molasses 的乙醇产量 。 (注:molasses 通常译为“糖蜜” ,这里按照原文未完全翻译准确,推测原文可能有拼写错误等情况 )
RSC Adv. 2020 Jan 10;10(4):2267-2276. doi: 10.1039/c9ra08673k. eCollection 2020 Jan 8.
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Direct bioethanol production from brown macroalgae by co-culture of two engineered Saccharomyces cerevisiae strains.通过两种工程化酿酒酵母菌株的共培养从褐藻中直接生产生物乙醇。
Biosci Biotechnol Biochem. 2018 Aug;82(8):1459-1462. doi: 10.1080/09168451.2018.1467262. Epub 2018 Apr 30.
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Engineering of Saccharomyces cerevisiae for the efficient co-utilization of glucose and xylose.工程化酿酒酵母以实现葡萄糖和木糖的高效共利用。
FEMS Yeast Res. 2017 Jun 1;17(4). doi: 10.1093/femsyr/fox034.
4
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Bioresour Technol. 2016 Feb;202:231-7. doi: 10.1016/j.biortech.2015.12.025. Epub 2015 Dec 14.
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Selection of the best chemical pretreatment for lignocellulosic substrate Prosopis juliflora.选择最佳的木质纤维素基质 Prosopis juliflora 的化学预处理方法。
Bioresour Technol. 2013 May;136:542-9. doi: 10.1016/j.biortech.2013.03.053. Epub 2013 Mar 16.
6
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Bioresour Technol. 2013 Mar;131:508-14. doi: 10.1016/j.biortech.2012.12.135. Epub 2013 Jan 10.
7
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Carbohydr Polym. 2013 Jan 16;91(2):646-50. doi: 10.1016/j.carbpol.2012.08.019. Epub 2012 Aug 13.
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Saccharomyces cerevisiae engineered for xylose metabolism requires gluconeogenesis and the oxidative branch of the pentose phosphate pathway for aerobic xylose assimilation.经过基因工程改造以代谢木糖的酿酒酵母需要糖异生和戊糖磷酸途径的氧化分支来进行有氧木糖同化。
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9
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Bioresour Technol. 2011 Jun;102(11):6473-8. doi: 10.1016/j.biortech.2011.03.019. Epub 2011 Mar 16.
10
Bioconversion of Saccharum spontaneum (wild sugarcane) hemicellulosic hydrolysate into ethanol by mono and co-cultures of Pichia stipitis NCIM3498 and thermotolerant Saccharomyces cerevisiae-VS₃.毕赤酵母 NCIM3498 单菌和耐热酿酒酵母-VS₃混菌对甜高粱秸秆稀酸水解液的生物转化生产乙醇
N Biotechnol. 2011 Oct;28(6):593-9. doi: 10.1016/j.nbt.2010.12.002. Epub 2010 Dec 23.

(VS3)和(NCIM 3498)的共培养提高了浓缩水解产物的生物乙醇产量。

Co-culture of (VS3) and (NCIM 3498) enhances bioethanol yield from concentrated hydrolysate.

作者信息

Naseeruddin Shaik, Desai Suseelendra, Venkateswar Rao L

机构信息

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.

出版信息

3 Biotech. 2021 Jan;11(1):21. doi: 10.1007/s13205-020-02595-6. Epub 2021 Jan 3.

DOI:10.1007/s13205-020-02595-6
PMID:33442519
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC7779385/
Abstract

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.

摘要

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。