油棕空果束生产木糖醇和生物乙醇的整体和部分工艺

E. Mardawati, Budi Mandra Harahap, Emilda Ayu Febrianti, Agus Try Hartono, Natasha Putri Siahaan, A. Wulandari, S. Yudiastuti, S. Suhartini, Kasbawati Kasbawati
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引用次数: 3

摘要

油棕空果束(OPEFBs)在印度尼西亚非常丰富,已被强调为生物乙醇和木糖醇生产的潜在原料。然而,发酵技术将OPEFBs转化为生物乙醇和木糖醇的效果,无论是在部分(即单一生产)还是在整体(即联合生产)过程中,仍需要进一步提高。本研究旨在评价OPEFBs生产木糖醇和生物乙醇的部分和综合工艺。在集成工艺中,木糖醇提取后的剩余固体残渣由于其高纤维素化合物而被用作生物乙醇的原料。这种固体残渣更容易被纤维素酶降解为葡萄糖,并进一步转化为生物乙醇。在木糖醇生产的部分过程中,利用木聚糖酶将木聚糖水解为木糖,再利用汉斯德巴氏菌将木糖转化为木糖醇。而在生物乙醇生产的部分过程中,OPEFB中的纤维素通过纤维素酶水解成葡萄糖,然后通过酿酒酵母发酵。结果表明,部分工艺木糖醇产率(Yp/s)为0.10 g-木糖醇/g-木糖,生物乙醇产率(Yp/s)为0.32 g-生物乙醇/g-葡萄糖。该集成工艺生成木糖醇产率(Yp/s)为0.298 g-木糖醇/g-木糖,剩余固体的生物乙醇产率为0.051 g-生物乙醇/g-OPEFB(或0.078 g-生物乙醇/g-葡萄糖)。因此,这些发现证实了木糖醇与生物乙醇生产的整合工艺可能会提高OPEFB利用的高附加值产品的效率。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Integrated and partial process of xylitol and bioethanol production from oil palm empty fruit bunches
Oil palm empty fruit bunches (OPEFBs) are highly abundant in Indonesia and have been highlighted as a potential feedstock for bioethanol and xylitol production. However, the efficacy of the fermentation technology to convert OPEFBs to bioethanol and xylitol, either in partial (i.e. mono-production) or integrated (i.e. co-production) process, still needs further improvement. This study aimed to evaluate the partial and integrated process for xylitol and bioethanol production from OPEFBs. In the integrated process, the remaining solid residues after xylitol extraction are used as feedstock for bioethanol due to their high cellulose compounds. This solid residue is more susceptible to be degraded by cellulase enzymes into glucose and further transformed into bioethanol. In the partial process of xylitol production, xylanase enzyme was used to hydrolyze xylan into xylose, which was then converted into xylitol using Debaryomyces hansenii. While in the partial process of bioethanol production, the hydrolysis of cellulose in the OPEFB into glucose was carried out using cellulase enzymes, followed by fermentation using Saccharomyces cerevisiae. The results show that the partial process produced xylitol yield (Yp/s) of 0.10 g-xylitol/g-xylose, while bioethanol at yield (Yp/s) of 0.32 g-bioethanol/g-glucose, respectively. The integrated process generates xylitol yield (Yp/s)of 0.298 g-xylitol/g-xylose, with bioethanol yield from the remaining solid at 0.051 g-bioethanol/g-OPEFB (or 0.078 g-bioethanol/g-glucose). These findings, therefore, confirmed that the integrated process of xylitol with bioethanol production might offer higher efficacy of OPEFB utilization into high value-added products.
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