Novak Mario, Marđetko Nenad, Trontel Antonija, Pavlečić Mladen, Kelemen Zora, Perković Lucija, Petravić Tominac Vlatka, Šantek Božidar
University of Zagreb Faculty of Food Technology and Biotechnology, Department of Biochemical Engineering, Laboratory of Biochemical Engineering, Industrial Microbiology, Malting and Brewing Technology, Pierottijeva 6, 10000 Zagreb.
Food Technol Biotechnol. 2024 Mar;62(1):89-101. doi: 10.17113/ftb.62.01.24.8230.
An innovative integrated bioprocess system for bioethanol production from raw sugar beet cossettes (SBC) and arabitol from remaining exhausted sugar beet cossettes (ESBC) was studied. This integrated three-stage bioprocess system is an example of the biorefinery concept to maximise the use of raw SBC for the production of high value-added products such as sugar alcohols and bioethanol.
The first stage of the integrated bioprocess system was simultaneous sugar extraction from SBC and its alcoholic fermentation to produce bioethanol in an integrated bioreactor system (vertical column bioreactor and stirred tank bioreactor) containing a high-density suspension of yeast (30 g/L). The second stage was the pretreatment of ESBC with dilute sulfuric acid to release fermentable sugars. The resulting liquid hydrolysate of ESBC was used in the third stage as a nutrient medium for arabitol production by non- yeasts ( CBS 10155 and CBS 11463).
The obtained results show that the efficiency of bioethanol production increased with increasing temperature and prolonged residence time in the integrated bioreactor system. The maximum bioethanol production efficiency (87.22 %) was observed at a time of 60 min and a temperature of 36 °C. Further increase in residence time (above 60 min) did not result in the significant increase of bioethanol production efficiency. Weak acid hydrolysis was used for ESBC pretreatment and the highest sugar yield was reached at 200 °C and residence time of 1 min. The inhibitors of the weak acid pretreatment were produced below bioprocess inhibition threshold. The use of the obtained liqiud phase of ESBC hydrolysate for the production of arabitol in the stirred tank bioreactor under constant aeration clearly showed that CBS 10155 with 8.48 g/L of arabitol (=0.603 g/g and bioprocess productivity of 0.176 g/(Lh)) is a better arabitol producer than CBS 10155.
An innovative integrated bioprocess system for the production of bioethanol and arabitol was developed based on the biorefinery concept. This three-stage bioprocess system shows great potential for maximum use of SBC as a feedstock for bioethanol and arabitol production and it could be an example of a sustainable 'zero waste' production system.
研究了一种创新的集成生物工艺系统,用于从生甜菜丝(SBC)生产生物乙醇以及从剩余的耗尽甜菜丝(ESBC)生产阿拉伯糖醇。这种集成的三阶段生物工艺系统是生物精炼概念的一个实例,旨在最大限度地利用生SBC来生产高附加值产品,如糖醇和生物乙醇。
集成生物工艺系统的第一阶段是在含有高密度酵母悬浮液(30 g/L)的集成生物反应器系统(立式柱生物反应器和搅拌罐生物反应器)中同时从SBC提取糖分并进行酒精发酵以生产生物乙醇。第二阶段是用稀硫酸对ESBC进行预处理以释放可发酵糖。所得的ESBC液体水解产物在第三阶段用作非酵母(CBS 10155和CBS 11463)生产阿拉伯糖醇的营养培养基。
所得结果表明,在集成生物反应器系统中,生物乙醇生产效率随着温度升高和停留时间延长而提高。在60分钟和36°C的温度下观察到最大生物乙醇生产效率(87.22%)。停留时间进一步增加(超过60分钟)并未导致生物乙醇生产效率显著提高。采用弱酸水解对ESBC进行预处理,在200°C和1分钟的停留时间下达到最高糖产率。弱酸预处理产生的抑制剂低于生物工艺抑制阈值。在持续曝气的搅拌罐生物反应器中,将所得的ESBC水解液液相用于生产阿拉伯糖醇,结果清楚表明,产阿拉伯糖醇8.48 g/L(=0.603 g/g,生物工艺生产力为0.176 g/(L·h))的CBS 10155比CBS 11463更适合生产阿拉伯糖醇。
基于生物精炼概念开发了一种创新的用于生产生物乙醇和阿拉伯糖醇的集成生物工艺系统。这种三阶段生物工艺系统在最大限度利用SBC作为生物乙醇和阿拉伯糖醇生产的原料方面显示出巨大潜力,并且可能成为可持续“零废物”生产系统的一个实例。