超声波处理植物生物资源的有效悬浮层

V. Bratishko, S. Shulga, O. Tigunova, V. Khmelovskyi
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引用次数: 1

摘要

寻找合理的植物原料加工参数以提高生物燃料生产效率的任务并不失去其重要性。对超声波空化处理植物原料制备第二代生物燃料(生物丁醇)的工艺进行了实验研究。以油菜秸秆为特色作物。该研究使用了容量为4.93升的超声空化装置和总功率为720瓦的发射器,超声波频率为28 kHz。超声强度为2.2 W·cm。油菜秸秆的加权平均粒径为0.78 mm。水悬浮液中干物质含量为10%。研究结果表明,超声空化器工作室内的悬浮液层对生物丁醇生产效率有显著影响。该因素的有效性随着超声治疗时间的增加而增加。与对照相比,0.03和0.12 m处理层的生物丁醇比含量分别为1.22±0.04 g·l和1.24±0.03 g·l。发酵后未经处理的物质允许得到0.73±0.04 g·l的丁醇。然而,在25分钟的处理时间内,在0.03 m的空化室中有效悬浮液层中获得的生物丁醇量显著增加(高达1.57±0.09 g·l),而在0.12 m的层中几乎没有变化。在干物质含量为5%的悬浮液处理中,丁醇产率从0.12 m有效层的1.63±0.06 g·l上升到0.03 m有效层的2.44±0.09 g·l。干物质含量为5%的未经处理的油菜秸秆生物质发酵丁醇产率为0.24±0.02 g·l。
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Effective suspension layer in ultrasonic treatment of plant bioresources
The task of finding the rational parameters of plant raw material processing to increase the production of biofuel efficiency does not lose its importance. Experimental studies on ultrasonic cavitation treatment of plant raw materials in the technology of obtaining a promising second-generation biofuel (biobutanol) were conducted. Rapeseed straw was used as a characteristic crop. The study used an ultrasonic cavitation unit with a capacity of 4.93 litres and emitters with a total power of 720 W and an ultrasonic frequency of 28 kHz. The ultrasound intensity was 2.2 W·cm. The weighted average particle size of rapeseed straw was 0.78 mm. The dry matter content in the aqueous suspension was 10%. As a result of the study, it is established that the layer of suspension in the working chamber of the ultrasonic cavitator has a significant impact on the efficiency of biobutanol production. The effectiveness of this factor increases with increasing the duration of ultrasonic treatment. Compared with the control, the specific content of biobutanol was 1.22 ± 0.04 g·l and 1.24 ± 0.03 g·l for the treated layer of 0.03 and 0.12 m, respectively. Fermentation of the untreated material allowed to obtain 0.73 ± 0.04 g·l of butanol. However, for the duration of processing at the level of 25 minutes, there was a significant increase in the amount of the obtained biobutanol for the effective layer of suspension in the cavitation chamber at the level of 0.03 m (up to 1.57 ± 0.09 g·l) at almost unchanged values for the layer of 0.12 m. These trends were confirmed in the treatment of the suspension with 5% dry matter content, where for the effective layer of the suspension of 0.12 m butanol yield was 1.63 ± 0.06 g·l increasing to 2.44 ± 0.09 g·l for the layer of 0.03 m. The yield of butanol after fermentation of untreated rapeseed straw biomass with 5% dry matter content was 0.24 ± 0.02 g·l.
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