陆生蓝藻移动床生物膜培养的新型光生物反应器

Biofilms Pub Date : 2020-07-01 DOI:10.5194/biofilms9-28
J. Walther, N. Erdmann, Katharina Wastian, D. Strieth, R. Ulber
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引用次数: 0

摘要

陆地蓝细菌在悬浮培养中生长非常差。这就是为什么它们还没有被认为是抗菌物质等有趣代谢物的产生者的原因之一。我们小组先前的工作表明,与表面相关的生长可以显著提高生产力[1]。移动床生物反应器技术已经在废水处理中建立起来,为更大规模地进行这种生长提供了可能性。在这些反应器中,细菌生长在固体结构载体颗粒的表面,受保护的区域不受机械磨损(受保护的表面)。这些颗粒的尺寸通常约为1-5cm,并且由高密度聚乙烯(HDPE)制成。微藻的移动床工艺仅针对作为固体基质的织物[2]进行了描述,其中只有30%的生物质实际固定在载体颗粒上。因此,对不同的HDPE载体颗粒和不同的蓝藻进行了研究。在移动床中的1.5升光生物反应器中,三种不同的蓝藻可以在两种不同的颗粒上成功培养。作为扩大规模的步骤,开发了一个更大的反应器,它提供了更大的培养表面和足够的照明。光生物反应器反应器的设计与Zhuang等人[2]相似。基于80x35x40 ;cm罐,反应器具有65 ;升。在颗粒填充度为27 ;%时,反应器具有11.26 ;m²;在颗粒内。这对应于173 ;m²;每米³;反应器体积。它们的循环是由地面上的放气装置产生的。在放气装置旁边安装了一个倾斜板,以避免反应器底部出现流动死区。反应堆由位于反应堆外部的LED照明。通过测定干生物量(bdm)和通过光学相干断层扫描(OCT)测量生物膜厚度来离线监测生长。结果用蓝细菌社交毛coleus sociatus进行了培养。将接种物作为浓度为0.035gbdm/L的悬浮生物质添加到反应器中。两周后,将完整的生物质作为薄生物膜固定在载体颗粒上。在第18天和第45天之间,中值生物膜厚度从36µ;m至65µ;m可以随着干生物量从0.44g/L增加到1.56g/L而测量。这种体积比产量类似于在具有载体颗粒的1.5升光生物反应器中的培养 ;资助该项目由DFG(项目编号UL 170/16-1)和莱茵兰-普法尔茨州教育部(bm.rlp)提供财政支持(iProcess智能过程开发从建模到产品)  ;参考文献Strieth,Dorina;Julia Schwing;Kuhne,Stephan;拉卡托斯,迈克尔;消音器,Kai;Ulber,Roland(2017):一种基于ePBR的半连续工艺,用于使用社交毛coleus sociatus生产EPS。在:Journal of biotechnology 256,S.6–;12.庄、林兰;胡、洪英;吴、尹虎;王,婷;张,田源(2014):一种新型悬浮固相光生物反应器,用于提高微藻的生物量生产和分离。在:生物资源技术153,S.399–;402
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Novel photobioreactor for moving bed biofilm cultivation of terrestrial cyanobacteria

Terrestrial cyanobacteria grow quite poorly as suspension culture. This is one of the reasons why they have not yet been considered as producers of interesting metabolites such as antibacterial substances. Previous work in our group have shown that surface-associated growth can significantly increase productivity [1]. Moving bed bioreactor technology, which is already established in wastewater treatment, offers a possibility to carry out such growth on a larger scale. In these reactors, the bacteria grow on the surface of solid structured carrier particles in areas protected from mechanical abrasion (protected surface). These particles are usually about 1-5 cm in size and are made of high-density polyethylene (HDPE). Moving bed processes for microalgae have only been described for fabric as a solid substrate [2] whereby only 30% of the biomass was actually immobilized on the carrier particles. For this reason, different HDPE carrier particles and different cyanobacteria were investigated. Three different cyanobacteria could be successfully cultivated on two different particles in a 1.5-liter photobioreactor in a moving bed. As an up-scale step, a larger reactor was developed, which provided a larger cultivation surface in combination with a sufficient illumination.

Photobioreactor

The design of the reactor is similar to Zhuang et al. [2]. Based on an 80x35x40 cm tank, the reactor has a working volume of 65 liters. At a particle filling degree of 27 %, the reactor has a protected cultivation surface area of 11.26 m² within the particles. This corresponds to 173 m² per m³ reactor volume. Their circulation is generated by a gassing unit on the ground. An inclined plate is installed beside the gassing unit, to avoid a flow dead zone at the bottom of the reactor. The reactor is illuminated by LEDs located outside the reactor. The growth is monitored offline by the determination of the dry biomass (bdm) and the measurement of the biofilm thickness by optical coherence tomography (OCT).

Results

Cultivations with the cyanobacterium Trichocoleus sociatus were carried out. The inoculum was added to the reactor as suspended biomass with a concentration of 0.035 gbdm/L. After two weeks, the complete biomass was immobilized as a thin biofilm on the carrier particles. Between day 18 and day 45, an increase in the median biofilm thickness from 36 µm to 65 µm could be measured with an increase of the dry biomass from 0.44 to 1.56 g/L. This volume-specific yield is similar to cultivations in the 1.5-liter photobioreactors with carrier particles.

 

Funding

The project is financially supported by the DFG (Project number UL 170/16-1) and the Ministry of Education of Rhineland-Palatinate (bm.rlp) (iProcess intelligent process development – from modelling to product)

 

 References

  1. Strieth, Dorina; Schwing, Julia; Kuhne, Stephan; Lakatos, Michael; Muffler, Kai; Ulber, Roland (2017): A semi-continuous process based on an ePBR for the production of EPS using Trichocoleus sociatus. In: Journal of biotechnology 256, S. 6–12.
  2. Zhuang, Lin-Lan; Hu, Hong-Ying; Wu, Yin-Hu; Wang, Ting; Zhang, Tian-Yuan (2014): A novel suspended-solid phase photobioreactor to improve biomass production and separation of microalgae. In: Bioresource technology 153, S. 399–402.
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