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中温及高温条件下高负荷厌氧反应器中产乙酸菌的富集。

Enrichment of acetogenic bacteria in high rate anaerobic reactors under mesophilic and thermophilic conditions.

机构信息

Environmental Microbiology Research Unit, Department of Microbiology, National University of Ireland, Galway, Ireland.

出版信息

Water Res. 2010 Jul;44(14):4261-9. doi: 10.1016/j.watres.2010.05.033. Epub 2010 Jun 1.

Abstract

The objective of the current study was to expand the knowledge of the role of acetogenic Bacteria in high rate anaerobic digesters. To this end, acetogens were enriched by supplying a variety of acetogenic growth supportive substrates to two laboratory scale high rate upflow anaerobic sludge bed (UASB) reactors operated at 37 degrees C (R1) and 55 degrees C (R2). The reactors were initially fed a glucose/acetate influent. Having achieved high operational performance and granular sludge development and activity, both reactors were changed to homoacetogenic bacterial substrates on day 373 of the trial. The reactors were initially fed with sodium vanillate as a sole substrate. Although % COD removal indicated that the 55 degrees C reactor out performed the 37 degrees C reactor, effluent acetate levels from R2 were generally higher than from R1, reaching values as high as 5023 mg l(-1). Homoacetogenic activity in both reactors was confirmed on day 419 by specific acetogenic activity (SAA) measurement, with higher values obtained for R2 than R1. Sodium formate was introduced as sole substrate to both reactors on day 464. It was found that formate supported acetogenic activity at both temperatures. By the end of the trial, no specific methanogenic activity (SMA) was observed against acetate and propionate indicating that the methane produced was solely by hydrogenotrophic Archaea. Higher SMA and SAA values against H(2)/CO(2) suggested development of a formate utilising acetogenic population growing in syntrophy with hydrogenotrophic methanogens. Throughout the formate trial, the mesophilic reactor performed better overall than the thermophilic reactor.

摘要

本研究的目的是扩展产乙酸菌在高负荷厌氧消化器中的作用的知识。为此,通过向两个实验室规模的高负荷上流式厌氧污泥床(UASB)反应器提供各种产乙酸生长支持基质来富集产乙酸菌,这两个反应器分别在 37°C(R1)和 55°C(R2)下运行。 反应器最初以葡萄糖/乙酸为进料。在试验的第 373 天,当达到高操作性能和颗粒污泥的发展和活性后,两个反应器都改为单相产乙酸细菌基质。 反应器最初用香草酸钠作为唯一底物进行进料。尽管 COD 去除率表明 55°C 反应器的性能优于 37°C 反应器,但 R2 的出水乙酸水平通常高于 R1,达到高达 5023mg/L。在试验的第 419 天,通过特定的产乙酸菌活性(SAA)测量确认了两个反应器中的单相产乙酸菌活性,R2 的 SAA 值高于 R1。在试验的第 464 天,将甲酸钠作为唯一底物引入两个反应器。结果发现,两种温度下甲酸钠都支持产乙酸菌活性。在试验结束时,没有针对乙酸和丙酸观察到特定的甲烷生成活性(SMA),这表明产生的甲烷仅由氢营养型古菌产生。针对 H2/CO2 的更高 SMA 和 SAA 值表明,在氢营养型产甲烷菌的共生作用下,形成了一种利用甲酸盐的产乙酸菌种群。在整个甲酸钠试验中,中温反应器的整体性能优于高温反应器。

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