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苯酚梯度馴化過程中厭氧折流板反應器微生物群落演替特征

Microbial community succession characteristics in an anaerobic baffled reactor during phenol gradient acclimation

  • 摘要: 厭氧消化是工業廢水和城市廢水處理過程中常用的技術之一. 由于廢水中的苯酚會影響厭氧消化系統的穩定性,因此在使用厭氧消化工藝前需要使用苯酚對活性污泥進行馴化,從而降低其抑制作用. 本文考察了厭氧折流板反應器在進行苯酚梯度馴化時各隔室出水的化學需氧量(COD)、pH、苯酚及沼氣中氫氣分壓的變化情況. 運用Illumina高通量測序平臺分析了細菌和古菌群落的演替過程,并使用氣相色譜與質譜聯用儀(GC–MS)和高效液相色譜儀(HPLC)對苯酚厭氧降解產物分別進行了定性和定量分析. 結果表明,使用葡萄糖作為唯一進水碳源時第1隔室出水的pH在5.0~6.8之間波動. 當進水中加入苯酚后該隔室出水pH有所上升. 約90%的COD和苯酚在前兩個隔室內降解,但后續隔室的COD始終保持在100 mg·L?1左右,因此推測最終出水中含有未降解物質. 使用葡萄糖和苯酚作為進水碳源時細菌和古菌群落的α生物多樣性指數高于使用單一進水碳源. 苯酚的加入導致細菌群落的優勢菌科StreptococcaceaeEnterobacteriaceaeSyntrophaceae取代;古菌群落的優勢菌科Methanobacteriaceae 則被Woesearchaeales取代. 冗余分析顯示,細菌Syntrophaceae科和古菌Woesearchaeales科分別與苯酚和乙酸的相關性較高. 產物定性分析確認了最終出水中的難降解物質為丙酸. 熱力學計算表明反應器內過高的氫氣分壓是導致丙酸難以降解的原因.

     

    Abstract: Anaerobic digestion (AD) is extensively used for treating both industrial and municipal wastewater owing to its cost-efficiency and eco-friendly nature. However, phenol in polluted effluents can destabilize AD performance. To increase phenol tolerance to AD microbial communities, stepwise acclimatization is commonly employed. This method also aids in selecting microorganisms well-suited for phenol degradation. In this study, anaerobic sludge acclimatization was conducted using a four-chamber anaerobic baf?ed reactor (ABR). Initially, the reactor was fed with glucose as the sole carbon source. Phenol levels in the influent increased stepwise from 100 to 300 mg·L?1. In the final experimental phase, the reactor processed wastewater containing 780 mg·L?1 of phenol as the sole substrate, without glucose. We analyzed hydrogen partial pressure, pH, chemical oxygen demand (COD), and phenol concentration to examine changes in reactor performance. The Microbial community dynamics were investigated using Illumina high-throughput sequencing technology. Phenol degradation intermediates were performed using gas chromatography/mass spectrometry (GC–MS), with their quantities measured by high-performance liquid chromatography. The results showed a decrease in hydrogen partial pressure from 5 to 20 Pa in the ABR from Chamber 1 to Chamber 4. The pH levels in the first chamber fluctuated from 5.0 to 6.8 with glucose alone and increased with phenol addition. Nearly 90% of COD and phenol were degraded in the initial two chambers. However, COD levels remained at 100 mg·L?1 in the last two chambers, suggesting the presence of nondegradable components in the effluent. α-diversity analysis indicated Shannon, Simpson, and Chao1 indices for bacterial and archaeal communities with glucose and phenol as carbon sources in the feed. Acclimatization significantly altered the microbial community structure, shifting dominant families from Streptococcaceae and Enterobacteriaceae to Syntrophaceae, and archaeal families from Methanobacteriaceae to Woesearchaeales. Redundancy analysis (RDA)linked Syntrophaceae and Woesearchaeales to phenol degradation and acetotrophic processes, respectively. GC–MS analysis revealed propionic acid as the only effluent component. The randomized methyl–malonyl–CoA pathway and the C-6-dismutation pathway are two known routes for propionate degradation. However, the ΔG' values for these reactions were consistently greater than ?20 kJ·mol?1, indicating that propionate degradation did not occur under the experimental conditions. From a thermodynamic point of view, high hydrogen partial pressure levels in the reactor affected the propionate degradation process and also inhibited sludge bioactivity. Syntrophobacter and Smithella are responsible for degrading propionate. The relative abundance of these two families slowly increased from 0.35% to 6.9% in the ABR from Chamber 1 to Chamber 4. These findings account for the inadequate efficiency of COD removal observed in the effluent.

     

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