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Sulfidogenesis process to strengthen re-granulation for biodegradation of methanolic wastewater and microorganisms evolution in an UASB reactor

机译:UASB反应器中硫化物生成过程,可增强重颗粒化以降解甲醇废水和微生物。

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摘要

A lab-scale methanolic wastewater-fed (3000 mg COD L-1) UASB reactor was operated for 235 days to evaluate the influence of the sulfidogenesis process on metabolic routes, the re-granulation of dispersed granules and long-term process performance. Various sulfidogenesis scenarios were created by stepwise decreasing the influent COD/SO42- ratio from 20 to 0.5 at a fixed organic loading rate (OLR) of 12 g COD L-1 d(-1). It was shown that the conversion of methanol to methane was stable at a wide COD/SO42- range of >= 2, attaining high biogas production rate of 3.78 +/- 0.32 L L-1 d(-1) with efficient concurrent removal of the total COD (96.5 +/- 4.4%) and sulfate (56.3 +/- 13.0%). The methane content in biogas remained relatively stable at 81.5 +/- 1.6% for all COD/SO42- ratios tested. The particle size of the granules was shown to clearly increase as the COD/SO42- ratios decreased. A slight linear decline was noted in the number of electrons utilized by methane producing archaea (MPA) (from 98.5 +/- 0.5% to 80.0 +/- 2.4%), whereas consumption by sulfate reducing bacteria (SRB) increased (from 1.5 +/- 0.5% to 20.0 +/- 2.4%) with the decreasing COD/SO42- ratio. According to the results of activity tests and microbial community analysis, the conversion of methanol to methane at a low COD/SO42- ratio, except from Methanomethylovorans sp., depends not only on low levels of acetoclastic and hydrogenotrophic methanogens, but also on incomplete oxidizer SRB species (e.g. Desulfovibrio sp.) that utilize H-2-CO2 with acetate to mineralize the methanol. This serves to diversify the metabolic pathway of methanol. Further analysis through scanning electron microscopy (SEM) revealed that a lower COD/SO42- ratio favored the sulfidogenesis process and diversified the microbial community inside the reactor. The benefical sulfidogenesis process subsequently invoked the formation of a sufficient, rigid [-Fe-EPS-](n) network (EPS: extracellular polymeric substances), binding and immobilizing the sludge, and resulting in the re-granulation of the dispersed granules. (C) 2016 Elsevier Ltd. All rights reserved.
机译:实验室规模的饲喂甲醇废水(3000 mg COD L-1)UASB反应器运行235天,以评估硫化过程对代谢途径,分散颗粒的重新造粒和长期过程性能的影响。通过以固定的12 g COD L-1 d(-1)的有机负载速率(OLR)将进水COD / SO42-比从20逐步降低到0.5,可以创建各种硫化物生成方案。结果表明,甲醇的甲烷转化率在大于等于2的宽COD / SO42-范围内是稳定的,获得了3.78 +/- 0.32 L L-1 d(-1)的高沼气生产率,同时高效去除了总化学需氧量(96.5 +/- 4.4%)和硫酸盐(56.3 +/- 13.0%)。对于所有测试的COD / SO42-比率,沼气中的甲烷含量保持相对稳定在81.5 +/- 1.6%。随着COD / SO42-比例的降低,颗粒的粒径明显增加。产甲烷的古细菌(MPA)使用的电子数量略有线性下降(从98.5 +/- 0.5%增至80.0 +/- 2.4%),而硫酸盐还原细菌(SRB)的消耗量增加(从1.5 + /-0.5%至20.0 +/- 2.4%),同时COD / SO42-比率降低。根据活性测试和微生物群落分析的结果,除甲硫基甲基卵磷脂外,低COD / SO42-比率下甲醇向甲烷的转化不仅取决于低水平的破乳和氢营养型产甲烷菌,还取决于不完全的氧化剂利用H-2-CO2和乙酸盐使甲醇矿化的SRB物种(例如Desulfovibrio sp。)。这用于使甲醇的代谢途径多样化。通过扫描电子显微镜(SEM)进行的进一步分析表明,较低的COD / SO42-比率有利于硫化过程,并使反应器内部的微生物群落多样化。有益的硫化生成过程随后引发了足够的刚性[-Fe-EPS-](n)网络(EPS:细胞外聚合物)的形成,结合并固定了污泥,并导致了分散颗粒的重新造粒。 (C)2016 Elsevier Ltd.保留所有权利。

著录项

  • 来源
    《Water Research》 |2017年第1期|137-150|共14页
  • 作者单位

    Tohoku Univ, Grad Sch Engn, Dept Civil & Environm Engn, Sendai, Miyagi 9808579, Japan;

    Tohoku Univ, Grad Sch Engn, Dept Civil & Environm Engn, Sendai, Miyagi 9808579, Japan;

    Tohoku Univ, Grad Sch Engn, Dept Civil & Environm Engn, Sendai, Miyagi 9808579, Japan;

    Tohoku Univ, Grad Sch Engn, Dept Civil & Environm Engn, Sendai, Miyagi 9808579, Japan;

    Tohoku Univ, Grad Sch Engn, Dept Civil & Environm Engn, Sendai, Miyagi 9808579, Japan|Tohoku Univ, Grad Sch Environm Studies, Sendai, Miyagi 9808579, Japan;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Methanol; Microbial community shift; Granular sludge; Sulfidogenesis; Methane; Extracellular polymeric substances (EPS);

    机译:甲醇;微生物群落迁移;颗粒污泥;硫化作用;甲烷;细胞外聚合物(EPS);

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