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Biodegradation of 2-chlorophenol (2CP) in an anaerobic sequencing batch reactor (ASBR)

机译:厌氧顺序分批反应器(ASBR)中的2-氯苯酚(2CP)生物降解

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The aim of this study is to contribute to the knowledge about anaerobic digestion of 2-chlorophenol (2CP) in an anaerobic sequencing batch reactor (ASBR). Two reactors were set up (ASBR _A and ASBR _B). The ASBR _A was fed with 2-chlorophenol (28-196 mg 2CP-C/L) and no other exogenous electron donor. The ASBR _B was fed with a mixture of 2CP (28-196 mg 2CP-C/L) and phenol (28-196 mg phenol-C/L) as an electron donor. The process evaluation was conducted by three means: first by substrate consumption efficiency (E _(2CP)), second, by biogas yield (Ybiogas-C/2CP-C) and third, by the specific consumption rates (q _(2CP)) as response variables. The 2CP consumption efficiency (90±0.4%) was not influenced by the increase in the concentrations tested. In both reactors ASBR _A and ASBR _B, both concentration as well as speed increased. Concentration increased from 28 to 114 mg 2CP-C/L. The specific consumption rate (q _(2CP)) values were fivefold higher. However, a decrease of 37% was observed at 140 mg 2CP-C/L and one of 72% at 196 mg 2CP-C/L. The biogas yields (0.80±0.06) remained stable in both reactors. In both reactors the biogas yield decreased to 78±3% at 196 mg 2CP-C/L. We might assume this decrease was due to the accumulation of VFA. Finally, poor sludge settleability was determined only in the SBRB reactor at 140 and 196 mg 2CP-C/L. An increase was observed in both SVI≤ 140± 5 mL/g and over exopolymeric protein ≤120 mg EP/L.
机译:这项研究的目的是为厌氧测序间歇反应器(ASBR)中的2-氯苯酚(2CP)厌氧消化提供知识。设置了两个反应堆(ASBR _A和ASBR _B)。用2-氯苯酚(28-196 mg 2CP-C / L)喂ASBR _A,没有其他外源电子供体。向ASBR_B喂入作为电子给体的2CP(28-196mg 2CP-C / L)和苯酚(28-196mg苯酚-C / L)的混合物。通过三种方式进行工艺评估:首先是通过底物消耗效率(E _(2CP)),第二是通过沼气产量(Ybiogas-C / 2CP-C),第三是通过特定消耗率(q _(2CP) )作为响应变量。 2CP消耗效率(90±0.4%)不受测试浓度增加的影响。在两个反应器ASBR_A和ASBR_B中,浓度和速度均增加。浓度从28 mg的2CP-C / L增加到114 mg。比消耗率(q _(2CP))值高五倍。但是,在140 mg 2CP-C / L下观察到降低了37%,在196 mg 2CP-C / L下观察到降低了72%之一。在两个反应器中沼气产量(0.80±0.06)保持稳定。在两个反应器中,在196 mg 2CP-C / L下,沼气产率降至78±3%。我们可以假设这种下降是由于VFA的积累。最后,仅在140和196 mg 2CP-C / L的SBRB反应器中确定了较差的污泥沉降能力。观察到SVI≤140±5 mL / g和外聚合蛋白≤120 mg EP / L均增加。

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