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首页> 外文期刊>Journal of Hazardous Materials >Alternated biodegradation of naphthalene (NAP), acenaphthylene (ACY) and acenaphthene (ACE) in an aerobic granular sludge reactor (GSBR)
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Alternated biodegradation of naphthalene (NAP), acenaphthylene (ACY) and acenaphthene (ACE) in an aerobic granular sludge reactor (GSBR)

机译:好氧颗粒污泥反应器(GSBR)中萘(NAP),(ACY)和(ACE)的交替生物降解

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The paper presents quantitative changes of selected 2- and 3-ring PAHs after process phases of GSBR reactor. The studies have been carried out for 264 cycles of GSBR reactor, during which concentration of naphthalene was increased in the range of 3.00-710.00 mu g/L, acenaphthylene 1.00-160.00 mu g/L, acenaphthene 3.00-440.00 mu g/L. GSBR operating cycle consisted of filling (30 min), mixing (90 min), aeration (540 min), sedimentation (10 min), decanting (30 min) and downtime (20 min) phases. Activated sludge dry mass concentration was 4.00 kg/m(3). Conducted studies showed that in GSBR reactor naphthalene was degraded with the highest intensity. Results of the statistical analysis confirmed that naphthalene concentrations were statistically significantly different (alpha = 0.05) after each individual GSBR process phase, while in case of acenaphthene and acenaphthylene, the differences were observed only between mixing and aeration phases. Additionally, equations estimating concentrations of PAHs in treated wastewater were developed. Selected activated sludge technological parameters (sludge volume index, sludge and hydraulic retention time) and concentration of PAHs were used for equations. The R-2 coefficients of equations were above 0.99, which indicates a good adjustment of estimation to observed values.
机译:本文介绍了GSBR反应器加工阶段后选定的2环和3环PAH的定量变化。已经对GSBR反应器的264个循环进行了研究,在此期间萘的浓度在3.00-710.00μg/ L,L烯1.00-160.00μg/ L,烯3.00-440.00μg/ L的范围内增加。 GSBR操作周期包括填充(30分钟),混合(90分钟),通气(540分钟),沉淀(10分钟),倾析(30分钟)和停机时间(20分钟)阶段。活性污泥干质量浓度为4.00 kg / m(3)。进行的研究表明,在GSBR反应器中,萘的降解强度最高。统计分析结果证实,在每个单独的GSBR工艺阶段后,萘浓度在统计学上均存在显着差异(α= 0.05),而在of和and的情况下,仅在混合和曝气阶段之间观察到差异。此外,还建立了估算废水中PAHs浓度的方程式。选择的活性污泥工艺参数(污泥体积指数,污泥和水力停留时间)和多环芳烃的浓度用于方程式。方程的R-2系数大于0.99,这表明估计值可以很好地调整到观测值。

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