Bernat Katarzyna, Wojnowska-Baryła Irena, Dobrzyńska Adriana
Department of Environmental Biotechnology, University of Warmia and Mazury in Olsztyn, Sloneczna St. 45G, 10-709 Olsztyn, Poland.
Bioresour Technol. 2008 May;99(7):2410-8. doi: 10.1016/j.biortech.2007.05.008. Epub 2007 Jun 26.
The objective of the work reported here was to determine whether the ratio of COD/Nox has an impact on poly-beta-hydroxybutyrate (PHB) metabolism in activated sludge. Furthermore, it was tested if the ratio influenced the percentage use of organic compounds present in wastewater, for endogenous respiration, oxidation, accumulation and denitrification. Gas flow rate in SBR reactor was controlled by thermal mass flow controller (TMFC). Constant amount of air entering sequencing batch reactor was automatically adjusted to stable set-point 2mg O2 L(-1). It means that DO concentration in the reactor could change with oxygen uptake. During the filling period and part of the reaction time DO was nearly zero. Feast period of the external substrate availability and famine period of little amount or no external carbon availability were determined. At 23 h of the reaction time, and COD/Nox ratio 8, denitrification took place only during feast period. What was interesting, poly-beta-hydroxybutyrate degradation was observed in the feast period as well. However, at 11h of the reaction time and COD/Nox ratio 37, denitrification occurred in feast and famine period. In the feast period PHB was accumulated and in the famine period was used as the endogenous carbon source. COD consumption to reduce 1mg N-nitrate was ranging from 1.15 to 6.26 depending on carbon source and increased when exogenous and endogenous carbon were used by activated sludge. The increase in PHB content from 0.25 to 0.43 Cmol/Cmol resulted in a double increase in the amount of nitrogen removed due to denitrification was observed.
本文报道的工作目的是确定化学需氧量(COD)与硝态氮(Nox)的比例是否对活性污泥中聚-β-羟基丁酸酯(PHB)的代谢有影响。此外,还测试了该比例是否影响废水中有机化合物用于内源呼吸、氧化、积累和反硝化的利用百分比。序批式反应器(SBR)中的气体流速由热质量流量控制器(TMFC)控制。进入序批式反应器的空气量恒定自动调节至稳定设定点2mg O2 L(-1)。这意味着反应器中的溶解氧(DO)浓度会随氧气摄取量而变化。在进水期和部分反应时间内,DO几乎为零。确定了外部底物可利用的丰水期和少量或无外部碳可利用的缺水期。在反应时间23小时、COD/Nox比例为8时,反硝化仅在丰水期发生。有趣的是,在丰水期也观察到了聚-β-羟基丁酸酯的降解。然而,在反应时间11小时、COD/Nox比例为37时,反硝化在丰水期和缺水期均发生。在丰水期PHB积累,在缺水期用作内源碳源。根据碳源不同,还原1mg N-硝酸盐的COD消耗量在1.15至6.26之间,当活性污泥同时利用外源和内源碳时,该消耗量会增加。观察到PHB含量从0.25 Cmol/Cmol增加到0.43 Cmol/Cmol,导致因反硝化去除的氮量增加了一倍。