Rezakazemi Mashallah, Maghami Mohsen, Mohammadi Toraj
Faculty of Chemical and Materials Engineering, Shahrood University of Technology, Shahrood, Iran.
Research and Technology Centre for Membrane Processes, Faculty of Chemical Engineering, Iran University of Science and Technology (IUST), Narmak, Tehran, Iran.
Chem Cent J. 2018 Jul 9;12(1):79. doi: 10.1186/s13065-018-0450-1.
Phenolic wastewater was treated using anaerobic submerged membrane bioreactor (ASMBR). Effect of different solids retention times on MBR performance was studied. Various ratios of carbon to nitrogen were used in the synthetic wastewaters. During the operation, phenol concentration of feed was changed from 100 to 1000 mg L. Phenol concentration was increased stepwise over the first 30 days and kept constant at 1000 mg L, thereafter. For the first 100 days, a chemical oxygen demand (COD) to N ratio of 100:5.0 was used and this resulted in phenol and COD removal more than 99 and 95%, respectively. However, the ammonium removal decreased from 95 to 40% by increasing the phenol concentration of feed, from 100 to 1000 mg L. For the last 25 days, a COD to N ratio of 100:2.1 was used due to the ammonium accumulation in the ASMBR. This led to the complete ammonium removal and no ammonium was detected in the ASMBR permeate. These results suggest that in the ASMBR at high phenol loading of 1000 mg L, COD to N ratio of the phenolic wastewater must be 100:2.1 for ammonium removal, while at low phenol loading, COD to N ratio of 100:5.0 can be used.
采用厌氧浸没式膜生物反应器(ASMBR)处理含酚废水。研究了不同固体停留时间对膜生物反应器性能的影响。在合成废水中使用了各种碳氮比。运行期间,进水的苯酚浓度从100mg/L变化到1000mg/L。在最初30天内苯酚浓度逐步增加,此后保持在1000mg/L不变。在最初100天,化学需氧量(COD)与氮的比例为100:5.0,这使得苯酚和COD的去除率分别超过99%和95%。然而,随着进水苯酚浓度从100mg/L增加到1000mg/L,氨氮去除率从95%降至40%。在最后25天,由于ASMBR中氨氮积累,使用了COD与氮比例为100:2.1。这导致氨氮被完全去除,在ASMBR渗透液中未检测到氨氮。这些结果表明,在ASMBR中苯酚负荷为1000mg/L的高负荷条件下,为实现氨氮去除,含酚废水的COD与氮比例必须为100:2.1,而在低苯酚负荷下,可使用100:5.0的COD与氮比例。