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Reactor performances and fate of aromatic amines through decolorization of Direct Black 38 dye under anaerobic/aerobic sequentials

机译:厌氧/好氧顺序下直接黑38染料脱色的反应器性能和芳香胺的去向

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The removal of aromatic amines was evaluated by decolorization of CI Direct Black 38 (DB 38) dye varying between 100 and 3200 mg l~(-1) using an anaerobic upflow anaerobic sludge blanket reactor and an aerobic completely stirred tank reactor system. The effect of increasing dye loadings from 6.1 to 213.0g m~(-3) h~(-1) on decolorization and COD removal efficiency was investigated at constant glucose-COD (2000 mg l~(-1) ) concentrations in an UASB reactor. For 3200 mg l~(-1) of DB 38 and 2000 mg l~(-1) glucose-COD as co-substrate in the feed, 48.4% COD and 80% color removal efficiencies were observed at a maximum COD and dye loading rates of 5.37 kg COD m~(-3) per day and 213 g dye m~(-3) h~(-1), respectively at a hydraulic retention time (HRT) of 15 h in the UASB reactor. Sixty seven percentage remaining COD was removed at an HRT of 2.3 days and a maximum organic loading rate of 0.77 kg COD m~(-3) per day in the aerobic stage. Eighty four percentage COD, 86% color and 52.2% total aromatic amine (TAA) was removed at an HRT of 2.9 days and at an organic loading rate of 1.17 kg COD m~(-3) per day and a maximum DB 38 dye loading rate of 46.4 g dye m~(-3) h~(-1), respectively in a total system treating 3200 mg l~(-1) CI Direct Black 38 dye. The TAA produced under anaerobic conditions was ultimately removed in the aerobic stage and aromatic amine recoveries such as 45-50% were obtained in the aerobic reactor. The anaerobic/aerobic sequential process provides simultaneous color, COD and carcinogenic amine removal.
机译:使用厌氧上流厌氧污泥床反应器和需氧完全搅拌釜反应器系统,通过对CI Direct Black 38(DB 38)染料进行脱色来评估芳香族胺的去除情况,该染料在100到3200 mg l〜(-1)之间变化。在UASB反应器中,在恒定葡萄糖-COD(2000 mg l〜(-1))浓度下,研究了将染料负载量从6.1增加到213.0gm〜(-3)h〜(-1)对脱色和COD去除效率的影响。 。对于饲料中3200 mg l〜(-1)的DB 38和2000 mg l〜(-1)葡萄糖-COD作为共同底物,在最大COD和染料负载量下观察到48.4%COD和80%脱色效率在UASB反应器中的水力停留时间(HRT)为15 h时,每天的化学需氧量分别为5.37 kg COD m·(-3)和213 g染料mh·(-3)h·(-1)。在好氧阶段,在2.3天的HRT和每天最大有机负载量为0.77 kg COD m〜(-3)的情况下,去除了剩余的百分之六十七的COD。在2.9天的HRT和每天1.17千克COD m〜(-3)的有机负载量和最大DB 38染料负载量下去除了84%的COD,86%的颜色和52.2%的总芳香胺(TAA)。在处理3200 mg l〜(-1)CI直接黑38染料的整个系统中,分别达到46.4 g染料m〜(-3)h〜(-1)的速率。最终在好氧阶段将厌氧条件下产生的TAA去除,在好氧反应器中获得了45-50%的芳香胺回收率。厌氧/好氧顺序过程可同时去除颜色,COD和致癌胺。

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