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提高硝基苯负荷率对厌氧移动床生物膜反应器及序批式厌氧移动床生物膜反应器/完全搅拌槽式反应器系统性能的影响。

Effect of increasing nitrobenzene loading rates on the performance of anaerobic migrating blanket reactor and sequential anaerobic migrating blanket reactor/completely stirred tank reactor system.

作者信息

Kuşçu Ozlem Selçuk, Sponza Delia Teresa

机构信息

Department of Environmental Engineering, Faculty of Engineering and Architecture, Süleyman Demirel University, Isparta, Turkey.

出版信息

J Hazard Mater. 2009 Aug 30;168(1):390-9. doi: 10.1016/j.jhazmat.2009.02.060. Epub 2009 Feb 21.

Abstract

A laboratory scale anaerobic migrating blanket reactor (AMBR) reactor was operated at nitrobenzene (NB) loading rates increasing from 3.33 to 66.67 g NB/m(3)day and at a constant hydraulic retention time (HRT) of 6 days to observe the effects of increasing NB concentrations on chemical oxygen demand (COD), NB removal efficiencies, bicarbonate alkalinity, volatile fatty acid (VFA) accumulation and methane gas percentage. Moreover, the effect of an aerobic completely stirred tank reactor (CSTR) reactor, following the anaerobic reactor, on treatment efficiencies was also investigated. Approximately 91-94% COD removal efficiencies were observed up to a NB loading rate of 30.00 g/m(3)day in the AMBR reactor. The COD removal efficiencies decreased from 91% to 85% at a NB loading rate of 66.67 g/m(3)day. NB removal efficiencies were approximately 100% at all NB loading rates. The maximum total gas, methane gas productions and methane percentage were found to be 4.1, 2.6l/day and 59%, respectively, at a NB loading rate of 30.00 g/m(3)day. The optimum pH values were found to be between 7.2 and 8.4 for maximum methanogenesis. The total volatile fatty acid (TVFA) concentrations in the effluent were 110 and 70 mg/l in the first and second compartments at NB loading rates as high as 66.67 and 6.67 g/m(3)day, respectively, while they were measured as zero in the effluent of the AMBR reactor. In this study, from 180 mg/l NB 66 mg/l aniline was produced in the anaerobic reactor while aniline was completely removed and transformed to 2mg/l of cathechol in the aerobic CSTR reactor. Overall COD removal efficiencies were found to be 95% and 99% for NB loading rates of 3.33 and 66.67 g/m(3)day in the sequential anaerobic AMBR/aerobic CSTR reactor system, respectively. The toxicity tests performed with Photobacterium phosphoreum (LCK 480, LUMIStox) and Daphnia magna showed that the toxicity decreased with anaerobic/aerobic sequential reactor system from the influent, anaerobic and to aerobic effluents.

摘要

在实验室规模的厌氧移动床生物膜反应器(AMBR)中,以3.33至66.67 g硝基苯(NB)/m³·天的负荷率运行,水力停留时间(HRT)恒定为6天,以观察NB浓度增加对化学需氧量(COD)、NB去除效率、碳酸氢盐碱度、挥发性脂肪酸(VFA)积累和甲烷气体百分比的影响。此外,还研究了厌氧反应器之后的好氧完全搅拌槽反应器(CSTR)对处理效率的影响。在AMBR反应器中,NB负荷率达到30.00 g/m³·天时,COD去除效率约为91% - 94%。NB负荷率为66.67 g/m³·天时,COD去除效率从91%降至85%。在所有NB负荷率下,NB去除效率均约为100%。在NB负荷率为30.00 g/m³·天时,发现最大总气体产量、甲烷气体产量和甲烷百分比分别为4.1 l/天、2.6 l/天和59%。发现最大产甲烷的最佳pH值在7.2至8.4之间。在NB负荷率高达66.67和6.67 g/m³·天时,第一和第二隔室出水的总挥发性脂肪酸(TVFA)浓度分别为110和70 mg/l,而AMBR反应器出水的TVFA浓度测量为零。在本研究中,厌氧反应器中由180 mg/l NB产生了66 mg/l苯胺,而在好氧CSTR反应器中苯胺被完全去除并转化为2 mg/l的邻苯二酚。在厌氧AMBR/好氧CSTR串联反应器系统中,NB负荷率为3.33和66.67 g/m³·天时,总COD去除效率分别为95%和99%。用费氏弧菌(LCK 480,LUMIStox)和大型溞进行的毒性试验表明,从进水、厌氧到好氧出水,厌氧/好氧串联反应器系统的毒性降低。

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