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吡啶对用于去除苯酚、硫氰酸盐和氨的序批式厌氧-缺氧-好氧固定膜生物反应器系统的影响。

Pyridine influence on a sequential anaerobic-anoxic-aerobic FMBR system for phenol, thiocyanate and ammonia removal.

作者信息

Sahariah Biju Prava, Anandkumar J, Chakraborty Saswati

机构信息

a Department of Energy and Environmental Engineering , Chhattisgarh Swami Vivekanand Technical University , Chhattisgarh , India.

b Department of Chemical Engineering , National Institute of Technology Raipur , Chhattisgarh , India.

出版信息

Environ Technol. 2018 Jul;39(14):1786-1794. doi: 10.1080/09593330.2017.1340344. Epub 2017 Jun 26.

DOI:10.1080/09593330.2017.1340344
PMID:28592192
Abstract

A synthetic wastewater containing various pyridine concentrations (25-250 mg/L) was treated in a sequential anaerobic(B1)-anoxic(B2)-aerobic(B3) fed batch moving bed reactor (FMBR) system. Pyridine was associated with phenol (1500 mg/L), SCN- (800 mg/L), chemical oxygen demand (COD) (5400-5430 mg/L) and NH4+-N (500 mg/L) at hydraulic retention time (HRT) of 6 (B1: 3 days; B2 and B3: 1.5 days each) days. In B1, pyridine removal was 10-12% from influent concentration of 25-100 mg/L and beyond that, it was zero. Removal of phenol (53-39%) and COD (33-22%) occurred in B1, but pyridine above 50 mg/L inhibited both. In B2, 68-90% of pyridine removal occurred along with phenol (>98%), COD (>67%), SCN- (>85%) removal and denitrification. In B2, with an increase in pyridine loading removal rate of phenol, COD and nitrate increased, whereas SCN- removal decreased beyond pyridine loading of 0.031g/L day. In B3, nitrification decreased with high generation of free ammonia. Pyridine degradation in B1, B2 and B3 follows the Stover-Kincannon model with a maximum substrate removal rate of 111.1, 333.3 and 23.81 g/L day, respectively. Thiocyanate removal in B2 and ammonia removal in B3 follows the Bhatia inhibition model with a maximum substrate removal rate of 0.641 and 0.528/day, respectively. The overall efficiency of the FMBR system remained unaffected up to 250 mg pyridine/L at 6 days HRT.

摘要

在一个序批式厌氧(B1)-缺氧(B2)-好氧(B3)进水间歇移动床反应器(FMBR)系统中处理了含有不同吡啶浓度(25 - 250 mg/L)的合成废水。吡啶与苯酚(1500 mg/L)、SCN⁻(800 mg/L)、化学需氧量(COD)(5400 - 5430 mg/L)和NH₄⁺-N(500 mg/L)共存,水力停留时间(HRT)为6天(B1:3天;B2和B3各1.5天)。在B1中,进水吡啶浓度为25 - 100 mg/L时,吡啶去除率为10 - 12%,超过该浓度则为零。B1中发生了苯酚(53 - 39%)和COD(33 - 22%)的去除,但50 mg/L以上的吡啶对两者均有抑制作用。在B2中,68 - 90%的吡啶去除伴随着苯酚(>98%)、COD(>67%)、SCN⁻(>85%)的去除和反硝化作用。在B2中,随着吡啶负荷的增加,苯酚、COD和硝酸盐的去除率增加,而当吡啶负荷超过0.031 g/L·天,SCN⁻的去除率下降。在B3中,随着游离氨的大量产生硝化作用下降。B1、B2和B3中吡啶降解遵循Stover - Kincannon模型,最大底物去除率分别为111.1、333.3和23.81 g/L·天。B2中硫氰酸盐的去除和B3中氨的去除遵循Bhatia抑制模型,最大底物去除率分别为0.641和0.528/天。在HRT为6天的情况下,FMBR系统中吡啶浓度高达250 mg/L时,整体效率不受影响。

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