Comparison of benzotriazole ultraviolet stabilizers (BUVs) removal from wastewater after subsequent stages of sequencing batch reactor (SBR) treatment process

被引:1
|
作者
Struk-Sokolowska, Joanna [1 ]
Faszczewska, Alicja [1 ]
Kotowska, Urszula [2 ]
Mielcarek, Artur [3 ]
机构
[1] Bialystok Tech Univ, Fac Civil Engn & Environm Sci, Wiejska 45A, PL-15351 Bialystok, Poland
[2] Univ Bialystok, Fac Chem, Ciolkowskiego 1K, PL-15245 Bialystok, Poland
[3] Univ Warm & Mazury Olsztyn, Fac Geoengn, Warszawska 117a, PL-10720 Olsztyn, Poland
关键词
Benzotriazole ultraviolet stabilizers; BUVs; UV-326; UV-327; UV-328; UV-329; UV-P; Heterocyclic organic compound; Wastewater treatment; Sequencing batch reactor; SBR; PERFORMANCE LIQUID-CHROMATOGRAPHY; TANDEM MASS-SPECTROMETRY; UV STABILIZERS; ACTIVATED-SLUDGE; BIODEGRADATION; EXTRACTION; PROFILES; SEDIMENT; BENZOTHIAZOLE; ENVIRONMENT;
D O I
10.1016/j.scitotenv.2023.169813
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The research focused on benzotriazole ultraviolet stabilizers (BUVs) which are commonly used compounds despite being found dangerous, e.g. promoting breast cancer cell proliferation, damaging vital organs such as hearts, brains livers and kidneys. The aim of the study was to analyse the efficiency and removal rate of BUVs from wastewater depending on the quantity of tested compounds and SBR anaerobic -aerobic conditions. The study was conducted in sequencing batch reactors (SBRs - 17 L) with real flocculent activated sludge (8 L) and model wastewater (5 L) containing UV -326, UV -327, UV -328, UV -329 and UV -P from 50 to 600 mu g center dot L-1. The SBR were operated in 390 cycles of 7 h and 10 min over 130 days. The similarity of the technological parameters of the treatment process to those used in a real wastewater treatment plant was maintained. Efficiency removal of individual BUVs was strictly dependent on the dose of compounds introduced into wastewater and ranged from 68.2 to 97 %. Removal of UV -329 occurred with lowest efficiency (from 68.2 to 85.2 %) while UV -326 was most efficiently removed from the wastewater (from 94.1 to 97 %). UV -329 was removed from wastewater with the lowest (0.0968-0.9524 mu g center dot L-1 center dot min- 1) average removal rate while UV -327 with the highest (0.16-1.3357 mu g center dot L-1 center dot min- 1), irrespective of BUVs dose in the influent. Secondary release of BUVs into the wastewater occurred in SBR during the settling phase and was dependent on the type and concentration of the BUVs in the raw wastewater. This occurrence was noted for UV -326 >= 100; UV -327 = 600; UV -328 >= 200; UV -329 >= 50 and UV -P >= 100 mu g center dot L-1. The settling phase needs to be shortened to the required minimum. This is an important conclusion for WWTPs in regards to SBR cycle duration and technological parameters of the treatment process.
引用
收藏
页数:10
相关论文
共 50 条
  • [41] Sequencing Batch Reactor (SBR) for the removal of Hg2+ and Cd2+ from synthetic petrochemical factory wastewater
    Malakahmad, Amirhossein
    Hasani, Amirhesam
    Eisakhani, Mandieh
    Isa, Mohamed Hasnain
    JOURNAL OF HAZARDOUS MATERIALS, 2011, 191 (1-3) : 118 - 125
  • [42] Simultaneous removal of nutrients from milking parlor wastewater using an AO2 sequencing batch reactor (SBR) system
    Wu, Xiao
    Zhu, Jun
    JOURNAL OF ENVIRONMENTAL SCIENCE AND HEALTH PART A-TOXIC/HAZARDOUS SUBSTANCES & ENVIRONMENTAL ENGINEERING, 2015, 50 (04): : 396 - 405
  • [43] The development of aerobic granules from slaughterhouse wastewater in treating real dyeing wastewater by Sequencing Batch Reactor (SBR)
    Bashiri, Batoul
    Fallah, Narges
    Bonakdarpour, Babak
    Elyasi, Shilan
    JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING, 2018, 6 (04): : 5536 - 5543
  • [44] Improving municipal wastewater nitrogen and phosphorous removal by feeding sludge fermentation products to sequencing batch reactor (SBR)
    Yuan, Yue
    Liu, Jinjin
    Ma, Bin
    Liu, Ye
    Wang, Bo
    Peng, Yongzhen
    BIORESOURCE TECHNOLOGY, 2016, 222 : 326 - 334
  • [45] Sliding mode control of dissolved oxygen in an integrated nitrogen removal process in a sequencing batch reactor (SBR)
    Munoz, C.
    Young, H.
    Antileo, C.
    Bornhardt, C.
    WATER SCIENCE AND TECHNOLOGY, 2009, 60 (10) : 2545 - 2553
  • [46] Hybrid System of Fenton Process and Sequencing Batch Reactor for Coking Wastewater Treatment
    Grosser, Anna
    Neczaj, Ewa
    Krzeminska, Dorota
    Ratman-Klosinska, Izabela
    WATER, 2025, 17 (05)
  • [47] Impact of salinity on treatment of saline wastewater by sequencing batch biofilm reactor process
    Lu Jie
    Yan Xue
    Ma Yan-fei
    Tian Cai-xing
    Ding Jin-cheng
    JOURNAL OF CENTRAL SOUTH UNIVERSITY, 2014, 21 (05) : 1989 - 1994
  • [48] Impact of salinity on treatment of saline wastewater by sequencing batch biofilm reactor process
    Jie Lu
    Xue Yan
    Yan-fei Ma
    Cai-xing Tian
    Jin-cheng Ding
    Journal of Central South University, 2014, 21 : 1989 - 1994
  • [49] Impact of salinity on treatment of saline wastewater by sequencing batch biofilm reactor process
    卢杰
    闫雪
    马艳飞
    田彩星
    丁金城
    Journal of Central South University, 2014, 21 (05) : 1989 - 1994
  • [50] Fuzzy Sliding Mode Control for Sequencing Batch Reactor Wastewater Treatment Process
    Fan, Li-Ping
    Liu, Yi
    Xie, Ying
    Guo, Rui
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2013, 46 (02) : 167 - 172