• 文献检索
  • 文档翻译
  • 深度研究
  • 学术资讯
  • Suppr Zotero 插件Zotero 插件
  • 邀请有礼
  • 套餐&价格
  • 历史记录
应用&插件
Suppr Zotero 插件Zotero 插件浏览器插件Mac 客户端Windows 客户端微信小程序
定价
高级版会员购买积分包购买API积分包
服务
文献检索文档翻译深度研究API 文档MCP 服务
关于我们
关于 Suppr公司介绍联系我们用户协议隐私条款
关注我们

Suppr 超能文献

核心技术专利:CN118964589B侵权必究
粤ICP备2023148730 号-1Suppr @ 2026

文献检索

告别复杂PubMed语法,用中文像聊天一样搜索,搜遍4000万医学文献。AI智能推荐,让科研检索更轻松。

立即免费搜索

文件翻译

保留排版,准确专业,支持PDF/Word/PPT等文件格式,支持 12+语言互译。

免费翻译文档

深度研究

AI帮你快速写综述,25分钟生成高质量综述,智能提取关键信息,辅助科研写作。

立即免费体验

UASB 反应器处理酸性矿山废水的长期性能:硫酸盐负荷率、水力停留时间和 COD/SO 比的影响。

Long-term performance of a UASB reactor treating acid mine drainage: effects of sulfate loading rate, hydraulic retention time, and COD/SO ratio.

机构信息

Departamento de Hidráulica e Saneamento e Escola de Engenharia de São Carlos, Universidade de São Paulo (SHS/EESC/USP), Av. Trabalhador São-Carlense 400, 13566-590, São Carlos, SP, Brazil.

Laboratório de Biotecnologia Anaeróbia, Instituto de Ciência e Tecnologia, Universidade Federal de Alfenas (UNIFAL-MG), Rodovia José Aurélio Vilela, 11999 (BR 267, Km 533), 37715-400, Poços de Caldas, MG, Brazil.

出版信息

Biodegradation. 2019 Feb;30(1):47-58. doi: 10.1007/s10532-018-9863-8. Epub 2018 Nov 8.

DOI:10.1007/s10532-018-9863-8
PMID:30406872
Abstract

Acid mine drainage (AMD) is among the most serious threats to water and the typical alkali-based treatment costs are high. This study's main objective was the establishment of a highly efficient biological process using an upflow anaerobic sludge blanket (UASB) reactor to treat AMD based on a shorter hydraulic retention time (HRT) and lower organic matter input. The process was evaluated for a long-term operation (739 days) in terms of the influence of HRT (14-24 h), metal addition, sulfate loading rate (0.5-2.6 g SO l d), and the COD/SO ratio (0.67-1.0) using ethanol as the only electron donor at a pH of 4.0. Neutral effluent pH was achieved throughout the time apart from operational modifications. The reduction in HRT from 24 to 16 h and an increase in the sulfate loading rate (SLR) up to 2.25 g SO l d improved the sulfate removal to (92.1 ± 1.8)% with 80% chemical oxygen demand (COD) removal. However, the sulfate reduction was less than 80% when the HRT and SLR was changed to 14 h and 2.6 g SO l d, respectively. The oxidation of organic matter by sulfate reduction was greater than 50% regardless of the conditions imposed but the use of ethanol to treat AMD was more efficient when either the HRT was 16 h (1.5 g SO l d) in the presence of Fe, Zn, and Cu or the HRT was 14 h (2.6 g SO l d) but the COD/SO ratio was reduced to 0.67. The fully optimized conditions of the UASB reactor were set at an HRT of 16 h, SLR of 1.5 g SO l d, and a COD/SO ratio of 1.0.

摘要

酸性矿山排水 (AMD) 是对水的最严重威胁之一,而典型的碱性处理方法成本很高。本研究的主要目的是建立一个高效的生物处理过程,使用上流式厌氧污泥床 (UASB) 反应器,以较短的水力停留时间 (HRT) 和较低的有机物输入处理 AMD。该过程在长期运行 (739 天) 中,根据 HRT (14-24 小时)、金属添加、硫酸盐负荷率 (0.5-2.6 g SO l d) 和 COD/SO 比 (0.67-1.0) 的影响进行了评估,使用乙醇作为唯一电子供体,在 pH 值为 4.0 时运行。除了操作修改外,整个时间内都实现了中性流出物 pH 值。将 HRT 从 24 小时减少到 16 小时,并将硫酸盐负荷率 (SLR) 提高到 2.25 g SO l d,将硫酸盐去除率提高到 (92.1 ± 1.8)%,同时去除 80%的化学需氧量 (COD)。然而,当 HRT 和 SLR 分别变为 14 小时和 2.6 g SO l d 时,硫酸盐还原率低于 80%。无论施加何种条件,硫酸盐还原对有机物的氧化都大于 50%,但使用乙醇处理 AMD 时,在 HRT 为 16 小时(存在 Fe、Zn 和 Cu 时为 1.5 g SO l d)或 HRT 为 14 小时(但 COD/SO 比降低至 0.67)时,效率更高。UASB 反应器的完全优化条件设定为 HRT 为 16 小时、SLR 为 1.5 g SO l d 和 COD/SO 比为 1.0。

相似文献

1
Long-term performance of a UASB reactor treating acid mine drainage: effects of sulfate loading rate, hydraulic retention time, and COD/SO ratio.UASB 反应器处理酸性矿山废水的长期性能:硫酸盐负荷率、水力停留时间和 COD/SO 比的影响。
Biodegradation. 2019 Feb;30(1):47-58. doi: 10.1007/s10532-018-9863-8. Epub 2018 Nov 8.
2
Sulfate and metals removal from acid mine drainage in a horizontal anaerobic immobilized biomass (HAIB) reactor.在水平厌氧固定化生物量(HAIB)反应器中去除酸性矿山排水中的硫酸盐和金属。
J Environ Sci Health A Tox Hazard Subst Environ Eng. 2020;55(12):1436-1449. doi: 10.1080/10934529.2020.1806632. Epub 2020 Aug 19.
3
Upflow anaerobic sludge blanket reactor--a review.上流式厌氧污泥床反应器——综述
Indian J Environ Health. 2001 Apr;43(2):1-82.
4
Sulfidogenic fluidized bed treatment of real acid mine drainage water.硫化物流化床处理实际酸性矿山排水。
Bioresour Technol. 2011 Jan;102(2):683-9. doi: 10.1016/j.biortech.2010.08.042. Epub 2010 Aug 24.
5
Sulfidogenic biotreatment of synthetic acid mine drainage and sulfide oxidation in anaerobic baffled reactor.在厌氧折流板反应器中利用硫酸盐还原菌处理人工酸性矿山排水和硫化物氧化。
J Hazard Mater. 2011 May 30;189(3):670-6. doi: 10.1016/j.jhazmat.2011.01.087. Epub 2011 Jan 28.
6
Effects of shock 2,4-dichlorophenol (DCP) and cod loading rates on the removal of 2,4-DCP in a sequential upflow anaerobic sludge blanket/aerobic completely stirred tank reactor system.冲击负荷、2,4-二氯酚(DCP)及鳕鱼负荷率对序批式上流式厌氧污泥床/好氧完全搅拌槽式反应器系统中2,4-DCP去除效果的影响
Environ Technol. 2008 Apr;29(4):413-21. doi: 10.1080/09593330801983847.
7
Removal of residual dissolved methane gas in an upflow anaerobic sludge blanket reactor treating low-strength wastewater at low temperature with degassing membrane.采用脱气膜去除低温低浓度废水上流式厌氧污泥床反应器中残余溶解甲烷气体。
Water Res. 2011 May;45(11):3533-40. doi: 10.1016/j.watres.2011.04.030. Epub 2011 Apr 22.
8
The effect of acidic pH and presence of metals as parameters in establishing a sulfidogenic process in anaerobic reactor.酸性pH值和金属的存在作为厌氧反应器中建立硫酸盐还原过程的参数所产生的影响。
J Environ Sci Health A Tox Hazard Subst Environ Eng. 2016 Aug 23;51(10):793-7. doi: 10.1080/10934529.2016.1181433. Epub 2016 May 24.
9
High rate of biological removal of sulfate, organic matter, and metals in UASB reactor to treat synthetic acid mine drainage and cheese whey wastewater as carbon source.UASB 反应器中硫酸盐、有机物和金属的生物去除率高,可将合成酸性矿山排水和奶酪乳清废水作为碳源处理。
Water Environ Res. 2020 Feb;92(2):245-254. doi: 10.1002/wer.1235. Epub 2019 Sep 19.
10
Effect of pentachlorophenol and chemical oxygen demand mass concentrations in influent on operational behaviors of upflow anaerobic sludge blanket (UASB) reactor.进水五氯苯酚和化学需氧量质量浓度对升流式厌氧污泥床(UASB)反应器运行行为的影响。
J Hazard Mater. 2006 Aug 25;136(3):645-53. doi: 10.1016/j.jhazmat.2005.12.050. Epub 2006 Feb 28.

引用本文的文献

1
Sensitivity of Pathogenic Bacteria Strains to Treated Mine Water.处理后矿井水中病原菌的敏感性。
Int J Environ Res Public Health. 2022 Nov 23;19(23):15535. doi: 10.3390/ijerph192315535.