微絮凝砂滤-臭氧催化氧化强化石化生化出水COD去除

付丽亚; 李敏; 周鉴; 吴昌永; 朱晨; 于茵; 宋玉栋

doi:10.13205/j.hjgc.202111021

微絮凝砂滤-臭氧催化氧化强化石化生化出水COD去除

doi: 10.13205/j.hjgc.202111021

付丽亚^1,2,
李敏^1,2,
周鉴³,
吴昌永^1,2,
朱晨^1,2,4,
于茵^1,2,
宋玉栋^1,2, ,

1. 中囯环境科学研究院环境污染控制工程技术研究中心, 北京 100012;
2. 中国环境科学研究院环境基准与风险评估国家重点实验室, 北京 100012;
3. 中国石油吉林石化污水处理厂, 吉林吉林 132000;
4. 中铁水务集团有限公司, 西安 710199

基金项目:

中央级公益性科研院所基本科研业务专项（2020YSKY-005）；国家水体污染控制与治理科技重大专项（2017ZX07402-002）。

详细信息

作者简介:
付丽亚(1986-),女,助理研究员,博士,主要研究方向为水污染控制技术。liyafu1115@163.com

通讯作者:
宋玉栋(1982-),男,研究员,博士,主要研究方向为水污染控制技术。songyudong@263.net

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出版历程
- 收稿日期: 2021-07-01
- 网络出版日期: 2022-01-26

MICRO FLOCCULATING SAND FILTER-CATALYTIC OZONATION ENHANCED COD REMOVAL FROM BIO-TREATED PETROCHEMICAL WASTEWATER

FU Li-ya^1,2,
LI Min^1,2,
ZHOU Jian³,
WU Chang-yong^1,2,
ZHU Chen^1,2,4,
YU Yin^1,2,
SONG Yu-dong^{1,2
, ,}

1. Research Center for Environmental Pollution Control Technologies, Chinese Research Academy of Environment Sciences, Beijing 100012, China;
2. State Key Laboratory of Environmental Criteria and Risk Assessment, Chinese Research Academy of Environment Sciences, Beijing 100012, China;
3. Jilin Petrochemical Wastewater Treatment Plant, PetroChina, Jilin Petrochemical Company, Jilin 132000, China;
4. China Railway Water Co., Ltd, Xi'an 710199, China

摘要

摘要: 为强化石化生化出水COD的去除，采用微絮凝砂滤-臭氧催化氧化工艺处理石化生化出水，比较了臭氧催化氧化反应器不同氧化方式和不同回流比组合方式下COD的去除，开展了臭氧催化氧化深度处理单元小试、中试和生产性规模研究，确立了以双级臭氧催化氧化Ⅰ级自回流工艺（回流比100%）为双级臭氧催化氧化推荐的优化工艺。生化出水ρ（COD）为70~120 mg/L时，微絮凝砂滤出水ρ（COD）达到65~113 mg/L，Ⅱ级氧化出水COD平均去除率达到35.0%~42.6%，出水满足GB 31571-2015《石油化学工业污染物排放标准》排放限值要求。生产性试验条件下，优化工艺装置去除单位COD消耗臭氧量平均为1.04 g/g，比对照组现阶段生产工艺（仅Ⅰ级臭氧曝气）降低了21.2%。
- 微絮凝砂滤 /
- 臭氧催化氧化 /
- 石化生化出水 /
- 预处理 /
- 回流
Abstract: In order to enhance the COD removal of petrochemical biochemical effluent, the removal effect of micro flocculation sand filtration and ozone catalytic oxidation on COD in petrochemical biochemical effluent was analyzed. The COD removal under different combination modes of ozone catalytic oxidation tower was compared. The lab-scale, pilot-scale and productive scale of catalytic ozonation were carried out. The ozonation tower with two stages, one-stage aeration and one-stage reflux (reflux ratio 100%) were recommended for its good performance. When the bio-treated petrochemical wastewater was 70~120 mg/L, micro flocculating sand filter effluent was 65~113 mg/L, the remocal rate of COD in two-stage effluent reached 35.0%~42.6%, meeting the emission standard for petroleum chemical industry(GB 31571-2015). Compared with the one stage aeration process production test device, ozone consumption for per unit COD of the selected optimized technology was 1.04 g/g and reduced by 21.2% comparing with the original process (single stage ozonation).
- micro flocculating sand filter /
- catalysis ozonation /
- petrochemical wastewater /
- pretreatment /
- reflux

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