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硫自养反硝化生物滤池工艺处理石化废水

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采用硫自养反硝化生物滤池工艺处理某石化企业含NO3--N混合废水(硝基氯苯废水芬顿氧化出水和综合废水生化出水),开展了中试(20~80 m3/d)和工程应用(250~270 m3/h)试验。中试装置脱氮效果显著,TN和NO3--N平均去除率分别可达95。2%和96。5%。废水中的残留H2O2及较低碱度对脱氮效果抑制明显,通过控制H2O2浓度及适当补充碱度可提升脱氮性能。工程应用试验期间,进水TN平均47。3 mg/L,TN去除率平均95。5%,出水TN平均2。19 mg/L,满足江苏省《化学工业水污染物排放标准》(DB32/939-2020)要求。装置运行过程中无需投加有机碳源,避免了COD超标风险;不产生CO2,较异养反硝化生物滤池工艺CO2排放量减少约930 t/a,有效响应国家"双碳"战略目标;运行费用较低,较异养型节省约50%。
Treatment of high total nitrogen wastewater by autotrophic sulfur denitrification biological filter process
High TN wastewater(mixed by nitrochlorobenzene advanced oxidation effluent and biochemical effluent)of a petrochemical enterprise was treated by an autotrophic sulfur denitrification biological filter process.Pilot test(20-80 m3/d)and engineering application(250-270 m3/h)were both carried out.Satisfactory performance was obtained in a pilot test,with the average TN and NO3--N removal efficiency of 95.2%and 96.5%,respectively.The residual H2O2 and alkalinity deficiency in wastewater significantly inhibited the nitrogen removal effect,and the effect could be improved by controlling the H2O2 concentration and supplementing alkalinity appropriately.During the engineering application,the average influent TN was 47.3 mg/L,the average TN removal efficiency was 95.5%,and the average effluent TN was 2.19 mg/L,which met the requirements of Jiangsu Provincial standard of DB32/939-2020.Compared with the traditional heterotrophic denitrification nitrogen removal process,this process did not require organic carbon source addition,which avoided effluent COD excess.As no CO2 was produced during operation,CO2 emissions were reduced by about 930 t/a,which effectively responds to the"double-carbon"strategy.Besides,the operation cost of this process was reduced by about 50%.

autotrophic sulfur denitrificationbiological filtertotal nitrogendouble-carbon

程彬彬、陈春茂、王庆宏、李晋、刘植昌

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中国石油大学(北京)化学工程与环境学院,北京 102249

中国石油化工股份有限公司 炼油事业部,北京 100728

硫自养反硝化 生物滤池 总氮 双碳

2025

化工环保
中国石化集团资产经营管理有限公司北京化工研究院,中国化工环保协会

化工环保

北大核心
影响因子:0.921
ISSN:1006-1878
年,卷(期):2025.45(1)