首页|化学原料药及医药中间体废水处理工程实例

化学原料药及医药中间体废水处理工程实例

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针对某医药企业生产废水污染物因子多、浓度高低不一、可生化性差等特点,采用了分类处理,高浓度废水采用车间预处理-零价铁(ZVI)还原+氧化工艺处理,与低浓度废水混合后采用气浮-水解酸化-高效双循环(HIC)厌氧塔-两级AO-MBR-流化床芬顿(FBR)氧化塔组合工艺进行处理,在混合废水CODCr、氨氮、总氮质量浓度分别为5430、222和371 mg/L的条件下,处理出水分别为240、21和45 mg/L,对应去除率分别为95.6%、90.5%、87.9%,符合园区污水处理厂纳管标准.
An example of wastewater treatment project for chemical APIs and pharmaceutical intermediates
Wastewater from a pharmaceutical enterprise contains various kinds of pollutants with different concentrations,which exhibits poor biodegradability,according to the above characteristics,classification process was adopted.Using workshop pretreatment-zero valent iron(ZVI)reduction+oxidation process to treat high con-centration wastewater,the effluent water was mixed with low concentration wastewater,and the mixture was then be treated by combined process of air flotation-hydrolytic acidification-high efficiency dual cycle(HIC)anaero-bic tower-two stage AO-MBR-fludized bed Fenton(FBR)oxidation tower.Under the condition that the mass concentrations of CODCr,ammonia nitrogen,total nitrogen in the mixed wastewater were 5 430,222,371 mg/L re-spectively,the corresponding indexes in the effluent water were 240,21 and 45 mg/L respectively,the removal rates were 95.6%,90.5%and 87.9%respectively,which complied with the emission standard of the industrial park.

pharmaceutical wastewaterclassification processZVI reduction+oxidation processhydrolytic acidificationHIC anaerobic towertwo stage AOMBRFBR oxidation tower

陶超平、朱家辉、吴婉卿、郑津津

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绍兴市上虞区固体废物处理指导服务中心,浙江 绍兴 312300

医药废水 分类处理 ZVI还原+氧化工艺 水解酸化 HIC厌氧塔 两级AO MBR FBR氧化塔

2024

工业用水与废水
东化工程科技股份有限公司

工业用水与废水

CSTPCD
影响因子:0.649
ISSN:1009-2455
年,卷(期):2024.55(6)