| 水解酸化-SBR工艺处理饮料生产废水 |
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| 引用本文： | 杨文澜,殷竞洲,李宝山.水解酸化-SBR工艺处理饮料生产废水[J].环境工程,2007,25(4):94-96. |
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| 作者姓名： | 杨文澜 殷竞洲 李宝山 |
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| 作者单位： | 1. 淮阴师范学院化学系,江苏淮安,223300
2. 深圳市晓清环保实业有限公司,广东,深圳,518017 |
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| 摘 要： | 介绍了水解酸化+SBR工艺处理饮料生产废水的工艺设计和运行效果。该工艺具有处理效果好、低能耗、易管理等特点。在进水CODCr为2000～4000mg/L,BOD5为1000～2000mg/L的条件下,经过该系统处理,出水CODCr保持在130mg/L以下,BOD5保持在25mg/L以下,出水水质达到(GB8978-1996)《中华人民共和国国家标准污水综合排放标准》的Ⅱ级标准。
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| 关 键 词： | 饮料生产废水 水解酸化 SBR |
| 修稿时间： | 2006-10-24 |
TREATMENT OF WASTEWATER FROM PRODUCING BEVERAGE WITH HYDROLYSIS ACIDIFICATION-SBR PROCESS |
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| Yang Wenlan,Yin Jingzhou,Li Baoshan.TREATMENT OF WASTEWATER FROM PRODUCING BEVERAGE WITH HYDROLYSIS ACIDIFICATION-SBR PROCESS[J].Environmental Engineering,2007,25(4):94-96. |
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| Authors: | Yang Wenlan Yin Jingzhou Li Baoshan |
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| Institution: | Yang Wenlan Yin Jingzhou Li Baoshan |
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| Abstract: | It is introduced that the process design and running effect of treating wastewater from producing beverages by hydrolytic acidification-SBR process.This process has advantages of low energy consumption and easy control.Under normal conditon when COD_ Cr of influent at 2 000 ～ 4 000 mg/L ,BOD_5 at 1 000 ～ 2 000 mg/L ,the mean residual COD_ Cr in effluent will be lower than 130 mg/L,BOD_5 will be lower than 25 mg/L,which can meet the second-order of National Standard for Comprehensive Discharge of Wastewater(GB8978-1996). |
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| Keywords: | wastewater from producing beverage hydrolytic acidification and SBR |
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