[1]王莉,吴连成,于鲁冀..味精工业废水SBR生物脱氮实验研究[J].郑州大学学报(工学版),2008,29(03):95-98.[doi:10.3969/j.issn.1671-6833.2008.03.025]
 WANG Li,Wu Liancheng,Yu Luji.Experimental study on SBR biological denitrification of monosodium glutamate industrial wastewater[J].Journal of Zhengzhou University (Engineering Science),2008,29(03):95-98.[doi:10.3969/j.issn.1671-6833.2008.03.025]
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味精工业废水SBR生物脱氮实验研究()
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《郑州大学学报(工学版)》[ISSN:1671-6833/CN:41-1339/T]

卷:
29
期数:
2008年03期
页码:
95-98
栏目:
出版日期:
1900-01-01

文章信息/Info

Title:
Experimental study on SBR biological denitrification of monosodium glutamate industrial wastewater
作者:
王莉吴连成于鲁冀.
郑州大学,水利与环境学院,郑州,河南,450001, 郑州大学,水利与环境学院,郑州,河南,450001, 郑州大学,水利与环境学院,郑州,河南,450001
Author(s):
WANG Li; Wu Liancheng; Yu Luji
关键词:
味精废水 序批式生物反应器 生物脱氮
Keywords:
monosodium glutamate wastewater Sequencing batch bioreactors Biological denitrification
DOI:
10.3969/j.issn.1671-6833.2008.03.025
文献标志码:
A
摘要:
在脱氮要求条件下,选择脱氮型SBR运行模式,采取相应强化脱氮措施,研究味精废水SBR生物脱氮的效果.结果表明:进水阶段采用限制性曝气方式.运行工况为进水曝气8 h、厌氧搅拌1 h、后段曝气1 h、沉淀1 h、排水0.5 h;硝化反应过程pH值宜控制在8左右;硝化阶段、反硝化阶段溶解氧浓度宜分别控制在2.0 mg/L和0.5 mg/L左右;NH3-N污泥负荷宜控制在0.01~0.02 kg/(kg MLSS·d).当进水NH3-N浓度为18.2~269.1 mg/L时,出水浓度为8.0~38.4 mg/L,NH3-N的去除率范围为51.1%~87.7%,出水NH3-N指标能满足GB19431-2004<味精工业污染物排放标准>中50 mg/L的限值要求.
Abstract:
Under the conditions of nitrogen removal, the operation mode of denitrification SBR was selected, and corresponding enhanced nitrogen removal measures were taken to study the effect of biological denitrification of SBR in monosodium glutamate wastewater. The results show that restrictive aeration is adopted in the water influent stage. The operating conditions were 8 h of influent aeration, 1 h of anaerobic stirring, 1 h of aeration in the back section, 1 h of precipitation and 0.5 h of drainage. The pH value of the nitrification reaction process should be controlled at about 8; The concentration of dissolved oxygen in the nitrification stage and denitrification stage should be controlled at about 2.0 mg/L and 0.5 mg/L, respectively. NH3-N sludge load should be controlled at 0.01~0.02 kg/(kg MLSS·d).When the NH3-N concentration of influent is 18.2~269.1 mg/L, the effluent concentration is 8.0~38.4 mg/L, the removal rate range of NH3-N is 51.1%~87.7%, and the effluent NH3-N index can meet the limit value of 19431 mg/L in GB2004-50< monosodium glutamate industrial pollutant emission standard >.

更新日期/Last Update: 1900-01-01