首页|高浓度贲亭酸甲酯生产废水的处理研究

高浓度贲亭酸甲酯生产废水的处理研究

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研究了Fe/C微电解耦合Fenton工艺对高浓度贲亭酸甲酯生产废水的预处理,在优化反应条件下,氧化出水经中和絮凝沉淀后,COD平均去除率达54%,B/C由 0.11提升到0.34.氧化预处理后的废水进入生物倍增系统,经驯化培养完成后,生物倍增系统兼氧区和好氧区的污泥质量浓度分别达10.4、11.5 g·L-1 以上,较传统污泥增长1.7倍以上.通过逐步提升进水盐分质量浓度对系统进行耐盐驯化,当盐分达到10 000 mg·L-1 时,出水中COD、NH3-N、TN质量浓度平均在400 mg·L-1、15 mg·L-1、35 mg·L-1 以下.对于高浓度的生产废水,全流程运行时,最终出水COD、NH3-N、TN质量浓度分别在400 mg·L-1、5 mg·L-1、20 mg·L-1 以下,平均去除率分别达到94.5%、97%、90%.
Study on Treatment of High Concentration Wastewater From Production of Methyl 3,3-Dimethyl-4-pentenoate
The pretreatment of high concentration wastewater from the production of methyl 3,3-dimethyl-4-pentenoate by Fe/C micro-electrolysis coupled with Fenton process was studied,under the optimized reaction conditions,the effluent after the oxidation was neutralized,flocculated and precipitated,the average removal rate of COD reached 54%,and B/C increased from 0.11 to 0.34.The wastewater after oxidation pretreatment entered the biological multiplication system,after domestication and cultivation,the sludge mass concentrations in the facultative and aerobic areas of the biological multiplication system were 10.4 g·L-1and 11.5 g·L-1 respectively,it was 1.7 times more than traditional sludge.The salt tolerance of the system was acclimatized by gradually increasing the salt mass concentration of the influent water,when the salinity reached 10 000 mg·L-1,the average mass concentrations of COD,NH3-N and TN in the effluent were below 400 mg·L-1,15 mg·L-1and 35 mg·L-1.For production wastewater with high concentration,when the whole process was running,the mass concentrations of COD,NH3-N and TN in the final effluent were below 400 mg·L-1,5 mg·L-1and 20 mg·L-1 respectively,and the average removal rates were 94.5%,97%and 90%respectively.

Micro electrolysisPolyphase FentonBiological multiplicationMethyl 3,3-dimethyl-4-pentenoate

王忠泉

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中煤科工集团杭州研究院有限公司,浙江 杭州 311201

微电解 多相芬顿 生物倍增 贲亭酸甲酯

中国煤炭科工集团有限公司科技创新创业资金专项

2022-2-MS007

2024

当代化工
中国石油抚顺石化公司,中国石化抚顺石油化工研究院,沈阳市医药和化工行业联合会

当代化工

CSTPCD
影响因子:0.412
ISSN:1671-0460
年,卷(期):2024.53(4)
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