铁/炭微电解-Fenton氧化技术处理1,2,4酸生产废水
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国家水体污染控制与治理科技重大专项(2009ZX07315-005)


Treatment of 1,2,4-acid wastewater by ferric-carbon microelectrolysis combined with Fenton oxidation process
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    摘要:

    以6硝(6硝基1,2重氮氧基萘4磺酸)生产过程中产生的1,2,4酸废水作为研究对象,将铁/炭微电解和Fenton氧化技术结合进行废水处理,研究了微电解的pH值、反应时间、反应温度、铁炭质量比、活性炭用量的影响以及Fenton氧化的pH值和H2O2用量,并进行了处理工艺的经济性分析。通过单因素实验确定1,2,4酸废水处理的工艺条件为铁碳微电解的pH值为1时,铁碳质量比为3〖DK〗∶1,反应3 h,过滤,调pH值为3,添加废水体积2.5%的H2O2(质量分数为30%),反应1 h,电石渣调pH值7~8,过滤。该工艺对废水COD的去除率可提高到95%以上,废水处理成本5.4元/m3。

    Abstract:

    Experiments on the treatment process of 1,2,4-acid wastewater combined ferric-carbon microelectrolysis with Fenton oxidation process are carried out. The 1,2,4-acid wastewater is produced in the production process of 6-nitry(6-nitro-1-diazo oxygen naphthalene-4-acid). The experimental conditions of Ferric-Carbon microelectrolysis, including pH value, react time, react temperature, Fe/C ratio and dosage of active carbon are studied. Fenton oxidation conditions of pH value, dosage of H2O2 and the economy data of the process are analyzed. Through single-factor experiments, the conditions for treating acid wastewater are found out. pH value is 1, Fe and C mass ratio is 3〖DK〗∶1, and iron-carbon micro-electrolysis reaction time is 3 h. Filter the iron-carbon micro-electrolysis water to adjust its pH value into 3, and then adding 2.5% wastewater of H2O2 with mass fraction of 30 %, react at room temperature for 1 h, adjust the pH value into 7~8, and then filter the iron-carbon micro-electrolysis water. The removal efficiency of COD of raw water can be improved to more than 95%. The cost of wastewater treating is 5.4 yuan/m3.〖HQ〗

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原金海,鲜学福,雷菊.铁/炭微电解-Fenton氧化技术处理1,2,4酸生产废水[J].重庆大学学报,2011,34(9):121-127.

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  • 收稿日期:2011-04-08
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