工业水处理 ›› 2025, Vol. 45 ›› Issue (9): 190-195. doi: 10.19965/j.cnki.iwt.2024-0866

• 工程实例 • 上一篇    

己酸乙酯生产废水处理工程实例

刘峻1(), 刘从彬2, 朱亚飞1, 李文达2   

  1. 1. 郑州亿众环境科技有限公司,河南 郑州 450006
    2. 江苏润环环境科技有限公司河南分公司,河南 郑州 450006
  • 收稿日期:2025-02-07 出版日期:2025-09-20 发布日期:2025-11-20
  • 作者简介:

    刘峻(1982— ),硕士,高级工程师,E-mail:

Example of ethyl hexanoate production wastewater treatment project

Jun LIU1(), Congbin LIU2, Yafei ZHU1, Wenda LI2   

  1. 1. Zhengzhou E-zone Environmental Science and Technology Co. , Ltd. , Zhengzhou 450006, China
    2. Henan Branch of Jiangsu Rainfine Environmental Science and Technology Co. , Ltd. , Zhengzhou 450006, China
  • Received:2025-02-07 Online:2025-09-20 Published:2025-11-20

摘要:

己酸乙酯生产过程中产生的废水具有高COD、低pH、高氨氮和高总氮等特征,高浓度废水(己酸生产工艺废水)采用“中和+铁碳微电解+中和-絮凝沉淀”工艺预处理后,与低浓度废水(己酸乙酯合成工艺废水)混合,而后采用“中和+UASB+A/O+二沉池”工艺处理。工程设计处理规模为160 m3/d(高浓度废水25 m3/d,低浓度废水135 m3/d)。铁碳微电解工艺可有效降解难降解有机物并提高废水可生化性,UASB可实现COD的高效厌氧降解,A/O工艺可确保深度脱氮效果。最终出水COD、NH3-N、TN、SS分别稳定低于300、30、50、150 mg/L,pH维持在6~9,满足河南省《化工行业水污染物间接排放标准》(DB 41/1135—2016)表1要求。该组合工艺具有处理效率高、运行稳定、运行成本低、管理方便等优点,可为具有类似特征的废水处理提供参考和借鉴。

关键词: 己酸乙酯生产废水, 铁碳微电解, 上流式厌氧污泥床, 厌氧/好氧工艺, 絮凝沉淀

Abstract:

The wastewater generated during the production of ethyl hexanoate was characterized by high COD, low pH, high ammonia nitrogen, and high total nitrogen. The high-concentration wastewater (from the hexanoic acid production process) was pretreated by “neutralization+iron-carbon micro-electrolysis+neutralization-coagulating sedimentation” process, and then mixed with the low-concentration wastewater (from the ethyl hexanoate synthesis process). The mixed wastewater was treated by “neutralization+UASB+A/O+secondary sedimentation tank” process. The designed treatment capacity of the project was 160 m³/d, including 25 m³/d for high-concentration wastewater and 135 m³/d for low-concentration wastewater. The iron-carbon micro-electrolysis process effectively degraded refractory organic compounds and improved wastewater biodegradability. The UASB achieved efficient anaerobic degradation of COD, and the A/O process ensured advanced nitrogen removal. The final effluent COD, NH3-N, TN, and SS were consistently below 300, 30, 50, and 150 mg/L, respectively, with pH maintained between 6 and 9, meeting the requirements of Table 1 in the Indirect Emission Standard of Pollutants in Chemical Industry(DB 41/1135—2016) of Henan provincial standard. This combined process exhibited high treatment efficiency, stable operation, low operating costs and convenient management features, making it a valuable reference for similar wastewater treatment scenarios.

Key words: ethyl hexanoate production wastewater, iron-carbon micro-electrolysis, up-flow anaerobic sludge blanket(UASB), anoxic-oxic process, coagulating sedimentation

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