化工进展 ›› 2019, Vol. 38 ›› Issue (08): 3896-3901.DOI: 10.16085/j.issn.1000-6613.2018-2231

• 资源与环境化工 • 上一篇    下一篇

沉淀-氧化法处理乙烯废碱液

王凤荣1(),马克存1(),王天成2,杜龙弟1,郭桂悦1   

  1. 1. 中国石油天然气股份有限公司大庆化工研究中心,黑龙江 大庆 163714
    2. 浙江大学化学工程与生物工程学院,浙江 杭州 310027
  • 收稿日期:2018-11-15 出版日期:2019-08-05 发布日期:2019-08-05
  • 通讯作者: 马克存
  • 作者简介:王凤荣(1972—),女,工程师,研究方向为化工废水处理技术。E-mail:wfr459@petrochina.com.cn

Treatment of ethylene waste lye by precipitation-oxidation

Fengrong WANG1(),Kecun MA1(),Tiancheng WANG2,Longdi DU1,Guiyue GUO1   

  1. 1. Daqing Petrochemical Research Center of PetroChina, Daqing 163714, Heilongjiang, China
    2. College of Chemical and Biological Engineering, Zhejiang University, Hangzhou 310027, Zhejiang, China
  • Received:2018-11-15 Online:2019-08-05 Published:2019-08-05
  • Contact: Kecun MA

摘要:

采用沉淀-氧化法处理乙烯废碱液中的硫化物,考察了影响脱硫效果的各种因素。在n(CuSO4)∶n(Na2S)=1.1∶1、温度为40℃、时间为0.5h条件下,沉淀法脱硫后碱液残留的S2-浓度为0.04g/L;然后进一步采用双氧水氧化处理脱硫后碱液,在氧化反应温度为40℃、时间为2h、氧化剂双氧水用量为1.0mL/L废碱液时,乙烯废碱液中的S2-浓度可降至1mg/L以下,达到湿式氧化的处理效果和烟气脱硫对乙烯废碱液的要求。同时硫酸铜湿法氧化再生研究结果表明:在硫化铜浆液质量分数为15%、pH=3、氧分压为0.5MPa、温度为200℃、时间为0.5h的条件下,硫酸铜再生彻底,实现了硫酸铜的循环利用。

关键词: 乙烯, 废碱液, 脱硫, 沉淀, 氧化, 湿法氧化

Abstract:

Precipitation-oxidation process was used to treat sulfide in ethylene waste lye. The factors affecting removing efficiency were investigated. Under the condition of n(CuSO4)∶n(Na2S)=1.1∶1、temperature 40℃ and 2h, S2- in lye residue after desulfurization by precipitation was 0.04g/L. Then the lye after desulphurization was further treated by oxidation with hydrogen peroxide. When the oxidation reaction temperature is 40℃, the time is 2h, and the amount of oxidant hydrogen peroxide is 1.0mL/L waste lye, The S2- in ethylene waste lye could be reduced to below 1mg/L, and it meets the treatment effect of wet oxidation technology and the requirements of flue gas desulfurization for ethylene waste lye. At the same time, wet oxidation regeneration of copper sulfate was also studied. The results showed that: under the conditions of 15% concentration of copper sulfide slurry, pH=3, oxygen partial pressure of 0.5MPa, reaction temperature of 200℃, and reaction time of 0.5h, copper sulfate regeneration was complete. The recycling utilization of copper sulfate was realized.

Key words: ethylene, spent caustic, desulfurization, precipitation, oxidation, hydrometallurgy

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