欢迎访问《金属矿山》杂志官方网站,今天是 分享到:
×

扫码分享

金属矿山 ›› 2019, Vol. 48 ›› Issue (07): 189-193.

• 安全与环保 • 上一篇    下一篇

T-42树脂对沉钒废水中氨氮的动态吸附及解吸研究

郑巧巧1,张一敏1,2,3,4,黄晶2,3,4, 包申旭1,2,4   

  1. 1. 武汉理工大学资源与环境工程学院,湖北 武汉430070;2. 矿物资源加工与环境湖北省重点实验室,湖北 武汉430070;3. 国家环境保护矿冶资源利用与污染控制重点实验室,湖北 武汉430081;4. 钒资源高效利用湖北省协同创新中心,湖北 武汉430081
  • 出版日期:2019-07-15 发布日期:2019-09-17
  • 基金资助:

    基金项目:国家自然科学基金项目(编号:51774215),湖北省自然科学基金杰出青年项目 (编号:2018CFA068)。

Research on Dynamic Adsorption and Desorption of T-42 Resin on Ammonia Nitrogen in Vanadium Precipitated Wastewater

Zheng Qiaoqiao1,Zhang Yimin1,2,3,4,Huang Jing2,3,4,Bao Shenxu1,2,4   

  1. 1. School of Resource and Environmental Engineering, Wuhan University of Technology, Wuhan 430070, China;2. Hubei Province Key Laboratory of Mineral Resources Processing and Environment, Wuhan 430070, China; 3. State Key Laboratory of Environmental Protection Mineral Metallurgical Resources Utilization and Pollution Control, Wuhan 430081, China; 4. Hubei Collaborative Innovation Center for High Efficient Utilization of Vanadium Resources, Wuhan 430081, China
  • Online:2019-07-15 Published:2019-09-17

摘要: 为了了解T-42树脂吸附沉钒废水中氨氮的效果及其再生性能,研究了离子交换柱高径比、初始氨氮浓度和串联级数对吸附效果的影响,分析了等温吸附模型。此外,还研究了解吸过程中解吸剂的种类、流速、解吸剂溶液浓度对氨氮解吸效果的影响。结果表明:①当废水的流速为9 mL/min,柱高径比为21.0时,T-42树脂对氨氮的吸附效果较好,穿透点吸附量为21.91 mg/g,吸附终点吸附量为34.31 mg/g;随着初始氨氮浓度的升高,吸附量升高,处理废水量降低;氨氮浓度为1 999.56 mg/L的废水经2级串联吸附后达到一级标准(≤10 mg/L)。②T-42树脂吸附氨氮符合Langmuir等温吸附模型,吸附过程为单分子层化学吸附,在15、25、35 ℃下T-42树脂对氨氮的理论饱和吸附量分别为36.845 9、38.550 5、40.617 4 mg/g,温度升高有利于树脂的吸附。③在解吸剂硫酸溶液体积浓度为18%,流速为3 mL/min,解吸剂溶液用量为2.67个床层体积时,对吸附饱和的树脂上氨氮的解吸率大于99%。T-42树脂可以有效地去除废水中的氨氮,并且硫酸可以对吸附氨氮后的树脂进行解吸再生。

关键词: 沉钒废水, 树脂, 离子交换柱, 氨氮

Abstract: In order to understand the adsorption effect on ammonia nitrogen in vanadium precipitated wastewater and the recycle ability of T-42 resin, the influence of ratio of height to diameter of ion exchange column, original ammonia nitrogen concentration and series number on adsorption effect were studied,and the isothermal adsorption curve of T-42 resin was analyzed. In addition, the effect of the type, flow rate and concentration of desorbents on ammonia nitrogen desorption were also studied. The results showed that:①The adsorption effect of T-42 resin on ammonia nitrogen was better when the flow rate of wastewater was 9 mL/min and the ratio of height to diameter was 21.0. The adsorption capacity at the penetration point was 21.91 mg/g, and the adsorption capacity at the end point was 34.31 mg/g. The adsorption capacity of resin on ammonia nitrogen increases with original ammonia nitrogen concentration increasing, but the wastewater treated decreases. Wastewater with concentration of ammonia nitrogen 1 999.56 mg/L meets the standard Class One (≤10 mg/L) by two-stage series adsorption. ②The adsorption of ammonia nitrogen by resin matches the Langmuir isothermal adsorption model and the adsorption process is single molecular layer chemical adsorption. The saturated adsorption capacity is 36.845 9 mg/g in 15 ℃, 38.550 5 mg/g in 25 ℃, 40.617 4 mg/g in 35 ℃. The increasing temperature is beneficial to the adsorption. ③In the case of volume concentration of sulfuric acid 18%, flow rate 3 mL/min and desorbent dosage 2.67 bed volumes, the ammonia nitrogen desorption rate of adsorption saturated resin was higher than 99%. T-42 resin can effectively remove ammonia nitrogen from wastewater, and sulfuric acid can desorb and regenerate the resin which adsorbs ammonia nitrogen.

Key words: Vanadium precipitated wastewater, Resin, Ions exchange column, Ammonia nitrogen