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金属矿山 ›› 2023, Vol. 52 ›› Issue (03): 147-151.

• 矿物工程 • 上一篇    下一篇

二次铝灰酸浸—微量加碱法制备聚合氯化铝

贺子洋1 谭欣雨1 张海泉2 林文亮2 卢绍铿2 吴国情2 吴 旭1
  

  1. 1. 华中科技大学环境科学与工程学院,湖北 武汉 430074;2. 武汉鸿劲金属铝业有限公司,湖北 武汉 430208
  • 出版日期:2023-03-15 发布日期:2023-04-12

Preparation of Polyaluminum Chloride by Acid Leaching and Micro-addition of Alkali Method Treating Secondary Aluminum Dross

HE Ziyang1 TAN Xinyu1 ZHANG Haiquan2 LIN Wenliang2 LU Shaokeng2 WU Guoqing2 WU Xu1   

  1. 1. School of Environmental Science and Engineering,Huazhong University of Science and Technology,Wuhan 430074,China;2. Wuhan Hongjing Metal Aluminum Co. ,Ltd. ,Wuhan 430208,China
  • Online:2023-03-15 Published:2023-04-12

摘要: 二次铝灰是再生铝工业生产中的主要副产物之一,已被列为危险废物,长期堆放或随意处置会引发许 多环境问题。 采用武汉某再生铝公司的二次铝灰,通过控制加碱改进的酸浸工艺制备聚合氯化铝。 研究了酸浸物料 投加比、酸浸温度、酸浸时间对铝灰中铝浸出率的影响及碱化度 B 值、加碱速率、加碱时温度对铝离子水解聚合形态 的影响。 结果表明,二次铝灰最优浸出条件为物料投加比 m铝灰 ∶mHCl ∶m水 = 1 ∶4 ∶4、酸浸温度 85 ℃ 、酸浸时间 2. 0 h,此 时铝的浸出率达 60. 30%;向优化条件下制得的酸浸液中缓慢滴加 15% Na2CO3 溶液制备聚合氯化铝,当碱化度 B 值 为 2. 4、加碱速率为 3. 6 mL / min、加碱时温度为 80 ℃时,聚合氯化铝中 Alb 含量最高,达 57. 49%。 该工艺成功制备了 聚合氯化铝,实现了二次铝灰的资源化和无害化处理。

关键词: 二次铝灰, 聚合氯化铝, 微量加碱法, 形态

Abstract: Secondary aluminum dross is one of the main by-products in recycled aluminum industry and has been classified as hazardous waste. Long-term stacking or arbitrary disposal for secondary aluminum dross could cause many environmental problems. The secondary aluminum dross from a recycled aluminum company in Wuhan was used to prepare polyaluminum chloride by improved acid leaching process through controlling alkali addition. The effects of material dosing ratio,acid leaching temperature and leaching time on the leaching rate of aluminum from aluminum dross were studied. The effects of alkalinity B value,alkali adding rate and temperature on the morphology of polyaluminum hydrolytic polymerization were studied. The results showed that the optimal leaching conditions of secondary aluminum dross are as follows:material dosing ratio of m( secondary aluminum dross) ∶m(HCl) ∶m(water)= 1 ∶4 ∶4,acid leaching temperature of 85 ℃ and acid leaching time of 2. 0 h,in which the leaching rate of aluminum in the acid leaching solution reached the maximum of 60. 30%. Polyaluminum chloride was prepared by slowly adding 15% Na2CO3 solution into acid leaching solution prepared under optimized conditions. When the alkalinity B is 2. 4,the alkali adding rate is 3. 6 mL / min,and the alkali adding temperature is 80 ℃ ,the content of Alb in the polyaluminum chloride reaches the highest of 57. 49%. The polyaluminum chloride was successfully prepared by this process, realizing the recycling and harmless treatment of secondary aluminum ash.