자원리싸이클링 (Resources Recycling)

  • 제32권1호
  • /
  • Pages.33-41
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  • 2023
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  • 2765-3439(pISSN)
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  • 2765-3447(eISSN)
한국자원리싸이클링학회 (The Korean Institute of Resources Recycling)
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제강분진으로부터 습식제련공정에 의한 황산아연의 제조 연구

Study for Manufacturing of Zinc Sulfate from Electric Arc Furnace Dust by Hydrometallrugical Process

  • 신동주 (한국지질자원연구원 자원활용연구본부 순환자원연구센터) ;
  • 주성호 (한국지질자원연구원 자원활용연구본부 순환자원연구센터) ;
  • 이동석 (한국지질자원연구원 자원활용연구본부 순환자원연구센터) ;
  • 신선명 (한국지질자원연구원 자원활용연구본부 순환자원연구센터)
  • Dong Ju Shin (Resources Recycling Research Center, Resources Utilization Division, Korea Institute of Geoscience and Mineral Resources(KIGAM)) ;
  • Sung-Ho Joo (Resources Recycling Research Center, Resources Utilization Division, Korea Institute of Geoscience and Mineral Resources(KIGAM)) ;
  • Dongseok Lee (Resources Recycling Research Center, Resources Utilization Division, Korea Institute of Geoscience and Mineral Resources(KIGAM)) ;
  • Shun Myung Shin (Resources Recycling Research Center, Resources Utilization Division, Korea Institute of Geoscience and Mineral Resources(KIGAM))
  • 투고 : 2022.12.16
  • 심사 : 2023.01.03
  • 발행 : 2023.02.28
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초록

본 연구에서는 제강분진으로부터 습식제련을 이용하여 아연을 선택적으로 회수하고 황산아연을 제조하고자 하였다. 제강분진의 성상분석을 통해 기존의 제강분진과 다르게 철의 함유량이 9.9%로 상대적으로 낮고 망간이 19%로 다량 함유되어 있었으며 이에 알맞은 습식제련 공정을 설계하였다. 침출공정에서는 고액비, 온도, 황산 농도별 실험을 통해 1.6M 황산, 20% 고액비, 60℃, 1시간동안 침출하여 85%의 아연, 망간을 용해시키고 철은 침출되지 않았다. 망간으로부터 아연을 선택적으로 회수하기 위해 D2EPHA를 사용한 용매추출 공정을 선택하였고 0.8M D2EHPA, 32% 비누화도, O/A 비 2, 향류 3단 추출을 통해 에서 99% 아연을 추출하였으며, 공동 추출된 망간은 pH 1.5로 조정한 황산 수용액으로 전량 세정하였다. 최종적으로 1.5M 황산을 이용하여 O/A 비 4, 향류 4단 탈거를 통해 아연을 농축 탈거하였다. 탈거액에는 40g/L의 아연이 함유되어 있었으며 이를 감압증류하여 99.9%의 황산아연 1수화물을 획득하였다.

Herein, we selectively recovered Zn and produced ZnSO4 from electric arc furnace dust using a hydrometallurgical process. The analysis of the properties of the electric arc furnace dust revealed that the Fe content (9.9%) was relatively low while the Mn content (19%) was high as compared to the composition of general dust. Therefore, an appropriate hydrometallurgical process was designed based on the properties of the raw materials. In the leaching process involving the use of 1.6 M sulfuric acid and 20% solid-liquid ratio at 60℃ for 1 h, 85% of the Zn and Mn got dissolved while the Fe was not leached. To selectively recover Zn, a solvent extraction process using D2EHPA as the extractant was chosen, and 99% of the Zn was extracted using 0.8 M D2EHPA with 32% saponification and an O/A ratio of 2 using counter-current 3-stage extraction. Mn was entirely scrubbed with an aqueous sulfuric acid solution of pH 1.5. Finally, Zn was concentrated and stripped using 1.5 M sulfuric acid at an O/A ratio of 4 using counter-current 4-stage stripping. The stripping solution contained 40 g/L of Zn, and 99.9% of ZnSO4∙H2O was obtained by vacuum distillation.

키워드

과제정보

본 연구는 산업통상자원부의 재원으로 철강재도약기술개발사업의 지원을 받아수행하였습니다(과제번호: 20016885).

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