반도체 웨이퍼 製造工程 중 發生廢酸으로부터 Na₂SiF6 및 초산의 回收에 관한 硏究
Study on recovery of Na₂SiF6 and acetic acid from waste acid produced during semiconductor wafer process
0
조회
0
다운로드
0
인용
0
참고문헌
키워드
초록
반도체 웨이퍼 제조 공정 중 발생하는 질산, 불산, 초산으로 구성된 혼산을 재활용하기 위한 연구를 수행하였다. 초기에 NaNO₃ 와 Na₂SiO₃를 사용하여 불산을 Na₂SiF6로 침전시켜 회수하였고, 이 때 혼산 중 불산의 농도는 초기 110 g/L에서 0.5 g/L로 낮아져 불산 회수율은 99.5%였다. 불산회수 후 남은 혼산의 질산과 초산의 농도는 각각 498 g/L, 265 g/L였고, 이 혼산을 2단계 분별증류법에 의해 분리 • 회수하였다. 1단계에서는 초산을 증류하여 질산과 분리해내고, 2단계에서는 증류된 초산 중 잔류하는 미량의 질산을 제거하여 순수 초산만을 회수하였다. 회수된 초산의 농도는 약 20%였고, 최종회수율은 약 87.5%이었다.
Abstract
We researched recycle of mixed waste acids including HF, CH₃COOH, HNO₃ produced during semiconductor wafer process. At first, we recovered HF in form of Na2SiF6 by precipitation using NaNO₃ and Na₂SiO₃. Concentration of HF was made down from 110 g/L,initial concectration, to 0.5 g/L and Recovery rate of HF was 99.5%. After recovery of HF, concentration of HNO₃ and CH₃COOH is 498 g/L, 265 g/L respectively. From that mixed acid, we recovered CH₃COOH using 2 stages of fractional distillation. In first stage, CH₃COOH was distilled for separation from HNO₃. And in second stage, we recoverd refined CH₃COOH by using fractional distillation for removing a little amount of HNO₃ in CH₃COOH vapor. The concentration of recovered CH3COOH in second stage is 20% and finally recovery rate of CH₃COOH is about 87.5%.
참고문헌 (12)
- Yamamoto. A., "Recovery Process of Nitric and Hydrofluoric Acids from Waste Pickling Solutions for stainiess steel", Nissin steel Gihou, 40, pp.49~54 (1979)
- Kuylerstierna. U., "Solvent Extraction of HNO3-HF from Stainless Pickling Solutions", Proceedings from the International Solvent Extraction Conference, 통권 : 3, pp.2803~2816 (1974)
- 이향숙, "반도체 생산 공정에서 배출되는 폐산중 초산과 질산의 혼 합산 분리를 위한 기초 연구", 한국자원리싸이클링학회 추 계학술대회, pp.137~141 (2006)
- Yu, L., "Recovery of acetic acid from dilute wastewater by means of bipolar membrane electrodialysis", Desalination, 129(3), pp.283~288 (2000)
- Anasthas, H. M., "Adsorption of acetic acid on ion-exchange resins in non-aqueous conditions", Reactive & functional polymers, 47(1), pp.23~35 (2001)
- Tongwen, X., "Industrial recovery of mixed acid (HF + HNO3) from the titanium spent leaching solutions by diffusion dialysis with a new series of anion exchange membranes", Journal of membrane science, 220, pp.89~95 (2003)
- Hu Xinglan, "Simulation of extrative distillation of acetic acid-water", Computers and applied chemistry(China), 21(6), pp.828~830 (2004)
- Zhigang Lei, "Separation of acetic acid and water by complex extractive distillation", Separation and Purification Technology, 36, pp.131~138 (2004)
- Bock Heiko, "Analysis of reactive distillation using the esterfication of acetic acid as an example", Chemical engineering&technology, 3, pp.182~191
- Saha B., "Recovery of dilute acetic acid through esterification in a reactive distillation column", Catalysis Today, 60, pp.147~157 (2000)
- Seo Y. H., "Reaction kinetics of silicon etching in HF-K2Cr2O7-H2O solution", Korean J. of Chem. Eng, 11(2), pp.89~95 (1994)
