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유종영,양대영,신희동,손일,Yu, Jong Yeong,Yang, Dae Young,Shin, Hee Dong,Sohn, Il 한국자원리싸이클링학회 2015 資源 리싸이클링 Vol.24 No.3
Raw materials in steel industry decide on the productivity, quality and price competitiveness. Utilizing iron-containing by-products as raw materials for steel products can save the cost of cleaning up iron-containing by-products and solve environmental issues. Iron-containing by-products have a small particle size. If they are directly inserted in a steel making process, it cause a problem such as poor heat flow and scattering. To solve these problems and induce the additional reduction, study concern with iron ore-coal mixed briquette technique are conducted by many researchers. In this paper, method of making carbon composite briquette iron(CCBI) using iron-containing by-products was studied. The effect of composition of Fe-containing process wastes, reducing agent, flux and binder on formability of CCBI (carbon composite briquette iron) was measured. 철강 산업에서의 원재료는 생산성, 품질, 가격경쟁력에 결정적인 역할을 하고 있다. 철강제품의 원재료를 함철부산물로 활용한다면, 함철부산물을 처리하기 위한 비용 및 환경오염문제를 해결할 뿐만 아니라 가격경쟁력을 높일 수 있다. 함철부산물들은 대부분 작읍입도를 가지고 있어서, 제강공정 내에 직접 투입하게 되면 열 유동 및 원료 비산 등의 문제가 발생하게 된다. 이러한 문제점을 해결하고 추가적인 환원을 유도하기 위해 철원에 탄재를 혼합한 뒤 단괴를 성형하여 제강공정 내에 투입하는 방법이 연구되고 있다. 본 연구에서는 함철부산물에 탄재를 혼합하여 단괴를 성형하는 방법에 대해 연구하였다. 함철부산물, 탄재, 융제, 바인더에 따른 CCBI (carbon composite briquette iron)의 성형성 및 압축강도를 확인하였다.
제강 슬래그를 활용한 탄산화 반응에 대한 속도론적 고찰
유종영 ( Jong Yeong Yu ),정성석 ( Sung Suk Jung ),손일 ( Il Sohn ) 대한금속재료학회(구 대한금속학회) 2015 대한금속·재료학회지 Vol.53 No.1
Carbonation of a synthesized CaO-Al2O3-MgO-SiO2 ladle refining slag has been kinetically studied using a thermo-gravimetric analyzer (TGA). The effects of extended basicity (CaO/Al2O3), temperature, and the crystal phase ratio were considered. The carbonation ratio and the initial reaction rate increased with basicity. However, for the same basicity of the slag, a decreasing crystal phase ratio seemed to accelerate the carbonation reaction due to the higher reactivity of the O2-ions within the slag. The carbonation ratio and the initial reaction rate were also found to increase with temperature in the range between 973 K and 1073 K, where the temperature effect was clearly observed at the onset of the reaction. Parameters were set to identify the carbonation mechanism and their values were calculated via regression analysis. The activation energy for carbonation was calculated to be 129.9 kJ/mol at C/A=1.0 and 109.0 kJ/mol at C/A=1.2. (Received February 24, 2014)