• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.526-531
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• 2001

LD slag, that is, a by-product of steel making process, has been mainly used as land construction materials. Recently, the seashore application of LD slag was tried in Japan and Korea tut the reaction between LD slag and seawater was not studied yet. We tried to clarify the leaching reaction and/or mechanism of LD slag and the reaction between seawater and LD slag. We tried to apply these results to the decarbonization of seawater for seawater magnesia process. At first, LD slag was milled and classified into 5 grades, that is, (ⅰ)45${\mu}{\textrm}{m}$ under, (ⅱ)0.25~0.5mm (ⅲ)0.5~1mm(ⅳ)1~2mm, (ⅴ)2.36~3.35mm. These slags were leached in the distilled water. In case of 45${\mu}{\textrm}{m}$ under, the pH of the leached solution was over 12. The chemical analysis of leached solution showed that the $Ca^{+}$$^2$was main component and the S $i^{+}$$^4$was very low. On the other hand, the content of S $i^{+}$$^4$in leached solution was decreased with the increase of pH of this solution. The nearly pure calcium solution was made and the ultra high purity MgO could be made with this calcium solution. The leaching behavior of LD slag was different between the fine particle and coarse particle. The calcium was leached by bulk dissolution in the coarse particle and by surface controlled reaction in fine particle. The leaching rate was slow in coarse particle and fast in fine particle. Therefore, the high pH solution, that is, over 12, was obtained in fine particle.cle.e.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.537-541
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• 2001

For the development of reformation material of soft ground using the LD slag, the relation to the particle condition of LD slag and the pH behavior of slag dissolution water, extraction properties of slag, and origination of white water were investigated. When the LD slag is mixed with sea water, the pH of solution ranged between 9.47 and 10.0. On the other hand, when mixed with distilled water, the pH was about 10.4 to 12.1. For the as-received slag and the aged slag in sea water, a pH of 11.5 to 12.0 was observed when the particle size was less than 0.5mm. For the reoxidized slag in seawater, the pH of the solution was lower than 9.5 when the particle size was bigger than 0.075mm. For the aged slag and reoxidized slag, the pH of the solution remained constant when the addition ratio of sea water to the slag was higher than 500 times. The main elements dissolved from the slag were Ca and Mg ions. When the pH went over 9.0, the white water started to font which was caused by the CaCO$_3$and Mg(OH)$_2$.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.532-536
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• 2001

LD slag, that is, a by-product of steel making process, has been mainly used as land construction materials. Recently, the seashore application of LD slag was tried in Japan and Korea but the reaction between LD slag and seawater was not studied yet. We tried to clarify the leaching reaction and/or mechanism of LD slag and the reaction between seawater and LD slag. We tried to apply these results to the decarbonization of seawater for seawater magnesia process. The high pH solution(over 12) was injected into the sea water and the pH of mixed liquid was adjusted to 9.8. This mixed solution was aged for 8 hours and the 104ppm of CO$_3$$^{-2}$ in the sea water was decreased to 23ppm with the negligible loss of $Mg^2$$^{+}$. The slag particle was directly inserted into the seawater fur practical application. The 0.5~1mm particles were suitable for decarbonization when 5 grade slags mentioned above were reacted with sea water. In this case, the content of CO$_3$$^{-2}$ in the sea water was 53 ppm with the negligible loss of $Mg^2$$^{+}$ after 8 hours aging. The direct application of slag particle fur the decarbonization of seawater takes more reaction time.ime.

• 자원리싸이클링
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• 제12권2호
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• pp.21-27
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• 2003

LD제강슬래그에 함유된 바나디움 회수를 위한 기초실험 결과로써 용융환원시 염기도 최적 염기도 및 환원효율의 증가를 위하여 $SiO_2$, MgO, $Al_2$$O_3$을 첨가하였다. 이에 따라 염기도 1, 2에서 $Al_2$$O_3$의 첨가에 따라 바나디움의 환원율이 증가함이 확인되었다.

• 자원리싸이클링
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• 제7권2호
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• pp.39-45
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• 1998

LD 제강 더스트를 제철원료로 LD 전로 제강 슬래그를 용제로 하고 폐타이어에 의해 제조한 건류탄을 환원제로 사용하여 반사로에서 환원 실험하여 배합비, 온도 및 반응시간 변화에 따른 환원율 및 철 회수율의 영향을 조사하여 다음과 같은 결과를 얻을 수 있었다. 1) $1300^{\circ}C$에서 1시간 동안 환원실험한 결과 탈아연율(removal rate of zinc)이 97%이상이며 잔사중의 Zn은 0.1~0.2%이었다. 2)페렛트 중에 LD 스래그 15~20%, 폐타이어 건류탄 4.1~6.7% 함유된 시료를 대기압, $1350^{\circ}C$에서 3시간동안 환원실험한 결과 선철의 회수율은 89.3~92%이었다. 3)환원제련시에 집진장치에서 회수한 더스튼 Zn 60%의 조산화아연이었다. 4) 회수한 선철의 성분은 Fe 96%, C 1.6%, P 0.08%, S 0.05%이었다. 5) 환원시에 생성한 슬래그의 조성은 $Ca_2Al_2SiO_7$, 8CaO $5SiO_2$ 및 $Na_3Ca_6(PO_4)_5$가 확인되었다.

• 한국대기환경학회지
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• 제15권2호
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• pp.191-199
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• 1999

This study evaluated the availability as an alternative adsorbent which is cheaper and more efficient than CuO/${\gamma}$-$Al_2O_3$ which have been studing vigorously to remove $SO_2$. Five adsorbents (CuO/${\gamma}$-$Al_2O_3$, Iron ore, Slag, LD slag, $Fe_2O_3$) was employed in a fixed bed reactor. $SO_2$ breakthrough curves were obtained as a function of temperature, initial gas velocity and particle size. Saturation capacities calculated by the numerical integration of breakthrough curves of $SO_2$ increased with increasing reaction temperature. $SO_2$ breakthrough curve equation of $Fe_2O_3$ for this system can be expressed as Kr=3,914,000 exp(-37,329.86/RT). By means of the breakthrough curve, the influence of bed height on breakthrough time was also estimated.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1991년도 한국자동제어학술회의논문집(국제학술편); KOEX, Seoul; 22-24 Oct. 1991
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• pp.1639-1645
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• 1991

Because of the important role LD converters play in the production of high quality steel, various dynamic models have been attempted in the past by many researchers not only to understand the complex chemical reactions that take place in the converter process but also to assist the converter operation itself using computers. And yet no single dynamic model was found to be completely satisfactory because of the complexity involved with the process. The process indeed involves dynamic energy and mass balances at high temperatures accompanied by complex chemical reactions and transport phenomena in the molten state. In the present study, a mathematical model describing the dynamic behavior of LD converter process has been developed. The dynamic model describes the time behavior of the temperature and the concentrations of chemical species in the hot metal bath and slag. The analysis was greatly facilitated by dividing the entire process into three zones according to the physical boundaries and reaction mechanisms. These three zones were hot metal (zone 1), slag (zone 2) and emulsion (zone 3) zones. The removal rate of Si, C, Mn and P and the rate of Fe oxidation in the hot metal bath, and the change of composition in the slag were obtained as functions of time, operating conditions and kinetic parameters. The temperature behavior in the metal bath and the slag was also obtained by considering the heat transfer between the mixing and the slag zones and the heat generated from chemical reactions involving oxygen blowing. To identify the unknown parameters in the equations and simulate the dynamic model, Hooke and Jeeves parttern search and Runge-Kutta integration algorithm were used. By testing and fitting the model with the data obtained from the operation of POSCO #2 steelmaking plant, the dynamic model was able to predict the characteristics of the main components in the LD converter. It was possible to predict the optimum CO gas recovery by computer simulation

• 자원리싸이클링
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• 제12권5호
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• pp.36-41
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• 2003

슬래그는 철분함량이 높아 자원으로의 활용이 가능하나 시장상황에 따라 매립되는 등 재활용이 활발히 이루어지지 않은 실정이다. 따라서 본 연구에서는 슬래그의 재활용이 즘 더 용이하도록 슬래그 내에 존재하는 철분 회수의 중요한 방법인 자력선별 방안에 대하여 고찰하였다. 수재 슬래그, 수냉 전로 슬래그, 공냉 전로 슬래그를 시료로 사용하였고 자장의 세기, 드럼의 회전속도, 슬래그의 투입량에 따른 철분 회수량에 대하여 조사하였다. 철분함량이 적은 수재슬래그는 피더의 진동수 및 드럼의 회전수가 느릴수록 회수율이 증가하였으며 0.5mm 이상의 입도에서 자력선별시 고품위의 철분을 얻을 수 있었다. 수냉의 전로 슬래그의 경우 피더의 진동수가 빠를수록, 드럼의 회전수가 느릴수록 회수율이 증가하는 것으로 조사되었고 입도의 크기가 작아질수록 입도별 회수율이 증가하는 것으로 관찰되었다. 공냉의 전로 슬래그는 피더의 진동수가 낮은 경우 드럼의 회전수가 감소할수록, 높은 경우는 드럼의 회전수가 증가할수록 회수율이 증가하는 것으로 나타났다. 또한 자력선별시 자장의 세기를 증가시키면 회수율은 증가하나 금속철 이외의 철 화합물의 혼입이 많아져 품위가 낮아지는 것으로 관찰되었다.

• 한국세라믹학회지
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• 제38권9호
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• pp.829-833
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• 2001

전로 내화물의 화학적인 부식에 대해서는 많은 연구가 이루어져 왔다. 그러나 전로 내화물의 자체 무게와 구조적인 형상으로 발생되는 응력집중에 의한 내화물의 부식에 대해서는 그 연구가 미비한 실정이다. 따라서 본 연구에서는 각이 진 노저부 형상을 가지는 전로(모델 1)와 완만한 곡선 형상을 가지는 전로(모델 2)에 대하여 FEM을 이용하여 자중응력분포 시뮬레이션을 행하고 그 결과를 비교분석 하였다. 시뮬레이션결과 슬래그 라인 근방에서 모델 2가 모델 1보다 높은 응력값을 나타내었다. 따라서 열적${\cdot}$화학적인 요인을 모두 고려한다면 조업 중기에 모델 2의 슬래그 라인 근방에서의 부식이 모델 1에 비해 심각할 것이라 결론 내릴 수 있다.