• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.393-397
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• 2001

The innovatory process, that is the direct separation and recovery of the iron and zinc metals contained in the high temperature exhaust gas generated from the electric arc furnace fer the inn scrap melting and/or the dust treatment, has been proposed. This proposed process consists of the moving coke bed filter that is directly connected to the electric furnace, and the following heavy metal condenser. The exhaust gas passes through the filter and the condenser right after exhausting from the electric furnace. The moving coke bed filter is being controlled at about 1000℃ and collects iron and slag components contained in the high temperature exhaust gas. Heavy metals such as zinc and lead pass through the filter as vapor. Based on the thermodynamic considerations, the iron oxide and the zinc oxide are reduced in the filter. The solution loss reaction rate is comparatively low at about 1000℃ in the coke bed filter by the analysis using the mathematical simulation model. The heavy metal condenser is installed in the position after the coke bed filter, and rapidly cools the gas from about 1000℃ to 450℃ by a full of the cooling medium like the solid ceramic ball in addition to the cooling from the wall. The zinc and lead vapor condense and separate f개m the gas in a liquid state. The investigation of the characteristics of the exhaust gas of the commercial electric arc furnace, the fundamental experiments of the laboratory scale and the bench scale ensured the formation of this proposed process. A small-scale pilot plant examination is carrying out at present to confirm the formation of the process. It is certain that the dust generation of the electric arc furnace is extremely decreased, and it can save the energy consumption of usual dust treatment processes by the realization of this process.

• 한국세라믹학회지
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• 제40권8호
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• pp.804-810
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• 2003

건설폐기물 중 폐콘크리트를 40$0^{\circ}C$로 가열한 후 ball mill로 분쇄하여 재생골재를 생산할 때 발생된 미분말을 보통 포틀랜드 시멘트의 SiO$_2$, CaO, A1$_2$O$_3$원에 대한 대체원료물질로서 활용하고자 하였다. 클링커를 제조하기 위한 주원료는 석회석, shale, 전로슬래그, fly ash를 이용하였고, modulus는 LSF:91.0, SM:2.60, IM:1.60로 고정한 후 shale에 대해 미분말을 25, 50, 15, 100%까지 치환하여 클링커를 제조하였다. 클링커의 주요생성광물은 1,45$0^{\circ}C$에서 OPC와 같은 광물상인 $C_3$S, $\beta$-C$_2$S, $C_3$A, $C_4$AF 상으로 나타났다. 조합원료의 반응성을 비교하기 위해 시차열분석을 실시하고, 소성성지수를 구한 결과, 클링커의 광물상 생성온도는 plain과 유사했으며, 소성성지수는 48.6-51.4 정도로 나타났다.