• 제목/요약/키워드: melting slag

검색결과 90건 처리시간 0.032초

CaO-Al$_2$O$_3$-SiO$_2$계 슬래그와 스피넬의 반응에 미치는 스피넬중의 MgO함유량의 영향 (Effects of MgO content of Spinel on the Reaction of Spinel with CaO-Al$_2$O$_3$-SiO$_2$ Slag)

  • 조문규;홍기곤
    • 한국세라믹학회지
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    • 제36권4호
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    • pp.410-416
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    • 1999
  • The reactivity of three kinds of spinels which CaO-Al2O3-SiO2 slag was investigated in terms of mineral phases and microstructures. New crystal products were not formed by reaction of 12CaO.7Al2O3 in the slag with spinels and free MgO components was preferenctially dissolved into slag for MgO-rich spinel and stoichiometric spinel. Meanwhile mineral phase was changed from 12CaO.7Al2O3 to CaO.Al2O3 to CaO.2Al2O3 finally to CaO.6Al2O3 having high melting point for Al2O3 -rich spinel. The Fe-oxide component of the slag was taken up by only stoichiometric spinel grains within the spinel clinker and the trapped amount of Fe-oxide was independent of MgO content of MgO in spinel clinker the more th resistance to slag corrosion but the less resistance to slag penetration.

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저항센서를 이용한 제강용 슬래그 두께측정 방안 연구 (A study on the slag-thickness measuring system for steel making foundaries by using a resistivity detector.)

  • 김찬욱;임종인
    • 센서학회지
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    • 제9권2호
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    • pp.141-145
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    • 2000
  • 용강 및 고온슬래그의 현저한 저항차를 이용한 제강용 슬래그 두께 측정시스템을 개발하기 위하여 시험용 저항센서형 검출소자 제작 및 측정시스템을 구성하고 측정실험을 통하여 저항센서형 슬래그 측정시스템의 효율 및 측정정도 측면에 대하여 분석하였다. 분석결과 용강 및 슬래그의 저항차는 $10^3$ order로 확인되었으며 용강 및 슬래그의 이러한 현저한 저항차를 이용하여 고정도로 슬래그 두께를 측정할 수 있음을 보여주었다.

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용융환원법에 의한 LD제강 slag로부터 V의 회수(I) (The Recovery of Valuable Metals from LD-Slag by Smelting Reduction)

    • 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.

용융(熔融)슬래그로부터 Na-A형(型) 제올라이트의 수열합성(水熱合成) 거동(擧動)에 대(對)한 고찰(考察) (Behavior of Na-A Type Zeolite from Melting Slag in its Hydrothermal Synthesis)

  • 이성기;배인국;장영남;채수천;류경원
    • 자원리싸이클링
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    • 제17권4호
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    • pp.57-65
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    • 2008
  • 도시 소각재 용융슬래그로부터 반응시간 및 $SiO_2/Al_2O_3$의 비를 변화시키면서 Na-A형 제올라이트의 수열합성 거동에 대하여 고찰하였다. 반응시간에 대한 Na-A형 제올라이트를 수열합성한 반응물의 거동은 반응 초기에 첨가된 규산소다와 알루민산 소다가 먼저 반응하여 핵을 생성하였다. 생성된 핵은 시간이 지남에 따라 용융슬래그로부터 용해된 $SiO_2$$Al_2O_3$ 성분들과 반응하여 Na-A형 제올라이트로 성장되었다. 수열반응은 10시간 이내에 완결되며, 반응시간이 10시간 이상으로 증가하면 생성된 Na-A형 제올라이트가 용해되면서 하이드록시소달라이트로 변환되었다. 또한 $SiO_2/Al_2O_3=0.80{\sim}1.96$에서 Na-A형 제올라이트만 형성되었으나, $SiO_2/Al_2O_3=2.54$에서 Na-A형 제올라이트와 더불어 Na-P형 제올라이트가 생성되었다.

도시 소각재 용융슬래그로부터 P형 제올라이트 합성 (Synthesis of P-type Zeolite Using Melting Slag from Municipal Incineration Ash)

  • 이성기;장영남;채수천;류경원;배인국
    • 한국광물학회지
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    • 제19권1호통권47호
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    • pp.7-14
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    • 2006
  • 현대 산업사회의 큰 문제로 대두되고 있는 도시소각재를 용융시킨 용융슬래그를 출발물질로 하여 부가가치가 높은 P형 제올라이트를 "hydrogelation"법과 "clay conversion"법을 혼합한 새로운 방법에 의해 수열합성하였다. 출발물질은 용융슬래그 이외에 Si 공급원으로 시판되는 규산소다용액을, Al 공급원으로는 $Na_{2}O/Al_{2}O_{3}$의 비가 약 1.2인 알루민산소다용액을 사용하였다. $80^{\circ}C$의 반응 온도에서 P형 제올라이트의 최적합성조건은 $SiO_{2}/Al_{2}O_{3}$의 비율 $3.2{\sim}4.2,\;H_{2}O/Na_{2}O$의 비율 $70.7{\sim}80.0$, 그리고 반응시간이 15시간 이상일 때이었다. P형 제올라이트가 합성되었을 때, 크기가 일정하지 않은 용융슬래그 입자들은 용해되어 사라졌으며, 그 대신 균일한 크기의 P형 제올라이트 결정이 형성되었다. 암모니움 아세테이트법에 의해 측정된 합성 제올라이트의 양이온 교환능은 240cmol/kg 정도이었다.

석탄 및 폐기물로부터 합성가스 제조를 위한 가스화용융 Pilot Plant 운전특성 (Operation Characteristics of Gasification/Melting Pilot Plants for Synthesis Gas Production using Coal and Waste)

  • 정석우;윤용승;유영돈
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2005년도 춘계학술대회
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    • pp.561-564
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    • 2005
  • Gasification has been regarded as a very important technology to decrease environmental pollution and to obtain higher efficiency. The gasification process converts carbon containing feedstock into a synthesis gas, composed primarily of CO and $H_2$. And the synthesis gas can be used as a source for power generation or chemical material production. Through more than nine years, IAE developed and upgraded several gasification/melting pilot plant system, and obtained a good quality synthesis gas. This paper illustrates the gasification characteristics and operation results of two 3 ton/day synthesis gas production facilities. One is entrained-bed slagging type coal gasifier system which is normally operated in the temperature range of $1,400\~1,450^{\circ}C,\;8\~10$ bar pressure. And the other is fixed-bed type gasification/melting furnace system using MSW and industrial wastes as a feedstock.

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ESR공정분석 밑 해석 모델렁을 통한 최적 공정 선정 밑 제어에 대한 연구 (A Study on a control algorithm and determinant of an optimal process condition based upon ESR process analysis.)

  • 부광석;위철민;임태균
    • 제어로봇시스템학회:학술대회논문집
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    • 제어로봇시스템학회 2000년도 제15차 학술회의논문집
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    • pp.352-352
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    • 2000
  • ESR(ElectroSlag Remelting) Process is secondary fine process and melts steels by electric resistance heat and fines the melting steels by an appropriate solidification process parameters which affects the melting and solidification processes to get the high quality products. This paper describes a method to derive the mathematical model and analysis the dynamic characteristics for designing a controller of the ESR processes. The ESR process consists of a melting and solidificating processes and electrical system include the contact resistance mechanism. In this paper, we consider only the static relationship between inputs and outputs of the electric system because the dynamics of the electric system is so fast compared with the melting and solidificating processes which are analysed by using finite difference method. As the results, the fine processing in ESR is analysed and the process controller could be designed based on the process dynamic analysis.

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A Study on a control algorithm and determinant of an optimal process condition based upon ESR process analysis.

  • Hyun, Lim-Sung;Suck, Boo-Kwang;Gyoon, Lim-Tae;Min, Wi-Chul
    • 제어로봇시스템학회:학술대회논문집
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    • 제어로봇시스템학회 2001년도 ICCAS
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    • pp.76.4-76
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    • 2001
  • ESR(ElectroSlag Remelting) Process is secondary fine process and melts steels by electric resistance heat and fines the melting steels by an approproate solidification process. The final products are determined through the velocity of melting and the course of solidification in the process that is achieved by way of proper course of solidification. Thus, it is very important to monitor and control the process parameters which affects the melting and solidification process to get the high quality products. This paper describes a method to derive the mathematical model and analysis the dynamic characteristics for designing a controller of the ESR processes. The process consists of a melting and solidifying process and electrical system include the contact resistance mechanism ...

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철강산업 슬래그를 이용하여 제조한 바잘트 소재의 특성 (Characteristics of Basalt Materials Derived from Recycling Steel Industry Slags)

  • 정우광;백구슬;윤미정;이지욱
    • 한국재료학회지
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    • 제27권5호
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    • pp.281-288
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    • 2017
  • In this study, Fe-Ni slag, converter slag and dephosphorization slag generated from the steel industry, and fly ash or bottom ash from a power plant, were mixed at an appropriate mixing ratio and melted in a melting furnace in a mass-production process for glass ceramics. Then, glass-ceramic products, having a basalt composition with $SiO_2$, $Al_2O_3$, CaO, MgO, and $Fe_2O_3$ components, were fabricated through casting and heat treatment process. Comparison was made of the samples before and after the modification of the process conditions. Glass-ceramic samples before and after the process modification were similar in chemical composition, but $Al_2O_3$ and $Na_2O$ contents were slightly higher in the samples before the modification. Before and after the process modification, it was confirmed that the sample had a melting temperature below $1250^{\circ}C$, and that pyroxene and diopside are the primary phases of the product. The crystallization temperature in the sample after modification was found to be higher than that in the sample before modification. The activation energy for crystallization was evaluated and found to be 467 kJ/mol for the sample before the process modification, and 337 kJ/mol for the sample after the process modification. The degree of crystallinity was evaluated and found to be 82 % before the process change and 87 % after the process change. Mechanical properties such as compressive strength and bending strength were evaluated and found to be excellent for the sample after process modification. In conclusion, the samples after the process modification were evaluated and found to have superior characteristics compared to those before the modification.

염기도 조절에 의한 석면슬레이트 용융특성 (Melting Characteristics of Asbestos Cement Slate on Basicity Control)

  • 윤진한;길상인;민태진;이정규;장두훈
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2010년도 추계학술대회 초록집
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    • pp.159.2-159.2
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    • 2010
  • Asbestos is the collective name for a group of naturally occurring minerals in their fibrous form and hydrous silicates of magnesium and a mineral fiber that has been used commonly in a variety of building construction materials for insulation and as a fire-retardant. Asbestos has been used for a wide range of manufactured goods, because of its fiber strength and heat resistant properties. Nevertheless harmful of asbestos is quite serious. Exposure to airborne friable asbestos may result in a potential health risk because persons breathing the air may breathe in asbestos fibers. Continued exposure can increase the amount of fibers that remain in the lung. Fibers embedded in lung tissue over time may cause serious lung diseases including asbestosis, lung cancer. In this paper, we carried out as fundamental study for dispose of asbestos cement slate safely and perfectly. Melting Temperature of asbestos need to more than $1,520^{\circ}C$ and specially asbestos cement slate need more energy than that of pure asbestos. We need to decrease melting temperature of asbestos cement slate for economical efficiency. To the purpose, glass and bottom ash were chosen as additives for basicity control. we analyzed about properties of asbestos cements slate, melting characteristics on the additives ratio and temperature. We confirmed about harmlessness of melting slag through analysis of scanning electron microscope(SEM) and x-ray diffractometer(XRD).

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