• Title/Summary/Keyword: Spent oil-refining catalyst

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Synthesis and Properties of Calcium Sulfoaluminate Clinker Using Waste Shell, Spent Oil-Refining Catalyst and Desulfurized Gypsum (폐패각-정유폐촉매-배연탈황석고를 사용한 Calcium Sulfoaluminate 클링커의 합성과 특성)

  • Lee, Keon-Ho;Song, Tae-Woong
    • Journal of the Korean Ceramic Society
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    • v.42 no.7 s.278
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    • pp.483-489
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    • 2005
  • For the raw materials of 3CaO$\cdot$3Al$_{2}$O$_{3}$ $\cdot$CaSO$_{4}$(CSA) clinker manufacturing, the applications of industrial wastes such as waste shell, spent oil-refining catalyst and desulfurized gypsum were examined. The c1inkerbility of the raw mix and the behaviour of formation of clinker minerals were studied and then some hydraulic properties of cements containing the clinker were also investigated. By virtue of the high reactivity of thermally decomposed raw materials, CSA clinkers were obtained at relatively low temperature of 1250$^{\circ}C$ and thus oil-refining catalysts were more desirable than aluminium hydroxide as an aluminous raw material. The expansive cement samples showed somewhat lower flow value than that of OPC, but their compressive strengths were developed earlier and higher than that of OPC due to formation of ettringite in the early hydration time, which indicated the possibility of practical use of low-cost CSA clinker using industrial wastes only.

Study on the Synthesis of Tricalcium Aluminate Clinker from Waste Shell and Spent Oil-Refining Catalyst (폐 패각과 정유 폐촉매를 사용한 Tricalcium Aluminate 클링커의 합성에 관한 연구)

  • Lee, Keon-Ho;Song, Tae-Woong
    • Journal of the Korean Ceramic Society
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    • v.41 no.12 s.271
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    • pp.933-938
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    • 2004
  • The clinkerbility and the behaviour of formation of $3CaO{\cdot}Al_{2}O_3$ were studied using the mixture of waste oyster shell and spent oil-refining catalyst mainly by the mineral and microstructural observation. By virtue of the formation of $12CaO{\cdot}7Al_{2}O_3$ at relatively low temperature and its successive reaction with CaO, the $3CaO{\cdot}Al_{2}O_3$ clinkers were formed easily without affection of minor constituents contained in oyster shell. Thus clinkers were formed at $1400^{\circ}C$ directly but began to melt incongruently at higher temperature above that. Aluminium hydroxide, however, was not desirable as an aluminous raw materials of the clinker because rapid melting occurs before $3CaO{\cdot}Al_{2}O_3$ forms main clinker mineral.

Recovery of Precious Metals from Spent Catalyst Generated in Domestic Petrochemical Industry (한내 석유화학 폐촉매로부터 귀금속의 회수 연구)

  • 김준수;박형규;이후인;김성돈;김철주
    • Resources Recycling
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    • v.3 no.1
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    • pp.17-24
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    • 1994
  • Recovery of precious metal values from petrochemical spent catalyst is important from the viewpoint of environmental protection and resource recycling. Two types of spent catalysts were used in this study. One used in the manufacture of ethylene contains 0.3% Pd in the alumina substrate. The other used in oil refining contains 0.3% Pt and 0.3% Re. Both spent catalysts are roasted to remove volatile matters as carbon and sulfur. Then, metallic Pd powder from Pd spent catalyst is obtained in the course of grinding, hydrochloric acid or aqua regia leaching and cementation with iron. For the recovery of Pt and Re from Pt-Re spent catalyst, Pt and Re are leached with either HCI or aqua regia, first. Metallic Pt powder is recovered from the leach solution by cementation with Fe powder. Re in sulfide form is precipitated by the addition of sodium sulfide to the solution obtained after Pt recovery. It is found that 6N HCI can be successfully used as leaching agent for both types of spent catalyst. 6N HCI is considered to be better than aqua regia in consideration of reagent and equipment cost.

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A Study on Types and Reasons of Engine Troubles Related to Fuel Oil (연료유에 의한 선박 디젤엔진 손상에 관한 연구)

  • Na, Eun-Young;Baik, Shin-Young
    • Journal of the Korean Society for Marine Environment & Energy
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    • v.12 no.3
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    • pp.143-150
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    • 2009
  • Fuel oil mostly used for a ship is made from crude oil by refining process. In order to produce plenty of high-quality fuel oil, the Fluid catalytic cracking(FCC) method is widely adopted to many refinery factories during the decomposition process from high molecule into lower molecule. The major constituents in spent FCC catalysts are Si, Al, Fe, Ti, alkali metals and some others. The spent catalyst is also composed small amounts of rare metals such as Ce, Nd, Ni and V. The big problem in FCC oil is mixing the catalyst in the oil. This reason is unstable separation of FCC catalyst in separator. Such a FCC catalyst will become a reason of heavy wear down in moving parts of engine. The impurity in oil is ash and deposit compound, such as Al, Si, Ni, Fe and V, which will accelerate the wear down on fuel pump, fuel injection valve cylinder liner and piston ring. It is important to find a basic reason of an engine trouble for preventing similar troubles anymore. Insurance compensation will be different according to the reason of an engine trouble which might be natural abrasion or other external causes. In this study, types and reasons of engine troubles related to fuel oil will be covered.

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