• 제목/요약/키워드: Waste Catalyst

검색결과 177건 처리시간 0.031초

목질 폐재와 가정용 쓰레기의 열-화학적 분해에 의한 고수율 메탄가스(대체연료)의 합성 (Synthesis of Methane-rich Gases(Alternative Energy) by Thermochemical Gasification from Waste Municipal and Lignocellulosic Materials)

  • 이병근;이선행
    • Journal of the Korean Wood Science and Technology
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    • 제17권2호
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    • pp.13-19
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    • 1989
  • Two different quartz types of gasification reactor were used for pyrolysis and gasification of sawdust, ricestraw, ricehusk and municipal wastes which contain only cellulosics., operating at 1 atmospheric and vacuum pressure respectively. Also a stainless steel autoclave gasification reactor was used which is possible to use up to 100 atmospheric pressures and $800^{\circ}C$ of reaction temperature to complete pyrolysis and gasification reaction. The catalysts used in this reaction w- ere $K_2CO_3$, $Na_2CO_3$, Ni and Ni-$K_2CO_3$ as CO-Catalyst. The product gas mixtures were identified to be CO, $CO_2$, $C_3H_3$, $CH_4$ and $CH_3CHO$ etc. by Gas Chromatography and Mass Spectrometry. The pressurized gasification reaction shows significant increase in terms of methane composition and yield of product gases, comparing with those from unpressurized gasification reactions. The total volume of product gas mixtures amounts to 1600-1800ml per1gof waste of waste lignocellulosics or municipal waste, and the metane content of the gas mixtures reached to 40%, when $800^{\circ}C$ of reaction temperature and 100 atmospheric pressures with Ni-$K_2CO_3$ as CO-catalyst in the pressurized gasification reaction were used. This results show that the product gas mixtures containing 40% of methane call be used for alternative enegy source.

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폐플라스틱 분해 촉매의 특성 (Characterization of dissociation catalysts for waste plastics)

  • 김문찬;이철규
    • 분석과학
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    • 제23권4호
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    • pp.383-388
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    • 2010
  • 폐플라스틱을 오일로 전환하기 위하여 귀금속이 담지된 촉매를 사용하여 촉매 분해반응을 연구 하였다. 제조된 촉매의 결정 구조, 결정형태, 접촉분해 후 생성물의 분포를 알고자 XRD, SEM, GC/MSD 등의 분석을 시행하였다. 접촉분해 반응은 열분해반응에 비해서 저온에서 일어나며, 열분해생성물이 $C_1\simC_4$의 가스상이 대부분인데 비해, 액상화합물이 많아 휘발유 생성에 유리한 면이 있다. 접촉 분해반응결과 휘발유 성분이 많이 생성되었다. 귀금속이 담지된 촉매중 Pt-zeolite 촉매가 $340^{\circ}C$에서 $C_5\simC_{11}$ 근처의 휘발유 성상의 생성물 분포가 가장 많이 나타났으며, $340^{\circ}C$ 이상부터는 폐플라스틱(PE, PP, ABS)에 대해서 접촉 분해반응 전환율이 약 70% 이상인 것으로 나타났다.

An Insight Into the Recycling of Waste Flexible Polyurethane Foam Using Glycolysis

  • Woo Seok Jin;Pranabesh Sahu;Gyuri Kim;Seongrok Jeong;Cheon Young Jeon;Tae Gyu Lee;Sang Ho Lee;Jeong Seok Oh
    • Elastomers and Composites
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    • 제58권1호
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    • pp.32-43
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    • 2023
  • The worldwide use of polyurethane foam products generates large amounts of waste, which in turn has detrimental effects on the surroundings. Hence, finding an economical and environmentally friendly way to dispose of or recycle foam waste is an utmost priority for researchers to overcome this problem. In that sense, the glycolysis of waste flexible polyurethane foam (WFPF) from automotive seat cushions using different industrial-grade glycols and potassium hydroxide as a catalyst to produce recovered polyol was investigated. The effect of different molecular weight polyols, catalyst concentration, and material ratio (PU foam: Glycols) on the reaction conversion and viscosity of the recovered polyols was determined. The obtained recovered polyols are obtained as single or split-phase reaction products. Besides, the foaming characteristics and physical properties such as cell morphology, thermal stability, and compressive stress-strain nature of the regenerated flexible foams based on the recovered polyols were discussed. It was observed that the regenerated flexible foams displayed good seating comfort properties as a function of hardness, sag factor, and hysteresis loss compared to the reference virgin foam. With the growing demand for a sustainable and circular economy, a global valorization of glycolysis products from polyurethane scraps can be realized by transforming them into profitable substances.

탄소침적으로 피독된 탈질 촉매의 재생에 관한 연구 (A Study on the Regeneration of SCR Catalyst Deactivated by Unburned Carbon Deposition)

  • 문승현;이승재;유인수
    • 대한환경공학회지
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    • 제32권10호
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    • pp.928-935
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    • 2010
  • 폐 목재 소각 보일러 배가스로부터 질소산화물을 저감하기 위하여 설치된 선택적촉매환원 공정의 시운전 중에 전단에 설치된 여과포의 일부 소실이 발생되었다. 여과포 소실에 따른 불완전 연소 가스는 2단으로 설치된 저온 탈질촉매 표면을 미연탄소로 침적시켜 촉매의 탈질 효율을 급격히 저감시켰다. 활성 저하의 원인 분석을 위하여 XRD, EDX, BET, TGA, SEM 등 다양한 특성 분석을 실시하였다. 재생 방법으로 산 세척, 초음파 수 세척, 공기 중 소성의 방법을 적용한 결과, 공기분위기에서 $450^{\circ}C$로 2시간 소성하는 것이 최적조건 임을 밝혀내었다. 재생된 촉매는 2 cm ${\times}$ 2 cm ${\times}$ 10 cm(촉매 무게 10 g) Honeycomb 촉매 시료를 이용하여 활성을 측정한 결과 사용 전 촉매와 동일한 수준의 활성인 $180^{\circ}C$에서 NOx저감 효율 100%를 나타내었다.

석탄비산재(石炭飛散災)로부터 저밀도(低密度) 폴리에틸렌 폐기물(廢棄物) 열분해용(熱分解用) 저가(低價) 촉매(觸媒) 합성(合成) (Synthesis of Low-Priced Catalyst from Coal Fly Ash for Pyrolysis of Waste Low Density Polyethylene)

  • 정병환;나정걸;김상국;모세영;정수현
    • 자원리싸이클링
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    • 제16권2호
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    • pp.48-55
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    • 2007
  • 석탄화력발전소에서 부산물로 발생하는 비산재를 이용하여 저밀도 폴리에틸렌 열분해용 저가 크래킹 촉매를 합성하였다. 석탄비산재에 포함되어 있는 실리카와 알루미나를 NaOH와의 융합을 통해 용출시키고 이를 공침시킴으로써 비정질 실리카알루미나 촉매로 합성하였다. NaOH/석탄비산재 중량비와 활성화 시간 등의 합성조건이 촉매 합성에 미치는 영향을 살펴보기 위하여 열중량분석기를 사용하여 저밀도 폴리에틸렌 촉매 열분해를 수행하였다. 열분해 온도 변화와 열분해 생성물의 비점분포를 분석하여 합성 촉매의 성능을 평가하였으며 합성된 촉매의 물리적 특성과 촉매 활성간의 관계를 고찰하였다. NaOH/석탄비산재의 중량비가 1.2이고 활성화 시간이 8시간일 때 합성된 촉매가 가장 우수한 성능을 나타내었다. 최적 조건에서 합성된 촉매는 상용촉매와 유사한 활성을 나타내어 우수한 효과를 나타내었으며 폐플라스틱 재활용에 효과적으로 사용할 수 있으리라 예측된다.

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

  • 이건호;송태웅
    • 한국세라믹학회지
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    • 제42권7호
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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.

Polymeric Material Application for The Production of Ceramic Foam Catalyst

  • Sangsuriyan, Anucha;Yeetsorn, Rungsima;Tungkamani, Sabaithip;Sornchamni, Thana
    • International Journal of Advanced Culture Technology
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    • 제3권1호
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    • pp.21-30
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    • 2015
  • Ceramic foams are prepared as positive images corresponding to a plastic foam structure which exhibits high porosities (85-90%). This structure makes the ceramic foams attractive as a catalyst in a dry reforming process, because it could reduce a high pressure drop problem. This problem causes low mass and heat transfers in the process. Furthermore, the reactants would shortly contact to catalyst surface, thus low conversion could occur. Therefore, this research addressed the preparation of dry reforming catalysts using a sol-gel catalyst preparation via a polymeric sponge method. The specific objectives of this work are to investigate the effects of polymer foam structure (such as porosity, pore sizes, and cell characteristics) on a catalyst performance and to observe the influences of catalyst preparation parameters to yield a replica of the original structure of polymeric foam. To accomplish these objectives industrial waste foams, polyurethane (PU) and polyvinyl alcohol (PVA) foams, were used as a polymeric template. Results indicated that the porosity of the polyurethane and polyvinyl alcohol foams were about 99% and 97%. Their average cell sizes were approximate 200 and 50 micrometres, respectively. The cell characteristics of polymer foams exhibited the character of a high permeability material that can be able to dip with ceramic slurry, which was synthesized with various viscosities, during a catalyst preparation step. Next, morphology of ceramic foams was explored using scanning electron microscopy (SEM), and catalyst properties, such as; temperature profile of catalyst reduction, metal dispersion, and surface area, were also characterized by $H_2-TPR$ and $H_2-TPD$ techniques, and BET, respectively. From the results, it was found that metal-particle dispersion was relatively high about 5.89%, whereas the surface area of ceramic foam catalysts was $64.52m^2/g$. Finally, the catalytic behaviour toward hydrogen production through the dry reforming of methane using a fixed-bed reactor was evaluated under certain operating conditions. The approaches from this research provide a direction for further improvement of marketable environmental friendly catalyst production.