• Korean Chemical Engineering Research
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• 제44권3호
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• pp.235-242
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• 2006

분무 열분해법이란 전구체를 용해시킨 용액을 수 마이크론에서 수십 마이크론 크기의 액적으로 분무한 후, 용매를 증발시키고 석출된 전구체를 열분해하여, 입자 및 필름을 제조하는 공정이다. 이 분무 열분해법의 핵심 요소는 전구체,용매, 액적 제조 그리고 분해 반응기 등 4가지이다. 이 4가지 요소의 적절한 조합에 의해서 현존하는 거의 대부분의 입자와 필름을 제조할 수 있는 범용성이 높은 기술이다. 현재 기술 수준으로는 상업적인 성공을 거두기는 힘들지만 향후 다성분계의 입자나 필름, 혹은 고기능성 입자의 제조에 응용될 경우 매우 유용한 기술로 각광을 받을 전망이다. 본 총설에서는 이 분문 열분해법을 이용해서 만들어지는 입자 중에서 주로 형광체를 중심으로 지금까지 개발된 다양한 분무 열분해 공정 기술을 소개한다

• 한국재료학회지
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• 제16권9호
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• pp.538-542
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• 2006

Nano-sized cobalt oxide powders were prepared by low pressure spray pyrolysis process. The precursor powders obtained by low pressure spray pyrolysis process from the spray solution with ethylene glycol had several microns size and hollow structure. The precursor powders obtained from the spray solution with optimum concentration of ethylene glycol formed the nano-sized cobalt oxide powders with regular morphology after post-treatment without milling process. On the other hand, the cobalt oxide powders obtained from the spray solution without ethylene glycol had submicron size and spherical shape before and after posttreatment. The mean size of the cobalt oxide powders formed from the spray solution with concentration of ethylene glycol of 0.7M was 180 nm after post-treatment at temperature of $800^{\circ}C$. The mean size of the powders could be controlled from several tens nanometer to micron sizes by changing the post-treatment temperatures in the preparation of cobalt oxide powders by low pressure spray pyrolysis process.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.742-745
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• 2001

Plastics are one of difficult materials for recycling due to their characteristics in use. Recycling ratio of waste plastics was around 40% in last year in Japan, which includes energy recovery. Feed stock recycling and mechanical recycling are not easy because of additives in commercial plastics. Then, pyrolysis treatments have been done to recovery energy. Although plastics are easy to fire, complete combustion of them is not easy if anti-firing agents are added especially. Therefore, researches on pyrolysis or combustion behaviors of plastics containing additives are important from a view point recycling of plastics. Direct observation of popular plastics like polystyrene (PS), polycarbonate (PC), polyphenyle ether (PPE) and polyvinyl chloride (PVC) to investigate their pyrolysis behaviors in the present study. In case of PS, melting and gas evolution started at 9$0^{\circ}C$ and 39$0^{\circ}C$ respectively. And combustion finished at 445$^{\circ}C$. On the other hand, more than $600^{\circ}C$ and sufficient oxygen are required for complete combustion of PC and PPE.

• 한국산학기술학회논문지
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• 제8권3호
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• pp.632-638
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• 2007

HDPE와 LDPE에 대한 열분해실험을 반응기 크기가 40 $cm^3$인 스테인레스 스틸 반응기에서 수행하였으며 이때 반응온도는 $410{\sim}460^{\circ}C$이었다. 열분해생성물인 액상생성물과 기상생성물을 분리하여 채취하였고 각 생성물의 분자량분포는 HPLC-GPC와 GC분석을 통해 얻었다. 미분반응기에서 열분해온도와 시간이 증가할수록 액상생성물의 수율과 분자량 분포는 전체적으로 감소하는 경향을 보였다. 열분해반응에서 말단절단의 속도계수인 활성화에너지 값은 HDPE, 63.0kcal/mole, LDPE, 45.7kcal/mole 이었다.

• 자원리싸이클링
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• 제13권1호
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• pp.3-13
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• 2004

바이오매스의 이용은 과거부터 지속되어 왔지만 최근 들어 새로운 대체에너지로의 활용이라는 측면에서 집중적인 연구가 시도되고 있다. 바이오매스를 이용하는 방법으로서의 fast pyrolysis는 다른 방법들보다 고부가가치의 화학물질을 생성할 수 있다는 점에서 크게 주목을 받고 있다. 이 리뷰 논문은 현재 fast pyrolysis를 바이오매스 전환 공정으로 이용하고 있는 실례를 선보이고 그 공정에서 생산되는 생성물인 bio-oil의 특성을 소개하고 있다.

• 한국연소학회:학술대회논문집
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• 대한연소학회 2003년도 제27회 KOSCO SYMPOSIUM 논문집
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• pp.243-250
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• 2003

The present study discuss about numerical methods to analyze design parameters of pyrolysis-melting incineration system. Various numerical methods of different viewpoint are introduced to simulate the performance of the system. Process analysis of the overall system is the beginning procedure of basic design process. Heat and material flow of each element are connected and are influential to each other, hence, an appropriate process modeling should be executed to prevent from unacceptable process design concepts that may results in system failure. Models to simulate performance of each elementary facility generate valuable informations on design and operation parameters, and, derive the basic design concept to be optimized. A pyrolysis model derived from waste bed combustion model is introduced to simulate the mass conversion and heat transfer in the pyrolysis process. CFD(Computational fluid dynamics) is an effective method to optimize the thermal reacting flow in various reactors such as combustor and heat exchanger. Secondary air jets arrangement and the shape of the combustor could be optimized by CFD technology.

• 공업화학
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• 제3권2호
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• pp.201-206
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• 1992

Annual amount of plastics waste including rubber and leather waste, generated in 1990 was about 2,600,000 tons. Amount of generation of plastics waste has rapidly increased, but fractions of recycling and incineration have gradually decreased. Recently, two-stage incinerator, consisting of gasifier and gas combustor, draws much attention in Korea. Plastics are gasified in the starved air condition in the gasifier and produced gas is fired in the combustor. Combustion of produced gas is much easier than that of solid plastics, and produces a little pollutants. Standardzation of technology and process automation are still needed, but this incineration technology is in the commercial stage. Next topic concerned with this two-stage incineration will be how to treat complex plastics waste including toxic substances generated from automobiles and household appliances. Pyrolysis, realized by indirect heating in inert atmosphere, can provide high-quality products with minimum emissions. Many plastics are easily decomposed into oil in pyrolysis conditions, which can be utilized as chemical feedstocks, or gasoline or kerosene depending on feed materials and operating conditions. This has been demonstrated in several pilot-scale tests performed in Japan, Germany, etc. Easy removal of HCl from PVC is one of the most decisive merits of pyrolysis process. But in general, further efforts should be made for the process to obtain marketability. The future of pyrolysis process depends on public concern about environmental problems and oil prices.

• 분석과학
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• 제8권4호
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• pp.487-492
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• 1995

The chemical compositions and pyrolysis characteristics of oil shales and source rocks distributed in the southwestern and southeastern parts of the Korean peninsular have been investigated. In order to compare the results of Korean samples with those of shales giving high oil yields, two Colorado oil shale samples and one Paris source rock samples were also investigated. Chemical compositions of the samples were analysed by means of gravimetry, CHN analysis, X-ray diffraction method, inductively coupled plasma atomic emission spectrometry and atomic absorption spectrometry. A custom made pyrolyser and a Rock-Eval system were used for the pyrolysis studies. Pyrolyses of the samples were carried out by means of a temperature controlling device to $600^{\circ}C$ at a heating rate of $5^{\circ}C/min$ with a helium flow rate of $1200m{\ell}/min$. The results of pyrolysis study indicated that Colorado shale samples belong to type I and all the other samples belong to type II.

• 공업화학
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• 제16권4호
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• pp.576-580
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• 2005

Magadiite 주형에 PFO (pyrolized fuel oil)와 Cobalt(II)2-ethylhexanoate 촉매를 함께 층간 삽입, $900{\sim}1100^{\circ}C$에서 3~24 h 동안 열분해하여 층간에 흑연 박막을 형성하고 magadiite 주형을 제거함으로서 다공성 흑연을 합성하였다. 소성시간이 길어질수록, 소성온도가 높을수록 흑연의 결정화도가 향상되었다. 비표면적은 PFO의 혼합비율, 소성시간, 소성온도에 따라 $261{\sim}400m^2/g$의 크게 다른 값을 나타내었다.

• 한국수소및신에너지학회논문집
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• 제15권4호
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• pp.333-340
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• 2004

In this study, thermochemical degradation by pyrolysis-liquefaction of cellulose, the effects of reaction time, reaction temperature, conversion yield, degradation properties and degradation products were investigated . Experiments were performed in a tube reactor by varying reaction time from 20 to 80 min at $200{\sim}500^\circ{C}$. Combustion heating value of liquid products from thermochemical conversion processes of cellulose was in the range of 6,920~6,960cal/g. After 40min of reaction at $400^\circ{C}$ in pyrolysis-liquefaction of cellulose, the energy yield and mass yield was as high as 54.3% and 34.0g oil/100g raw material, respectively. The liquid products from pyrolysis-liquefaction of cellulose contained various kinds of ketones, phenols and furans. ketones and furans could be used as high-octane-value fuels and fuel additives. However, phenols are not valuable as fuels.