• 한국신재생에너지학회:학술대회논문집
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• 2008.05a
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• pp.483-486
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• 2008

본 연구에서는 디스크 이동식 열분해 실증 설비를 이용하여 폐타이어 열분해 반응을 수행하였고, 생성된 열분해 생성물들의 특성을 분석하였다. 폐타이어 열분해 반응은 약 $550^{\circ}C$에서 90분간 진행되었고, 반응 결과 Recovered Oil, Carbon Black, Non Condensing Gas(NC Gas)가 생성되었다. 폐타이어 열분해 생성물의 수율은 Recovered Oil $40{\sim}50%$, Carbon Black 30$\sim$35%, NC Gas 10$\sim$15%, Steel 10$\sim$15%로 나타났다. 폐타이어 열분해 반응 후 생성된 Recovered Oil은 비점 및 특성 분석 결과 상업용 중유와 비슷한 성질을 나타냈고, 폐타이어 열분해 반응의 또 다른 생성물인 Carbon Black은 특성 분석 결과 고정 탄소 비율이 낮은 반면 회분과 휘발분의 비율이 높아 상업용으로 사용하기 위해서는 적절한 정제 과정이 필요함을 알 수 있었다.열분해 과정 중에 생성된NC Gas는 GC/MS를 이용하여 성분 분석을 수행한 결과, $CO_2$, $CH_4$를 비롯하여 주로 탄화수소류로 이루어졌으며, 대부분이 연료 가스로 구성되어 있어 열분해 반응의 열원으로서 사용이 가능하였다.

• Applied Chemistry for Engineering
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• v.19 no.5
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• pp.568-573
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• 2008

Kinetic tests on pyrolysis of waste fishing net [WFN; nylon-6], waste ship lubricating oil [WSLO] and their mixture were carried out by thermogravimetric analysis (TGA) with heating rate of 0.5, 1.0, and $2.0^{\circ}C/min$. Pyrolysis of waste fishing net started at $300^{\circ}C$, and the main region of decomposition temperature was between 360 and $440^{\circ}C$ at each heating rate. Decomposition temperature of the mixture of WFN and WSLO was lower than that of WFN and WSLO, and the shape of thermogravimetic graph of mixture was different as well. The corresponding kinetic parameters including activation energy and pre-exponential factor were determined by differential method over the degree of conversions. The values of activation energies for the mixture of WFN and WSLO were between 98 and 427 kJ/mol as the conversion increased from 5% to 95%. Tubing reactor was used to analysis of pyrolyzed oil at $440^{\circ}C$ for 80 min. The selectivity of specific hydrocarbons was not detected and the carbon number distribution of the pyrolyzed oil was below $C_{22}$.

• Proceedings of the Korean Vacuum Society Conference
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• 2011.02a
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• pp.363-363
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• 2011

열분해 반응기 내에서 실리콘 필름을 성장시키는 것은 반도체/디스플레이, 태양전지, 신소재 등 다양한 분야에서 중요한 공정이다. 더욱이 반도체 소자 선폭이 줄어들면서 나노입자의 오염 제어가 더불어 중요해지고 있다. 생산 공정 기술의 집적화에 따라 패턴 사이 거리가 작아지고, 이에 불과 수 십 나노미터크기의 오염입자에 의해서 패턴불량이 발생하고 생산수율을 감소시킨다. 일반적으로 반도체 공정 중 발생한 오염입자는 반응기 내의 가스가 물리/화학적 공정에 의해 핵생성(nucleation)이 일어나 핵(nuclei)이 생성되고, 이 때 표면반응 및 응집(coagulation)에 의해 성장하게 된다. 이에 본 연구에서는 열분해 반응기 내에서 사일렌(SiH4) 가스를 열분해하여 발생되는 실리콘 오염입자의 핵생성과 성장 모델을 정립하고, 생성된 오염입자의 거동과 전달 현상을 이론적으로 고찰하였다. 열분해 반응기와 같은 기상공정(Gas to particle conversion)에서 오염입자가 생성될 때, 그 성질과 크기 등에 물리/화학적 영향을 주는 요소는 전구체/이송기체의 농도 및 유량, 작동 압력, 작동 온도와 반응기 고유 특성 등이 있다. 수치해석의 정당성과 빠른 계산을 위해 단순화시킨 0D 모델인 Batch 반응기와 1D모델인 plug flow 반응기 등에서 SiH4 가스의 열분해 과정시 생성되는 Si cluster를 상용코드인 CHEMKIN 4.1.1을 이용하여 계산하였으며, 2D모델인 Shear flow 반응기로 확장시켜 Si 오염입자가 생성특성을 연구하였다.

• Journal of Energy Engineering
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• v.18 no.1
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• pp.9-16
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• 2009

The experimental work has been carried out for the study of pyrolysis and char-air reaction of five coals used in Y power station in Korea. For five coals, the characteristics of pyrolyis and char reaction have been investigated with TGA, and their kinetic parameters were obtained and compared each other. The order of pyrolysis rate for five coals were as follows : Peabody, Flame, MIP, Indominco, Elk valley. The behavior of char - air reaction for five coal chars have been successfully described by the grain model. The rate of char-air reaction gave the maximum value for Flame coal char, on the while Elk valley coal char had the minimum value. For the reaction temperature over 1,000K, Flame coal char - air reaction was very fast compared with other coal chars.

• 한국신재생에너지학회:학술대회논문집
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• 2007.11a
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• pp.623-626
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• 2007

킬른형 열분해 반응기를 이용하여 혼합폐플라스틱의 열분해로부터 얻어진 고분자성분의 열적분해 특성에 관한 연구를 TGA와 GC-MS를 이용하여 수행하였다. 열적분해의 속도론적 연구는 $10{\sim}50^{\circ}C/min$ 사이의 여러 가열속도에서 비등온 질량감소 기술을 이용하여 수행하였으며 활성화 에너지 및 반응 차수와 같은 속도 상수들에 대한 정보를 얻기 위하여 문헌에 제시된 여러 가지의 속도론 해석방법을 이용하여 질량감소곡선 및 그 미분 값을 해석하였다. 또한 회분식 열분해 반응기를 이용하여 반응온도에 따른 액상 생성물의 수율변화를 고찰하였으며 GC-MS를 이용하여 액상 생성물의 반응온도 증가에 따른 특성연구를 수행하였다.

• Clean Technology
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• v.15 no.3
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• pp.186-193
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• 2009

The characteristics of product materials obtained from thermal degradation of low-qualify pyrolytic oil were investigated in this study. The reactants were produced by pyrolysis of mixed plastic waste with film type in a commercial rotary kiln reaction system. The properties of reactants were measured by elemental analysis, calorimetry analysis and SIMDIST analyst. The result of degradation experiments with different reaction temperature programs was discussed through product yields, cumulative yields and production rates of oil products. The multi-step reaction temperature program resulted in higher yields of product oils and lower yields of residues than one-step reaction temperature program. The product characteristics such as production yield and the rate of oil products etc. were influenced by reaction temperature program in the continuous thermal degradation.

• Applied Chemistry for Engineering
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• v.18 no.5
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• pp.511-515
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• 2007

The yield of oil was rapidly increased at $440^{\circ}C$ compared to $400^{\circ}C$ and $420^{\circ}C$ when the isothermal pyrolysis of waste ship lubricating oil was carried out in tubular type reactor, and pyrolysis was almost finished within 30 min. The yield of gas was decreased depending on the reaction temperature in which that of solid was not much changed. Pyrolysis experiments of waste ship lubricating oil were carried out with used ZSM-5 produced from a petrochemical process. The yield of gas was highly increased in the case of used ZSM-5 and fresh ZSM-5 compared to the case without catalyst. The produced oil and gas were almost constant for fresh ZSM-5 and used ZSM-5 at the same reaction temperature. In the reaction temperature $400{\sim}440^{\circ}C$, the selectivity of $C_5-C_{11}$ was two times higher with fresh ZSM-5 and used ZSM-5 than the case without catalyst.

• Journal of Energy Engineering
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• v.26 no.3
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• pp.97-104
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• 2017

In this study, waste tire rubbers were pyrolyzed in a lab-scale pyrolysis plant equipped with a fluidized bed reactor in a temperature ranges of $450-650^{\circ}C$. The main object of this work is to investigate the properties of pyrolysis oil with reaction temperatures and the behavior of sulfur in the products when waste polypropylene was added for co-pyrolysis. The maximum yield of oil was about 52wt.% at the reaction temperature of $456^{\circ}C$. From GC-MS analysis, the pyrolysis oils consisted mainly of limonene, toluene, xylene, styrene, trimethylbenzene, methylnaphthalenes and some heteroatom(sulfur and nitrogen)-containing compounds. The addition of waste polypropylene resulted in decrease in sulfur contents of the pyrolysis oils.

• Journal of the Korea Organic Resources Recycling Association
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• v.10 no.4
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• pp.65-74
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• 2002

This Study was investigated operating condition of pyrolysis processing for sludge disposal in sewage treatment plant. Important parameters studied include running time of pyrolysis, run time of dry and pyrolysis processing, water content of sewage sludge, solids amount of sewage sludge(TS%), condition of pyrolysis temperature. Most degradation reaction of sewage sludge are first order, it assumed first order and elucidated the kinetics. This was the basis of characteristics analysis of sludge degradation mechanism. Also, with the increasing of temperature, how the yield of oil and char product change was observed, and the distribution of gas product components was observed. Main components of gas and carbon product are a little difference with pyrolysis temperature, but it consist of $CH_4$, $C_2H_4$, $C_3H_8$, $C_4H_{10}$, toluene, $C_6H_6$, $SO_2$, CO etc. The gas of $C_1-C_4$ yield increased along with degradation temperature of $670^{\circ}C$ and oil yield decreased of $C_6H_6$ and $C_6H_5OH$ with temperature of $600^{\circ}C$. Particularly, low value added char yield 134kg/t at $670^{\circ}C$, but increased to 194kg/t at pyrolysis temperature of $600^{\circ}C$. In the result of elementary analysis on it, it is mainly composed of carbon. From this fact, in pyrolysis of sludge, it comfirmed that carbonization reaction occur at high temperature well.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.6
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• pp.1063-1072
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• 2000

Kinetic tests on pyrolysis of the mixture of waste automobile lubricating oil and polystyrene were carried out with thermogravimetric technique at the heating rates of 0.5, 1.0, $2.0^{\circ}C/min$ in a stirred batch reactor. The activation energy and the reaction order were determined at conversions of 1 to 100% using differential method. The mixture of waste automobile lubricating oil and polystyrene was pyrolyzed at lower temperature rather than waste automobile lubricating oil and polystyrene. respectively. Also, the thermal decomposition took place in two broad reaction steps. The pyrolyzed oil of mixture represented high selectivity of styrene monomer and dimer like that of polystyrene pyrolyzed products.