• 한국응용과학기술학회지
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• 제19권3호
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• pp.198-205
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• 2002

Isothermal pyrolysis of high density polyethylene(HDPE), polypropylene(PP) and polystyrene(PS) was performed at $450^{\circ}C$, respectively. The effect of pyrolysis time on yield and product composition was investigated. Conversion and liquid yield obtained during HDPE pyrolysis continuously increased with time up to 80minutes, but those of PP and PS did not largely change after 35minutes. Each liquid product formed during the pyrolysis was classified into gasoline, kerosene, light oil and wax according to the distillation temperature based on the petroleum product quality standard of Korea Petroleum Quality Inspection Institute. The major liquid product of HDPE pyrolysis was light oiH34 wt.% based on the amount of HDPE treated) and the amounts of the other liquid ingredients(gasoline, kerosene and wax) were almost the same. On the other hand, the pyrolysis of PP produced 27 wt.% gasoline, 22 wt.% kerosene, 24 wt.% light oil and 13wt.% wax, and the pyrolysis of PS produced 56 wt.% gasoline, 12 wt.% kerosene, 9 wt.% light oil and 13 wt.% wax.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2009년도 추계학술대회 논문집
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• pp.321-324
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• 2009

Upgrading of pyrolysis wax oil has been conducted in a continuous fixed bed reactor at $450^{\circ}C$, 1hour, LHSV 3.5/h. The catalytic degradation using HZSM-5 catalyst are compared with the thermal degradation and also was studied with a function of experimental variables. The raw pyrolysis wax oil shows relatively high boiling point distribution ranging from around $300^{\circ}C$ to $550^{\circ}C$, which has considerably higher boiling point distribution than that of commercial diesel. The product characteristic from thermal degradation shows a similar trend with that of raw pyrolysis wax oil. This means the thermal degradation of pyrolysis wax oil at high degradation temperature is not sufficiently occurred. On the other hand, the catalytic degradation using HZSM-5 catalyst relative to the thermal degradation shows the high conversion of pyrolysis wax oil to light hydrocarbons. This liquid product shows high gasoline range fraction as around 90% fraction and considerably high aromatic fraction in liquid product. Also, in the catalytic degradation the experimental variable such as catalyst amount and reaction temperature was studied.

• Environmental Analysis Health and Toxicology
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• 제19권2호
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• pp.201-206
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• 2004

Recently, waste plastic recycling technology is transforming from Incineration system to pyrolysis gasification system which can derive the resources from environmental waste and charge no more environmental burden to nature. The present study was carried out to investigate the potential acute toxicity of derived product of pyrolysis gasifications system for recycling of waste plastic by a single oral dose in Sprague-Dawley Rats. In order to evaluate the hepatotoxic effects of derived product of pyrolysis gasification system, activities of serum transaminase were measured in rats. No related changes in survivals, clinical signs and the ratio of the liver to body weights of rats were monitored. The results showed that the single oral administration of material of pyrolysis system for recycling of waste plastic did not induce any toxic effect at orally single dose level of 0 and 100, 200, 400, 800mg/kg body weight in rats. We could not find out any significant tocxicity induced by single oral administrate of material of pyrolysis system for recycling of waste plastic.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2005년도 춘계학술대회
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• pp.553-556
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• 2005

Pyrolysis of polyethylene was carried out in the stainless steel reactor of internal volume of $40cm^3$. Pyrolysis reactions were performed at temperature $390-450^{\circ}C$ and the pyrolysis product were collected separately as reaction products and gas products. The molecular weight distributions(MWDs) of each liquid product were determined by GC-SIMDIS. Molecular weight of each product were decreased wi th increase of react ion temperature and time.

• 한국응용과학기술학회지
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• 제23권4호
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• pp.307-318
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• 2006

The pyrolysis of high density polyethylene(HDPE) and low density polyethylene(LDPE) was carried out at temperature between 425 and $500^{\circ}C$ from 35 to 80 minutes. The liquid products formed during pyrolysis were classified into gasoline, kerosene, gas oil and wax according to the petroleum product quality standard of Korea Petroleum Quality Inspection Institute. The conversion and yield of liquid products for HDPE pyrolysis increased continuously according to pyrolysis temperature and pyrolysis time. The influence of pyrolysis temperature was more severe than pyrolysis time for the conversion of HDPE. For example, the liquid products of HDPE pyrolysis at $450^{\circ}C$ for 65 minutes were ca. 30wt.% gas oil, 15wt.% wax, 14wt.% kerosene and 11wt.% gasoline. The increase of pyrolysis temperature up to $500^{\circ}C$ showed the increase of wax product and the decrease of kerosene. The conversion and yield of liquid products for LDPE pyrolysis continuously increased according to pyrolysis temperature and pyrolysis time, similar to HDPE pyrolysis. The liquid products of LDPE pyrolysis at $450^{\circ}C$ for 65 minutes were ca. 27wt.% gas oil, 18wt.% wax, 16wt.% kerosene and 13wt.% gasoline.

• 신재생에너지
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• 제5권4호
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• pp.52-58
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• 2009

Upgrading of pyrolysis wax oil using HZSM-5 catalyst has been conducted in a continuous fixed bed reactor at $450^{\circ}C$, 1hour, LHSV 3.5/h. The catalytic degradation was studied with a function of catalyst amount and reaction temperature. The raw pyrolysis wax oil shows relatively high boiling point distribution ranging from around $300^{\circ}C$ to $550^{\circ}C$, which has considerably higher boiling point distribution than that of commercial diesel. The catalytic degradation using HZSM-5 catalyst shows the high conversion of pyrolysis wax oil to light hydrocarbons. The liquid product obtained shows high gasoline range fraction as around 90% fraction and considerably high aromatic fraction in liquid product. Here, the experimental variable such as catalyst amount and reaction temperature was influenced on the product distribution.

• 한국응용과학기술학회지
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• 제19권4호
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• pp.258-264
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• 2002

Pyrolysis of polypropylene(PP) Was performed to find the effects of the pyrolysis temperature(425, 450, 475 and $500^{\circ}C$) and the pyrolysis time(35, 50 and 65minutes), respectively. Conversion and liquid yield obtained during PP pyrolysis continuously increased with the pyrolysis temperature( up to $500^{\circ}C$) and the pyrolysis time(up to 65minutes), especially these were more sensitive to the pyrolysis time at $425^{\circ}C$ than other pyrolysis temperatures. Each liquid product formed during the pyrolysis was classified into gasoline, kerosene, light oil and wax according to the distillation temperature based on the petroleum product quality standard of Korea Petroleum Quality Inspection Institute. The liquid products of PP pyrolysis up to $450^{\circ}C$ were almost same fractions($26{\pm}3$wt.% gasoline, $20{\pm}2$wt.% kerosene and $23{\pm}2$wt.% light oil) except wax($3{\sim}13$wt.%). On the other hand, the pyrolysis of PP from $475^{\circ}C$ to $500^{\circ}C$ produced $26{\pm}3$wt.% wax, $24{\pm}1$wt.% gasoline, $18{\pm}1$wt.% kerosene and $16{\pm}1$wt.% light oil. After all, the main liquid product changed from gasoline to wax with increasing pyrolysis temperature.

• 에너지공학
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• 제2권2호
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• pp.208-214
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• 1993

직접 연소시 다량의 공해물질이 배출되는 유연탄을 가공하여 산업용 및 도시가스로 활용이 가능한 고열량 가스(발열량 : 7000 kca1/N㎥)를 생산하기 위한 유연탄 가공 기술개발 연구의 일환으로 고정층 유연탄 이단 열분해 실험을 수행하였다. 본 연구에서는 코우크스 촉매를 사용하여 열분해온도를 468, 516, 5$65^{\circ}C$, 촉매분해온도를 700, 750, 800, 85$0^{\circ}C$로 변화시키면서 이단열분해 조건이 생성물의 특성에 미치는 영향을 조사하였다. 동진탄에 대하여 코우크스 촉매를 사용하여 이단 열분해 실험을 수행한 결과 촉매에 퇴적되는 탄소량은 생성 tar의 5% 이하였으며, 전체 석탄에너지중 15% 정도가 고열량 가스로 회수되는 것을 확인하였다. Tar 중에 포함된 oil성분의 양은 이단 열분해의 경우가 저온 열분해에서 보다 많이 생성되었으며, 열분해온도가 5$65^{\circ}C$ 인 경우 생성된 tar는 516$^{\circ}C$에서 생성된 tar보다 이단 열분해의 경우 촉매 분해가 잘 되지 않았다. 생성가스의 분석 견과는 촉매분해온도가 80$0^{\circ}C$ 이상이면 에틸렌의 분해속도가 급격히 증가하므로 80$0^{\circ}C$ 이하로 유지하는 것이 적절함을 보여준다.

• 폴리머
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• 제27권1호
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• pp.84-89
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• 2003

열분해 온도 및 열분해 시간이 HDPE의 열분해에 미치는 영향을 해석하였다. HDPE 열분해의 시작온도와 활성화에너지는 가열속도가 증가함에 따라 증가하였다. 전환율과 액체수율은 열분해 온도와 시간이 증가함에 따라 계속 증가하였고, 특히 45$0^{\circ}C$에서 열분해 시간에 매우 민감하게 변하였다. 전환율에 있어 열분해 온도가 열분해 시간보다 더 큰 영향을 주었다. 열분해 과정에서 생성된 각각의 액체성분을 한국석유품질검사소 석유제품 품질기준에 기초하여 증류온도에 따라 가솔린, 등유, 경유, 왁스로 분류하여 본 결과, 450 $^{\circ}C$에서는 경유 > 왁스 > 등유 > 가솔린 순이었고, 475$^{\circ}C$와 50$0^{\circ}C$에서는 왁스 > 경유 > 등유 > 가솔린 순이었다.

• 한국수소및신에너지학회논문집
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• 제21권5호
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• pp.442-451
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• 2010

This paper describes the calculation method to obtain the product composition of coal pyrolysis at high pressure and high temperature. The products of coal pyrolysis should be determined for the coal gasifier simulation, and this is the first step of the coal gasifier simulation. The pyrolysis product distribution greatly affects the coal gasifier efficiency such as carbon conversion, cold gas efficiency and the syngas composition at the outlet of the gasifier. The present calculation method is based on the coal ultimate/proximate analysis and several correlations among gasifier pressure, coal properties and pyrolysis products. The calculated products for 5 coals have been compared with those from the commercial pyrolysis model.