• 신재생에너지
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• 제2권2호
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• pp.118-125
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• 2006

The target of this work was the process development of demonstration plant to produce the high quality alternative fuel oil by the pyrolysis of mixed plastic waste. In the first step of research, the bench-scale units of 70 t/y and the pilot plant of 360 t/y had been developed. Main research contents in this step were the process performance test of pilot plant of 360 ton/year and the development of demonstration plant of 3,000 t/y, which was constructed at Korea R & D Company in Kimjae City. The process performance of pilot plant of 360 t/y showed about 80% yield of liquid product, which was obtained by both light gas oil(LGO) and heavy gas oil(HGO), The boiling point range distribution of LO product that was mainly consisting of olefin components in PONA group appeared at between that of commercial gasoline and kerosene. On the other hand, HO product was mainly paraffin and olefin components and also appeared at upper temperature distribution range than commercial diesel. Gas product showed a high fraction of $C_3\;and\;C_4$ product like LPG composition, but also a high fraction of $CO_2$ and CO by probably a little leak of process.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2006년도 춘계학술대회
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• pp.523-526
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• 2006

The target of this work was the process development of demonstration plant to produce the high quailty alternative fuel oil by the pyrolysis of mixed plastic waste. In the first step of research, the bench-scale units of 70t/y and the pi lot plant of 360 t/v had been developed. Main research contents in this step were the process performance test of pilot plant ot 360ton/year and the development of demonstration plant of 3 000 t/y which was constructed at Korea R & D Company in Kimjae City. The process performance of pilot plant of 360 t/v showed components in PONA group appeared at between that of commercial gasoline and kerosene. On the other hand, HO product was mainly paraffin and olefin components and also appeared at upper temperature distribution range than commercial diesel. Gas product showed a high fraction of $C_3\;and\;C_4$ product like LPG composition, but also a high fraction of $CO_2$ and CO by probably a little leak of process.

• Korean Chemical Engineering Research
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• 제49권4호
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• pp.417-422
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• 2011

ABS 수지의 반응온도 및 반응시간에 따른 저온 열분해를 연구하기 위하여 ABS 수지의 저온열분해를 회분식 반응기를 이용하여 상압하에서 $425{\sim}500^{\circ}C$ 영역에서 수행하였다. 열분해 시간은 20~80분까지 하였고 열분해로 생성된 성분은 지식경제부에서 고시한 증류성상온도에 따라 가스, 가솔린, 등유, 경유, 중유로 분류하였다. ABS 수지의 열분해에서 80% 이상의 전환율을 얻기 위해서는 반응온도 $500^{\circ}C$ 이상에서 반응시간 60분 이상을 유지하여야 한다. 최종적으로 생성된 분해유는 가스 중유 > 가솔린 > 경유 > 등유 순으로 나타났으며, 온도와 반응시간이 증가함에 따라 중유 및 경유 성분이 늘어났다.

• 한국응용과학기술학회지
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• 제25권4호
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• pp.495-502
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• 2008

To investigate the synergy effect on the pyrolysis of mixture of polyethylene(PE) and polystyrene(PS), the pyrolysis of PE, PS and the mixture of PE-PS was carried out in a batch reactor at the atmospheric pressure and $450^{\circ}C$. The pyrolysis time was from 20 to 80 mins. The liquid products formed during pyrolysis were classified into gas, gasoline, kerosene, gas oil and heavy oil according to the distillation temperatures based on the petroleum product quality standard of Korea Institute of Petroleum Quality. The analysis of the product oils by GC/MS showed that the new components produced by mixing were not detected. The synergy effect according to mixing of PE and PS did not also appear. The conversion and yield of mixtures were in proportion to the mixing ratio of sample.

• 폴리머
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• 제29권1호
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• pp.64-68
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• 2005

폐플라스틱으로 수거되는 내충격 폴리스티렌의 액상연료로서의 재활용을 위해 열분해에 의한 HIPS 해중합 특성을 연구하였다. 열분해 온도 및 열분해 시간이 HIPS의 열분해에 미치는 영향을 조사하였다. HIPS의 열분해 반응 시작온도와 활성화에너지는 가열속도가 증가함에 따라 증가하였다. 전환율과 액체수율은 열분해 온도와 시간이 증가함에 따라 점진적으로 증가하였다. 열분해 과정에서 생성된 각각의 액체성분을 한국석유품질검사소 석유제품 품질기준에 기초하여 증류온도에 따라 가솔린, 등유, 경유, 중유로 분류하여 본 결과, 가솔린 > 중유 > 등유 > 경유 순이었다. 특히 가솔린 성분은 열분해된 HIPS의 51${\pm}$6 wt%를 차지하였다.

• 청정기술
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• 제15권2호
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• pp.109-115
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• 2009

폴리에틸렌-폴리프로필렌 혼합물의 열분해에 대한 시너지효과를 조사하기 위하여 폴리에틸렌(PE)과 폴리프로필렌(PP) 및 PE-PP혼합물의 저온열분해를 회분식 반응기를 이용하여 상압 및 $450^{\circ}C$에서 실행하였다. 열분해 시간은 20${\sim}$80분이었으며, 열분해로 생성된 성분은 한국석유품질검사소에서 고시한 증류성상온도에 따라 가스, 가솔린, 등유, 경유, 중유로 분류하였다. GC/MS에 의한 생성오일의 성분분석 결과 PE-PP 혼합에 의해서 새로운 성분이 검출되지 않았고 혼합에 따른 시너지효과 또한 나타나지 않았다. PE-PP 혼합물의 전환율과 각 생성물의 수율은 시료의 혼합비율에 비례하였다.

• 청정기술
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• 제16권1호
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• pp.26-32
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• 2010

폴리프로필렌-폴리스타이렌 혼합물의 열분해에 대한 시너지효과를 조사하기 위하여 폴리프로필렌(PP)과 폴리스타이렌(PS) 및 PP-PS혼합물의 저온열분해를 회분식 반응기를 이용하여 상압 및 $450^{\circ}C$에서 실행하였다. 열분해 시간은 20~80분까지 하였고 열분해로 생성된 성분은 지식경제부에서 고시한 증류성상온도에 따라 가스, 가솔린, 등유, 경유, 중유로 분류하였다. GC/MS(Gas chromatography/Mass spectrometry)에 의한 생성오일의 성분 분석은 PP-PS 혼합에 의해서 새로운 성분이 검출되지 않았음을 보여주었다. PP-PS 혼합물의 열분해 생성물의 분석결과, 혼합에 따른 시너지효과 또한 나타나지 않았다. PP-PS 혼합물의 중유수율을 제외한 각 생성물의 수율은 시료의 혼합비율에 비례하였다. 중유수율은 혼합비에 관계없이 거의 일정하게 나타났다.

• 한국수소및신에너지학회논문집
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• 제19권1호
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• pp.56-63
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• 2008

In this study, thermochemical degradation of hemicellulose by Acetone-Solvolysis, the effects of reaction temperature, conversion yield, degradation properties and degradation products were investigated. Experiments were performed in a tube reactor by varying reaction temperature from $200{\circ}C$ to $400{\circ}C$ at 40 min of reaction time. The liquid products from pyrolysis-liquefaction of hemicellulose contained various kinds of ketones. ketones, as 4-methyl-3-penten-2-one, 3-methylene-2-pentanone, 22,6-dimethyl-2, 5-heptadien-4-one, 4-methyl-2-pentanone, 5-methyl-2-hexanone, 3,5,5-trimethyl-2-cyclohexen-1-one, and bezenes. as 1,4-dimethylbenzene, 1-methyl-2-(1-methylethyl)-benzene, 1,4-dimethyl-2-(2-methylpropyl)benzene, 4-secbutyl-ethyl benzene, could be used as high-octane-value fuels and fuel additives. Combustion heating value of liquid products from thermochemical conversion processes of hemicellulose was in the range of $6,680{\sim}7,170cal/g$. After 40min of reaction at $400{\circ}C$ in Acetone-Solvolysis of hemicellulose, the energy yield and mass yield was as high as 72.2% and 41.2g oil/100g raw material, respectively.