• 한국신재생에너지학회:학술대회논문집
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• 2011.11a
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• pp.76.2-76.2
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• 2011

석탄의 탄종별 열분해 생성물은 석탄가스화기의 뮬레이션 기법의 첫 번째 단계이며 이러한 탄종별 생성물 예측은 가스화기의 성능, 즉 가스화기 출구 가스조성, 탄소전환율, 냉가스 전환율등을 예측하는데 있어 가장 기본적이고 중요한 절차이다. 본 논문에서는 석탄가스화기내 열분해 과정을 모사할 수 있도록 석탄 성상과 가스화기 운전압력에 따라 탄종별 고온고압 열분해시의 생성물을 정량적으로 계산하는 방법을 제시하였다. Merrick(1983)의 방법을 기반으로 석탄의 성상(공업/원소분석치), 가스화기 운전압력과 몇가지 상관관계식으로부터 고온고압하 열분해 생성물을 계산하는 방법이며 이를 프로그램화하여 가스화기 시뮬레이터용 모듈로 구성할 수 있도록 하였다. 또한, 국내 수입 5개 탄종에 대하여 열분해 생성물의 조성을 구하였으며 이를 상용 열분해모델의 결과와 서로 비교하였다. 열분해 생성물 조성의 분포는 다른 상용 프로그램 결과와 부합하였으며 생성물의 발열량도 원탄의 발열량과 적합한 결과를 보여주었다.

• Clean Technology
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• v.19 no.3
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• pp.233-242
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• 2013

The influences of Ca and Fe based oxides as dechlorination sorbents on the product distribution, boiling point distribution of liquid product, concentration of Cl of the products from the pyrolysis of PVC containing combustible wastes were investigated. With Fe based oxides as the sorbents, the yield of liquid product remarkably decreased whereas the decrease of the boiling point distribution of the liquid product was not noticeable. This phenomenon indicated that Fe based oxides worked as catalysts with weak catalytic activity. With Ca based oxides as the sorbents, the yield of liquid product did not decrease and the boiling point distribution of liquid product did not change significantly, but the dechlorination performance of these was much better than that with Fe based oxides.

• Journal of Energy Engineering
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• v.11 no.3
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• pp.269-275
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• 2002

Experimental studies are carried out to find the behavior of sulfur compounds which are evolved during high temperature pyrolysis of coals at the smelting reduction process for iron ore. Three kinds of bituminous coals, such as Hunter & Mt. Thorley (Australia), and Ensham (South Africa) are used. And forms of sulfur compound and their amounts are analyzed at the temperature ranges of 800~110$0^{\circ}C$. Then H$_2$S is the major gas, but CS$_2$ and COS are minor gases. Sulfur compounds in three coals are distributed into the volatiles (gas & tar) and coal char as the ratio of approximately 50%：50%, respectively.

• Proceedings of the Korea Committee for Ocean Resources and Engineering Conference
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• 2000.10a
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• pp.96-100
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• 2000

Recently ocean environmental pollution becomes very serious, so each governmental organization slove this problem. As part of the policy, KRISO has investigated distribution condition at ocean waste. Acc\ulcorner we found that combustble waste consists of ropes, fishing nets, and tires. These are, however, highly polyme\ulcorner existing incicerators have many problems to treat these. In this study we want to pyrolyze highly polymerized \ulcorner data for a design of fule production system without second pollution. Through the thermogravimetic experiment characteristics of pyrolysis and obtained some preliminary results.

• Clean Technology
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• v.10 no.4
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• pp.203-213
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• 2004

Natural gas thermal decomposition method is the technology of converting natural gas (methane) into hydrogen and carbon at high temperature. The most advantage of thermal decomposition method is that hydrogen and carbon can be produced without emitting carbon dioxide. In this study, the generation of hydrogen and carbon was investigated by this natural gas (methane) thermal decomposition method. We found that pyrocarbon was created on the surface of reactor, carbon black was deposited on the pyrocarbon and final plugging phenomenon took place. To solve this problem, we tried several attempts such as introduction of double pipe reactor instead of single pipe reactor or oxidization of carbon black using $O_2$ or $CO_2$ at regular intervals of reaction. Therefore, some plugging phenomenon was resolved by this methods. Also, carbon particle size was measured by SEM (Scanning Electron Microscope) image and the size was about 200 nm.

• Proceedings of the Korean Institute of Resources Recycling Conference
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• 2000.04a
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• pp.19-144
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• 2000

막대한 에너지원을 갖고 있는 고분자 폐기물은 열분해에 의하여 오일화가 가능하며 이 오일은 대체 연료유로서 사용이 가능하다. 그러나 이 연료유를 생산하기 위해서는 폐플라스틱 및 폐타이어의 경우는 공정을 서로 달리하여야 이용이 가능하며 생성유의 유질에서도 다소 차이가 있다. 올레핀계가 함유된 폐플라스틱을 열분해 오일화 하기 위해서는 분해 촉매를 사용하여야 하며 열분해유는 경유분과 d사한 성상을 갖고 있으며 폐타이어의 열분해유는 유황성분 및 BTX 분을 상당량 함유하고 있어서 경유분과는 다소 다른 성상을 갖고 있다. 또한 폐타이어 및 폐플라스틱의 열분해 기술이 사용화되기 위해서는 열분해시 발생하는 Coking 문제 극복 및 시스템에 대한 설계기술이 뒷받침되어야 한다.

• Tribology and Lubricants
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• v.4 no.1
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• pp.36-42
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• 1988

On the basis of the thermally-activated Wear theory, it is well estabilished that the secondary activated energy, which is mainly resulted from the exothermic reaction of hydrogen from thermal decomposition of the hydrocarbons at the high temperature and the high speed, caused catastropic failure. The new additive, viz., DEP was synthesized to reduce or eliminate the hydrogen effect at the contact junction. Through the thermal degrading and the thermodynamic consideration, the synthesized additive, viz., DEP showed the possibiliy as the hydrogen scavenger.

• Proceedings of the Korean Society For Composite Materials Conference
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• 2003.04a
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• pp.173-175
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• 2003

At the low temperature of $950^{\circ}C$ the $\mu\textrm{m}$-sized whisker growth during the catalytic CVD of pyrolytic carbon from methane with $H_2$- and Ar-gas on quartz substrate with NiO powder was found in this work. In the preliminary study it was observed from pure methane pyrolysis without catalyst at the high temperature $1500~1700^{\circ}C$. If the growth whisker should be stopped at initial stage, about 20 min. of the methane pyrolysis, it would be nanosized whisker growth. The screw growth mechanism and unique mechanical properties of whisker for composites were also recognized. If the pyrolysis would be continued, we could found also spiral growth of whistlers with diameter of about 1, 5 mm. The large length of whisker was about 10 cm in 20 minute.

• Journal of the Korean Applied Science and Technology
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• v.23 no.4
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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.

• 한국생물공학회:학술대회논문집
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• 2000.11a
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• pp.733-736
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• 2000

Lignin is usable as fuels and heavy oil additives if depolymerized to monomer unit, because the chemical structures are similar to high octane materials found in gasoline. In this study, the solvent-phase thermal cracking(solvolysis) of lignin was performed at the various temperature and time in a laboratory tubular reactor. Conversion yield was measured for the properties of thermal cracking and liquefaction reaction of lignin. Highest conversion yield when acetone was used as thermal cracking solvent was 55.5% at $350^{\circ}C$, 50minutes and highest tar generation were $260{\sim}350mg/g\;{\cdot}\;lignin$ at $250^{\circ}C$, and highest conversion yield after tar removal was 76.88% at $300^{\circ}C$, 30minutes. Conversion yield, product compositions and amounts were determined by tar degradation yield.