• Journal of Environmental Health Sciences
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• v.26 no.4
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• pp.38-44
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• 2000

Compared to other waste, waste tire has much discharge quantity and calorie. When we use waste heat from waste tire, it can be definitely better substitute energy than coal and anthracite in high oil price age. To use as a basic data for providing low cost and highly effective heating system, following conclusion was founded. Annual waste tire production was 19,596 million in 1999, Recycling ratio was almost 55% and more than 8.78 million was stored. Waste tire has lower than 1.5% sulfur contain ratio which is resource of an pollution, So it is a waste fuel which can be combustion based on current exhaust standard value without any extra SOx exclusion materials. Waste tire has 9,256Kcal/kg calorific value and it is higher than waste rubber, waste rubber, waste energy as same as B-C oil. When primary and second air quantity was 1.6, 8.0 Nm$^3$/min, dry gas production time was 270min and total combustion time was 360 min. In the SOx, NOx, HC of air pollution material density were lower than exhaust standard value at the back of cyclone and dusty than exhaust standard value without dust collector.

• Transactions of the Korean Society of Mechanical Engineers
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• v.18 no.7
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• pp.1833-1839
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• 1994

Experiments have been carried out to investigate the burning characteristics of waste tires in high temperature environments. The burning of waste tire chips consists of four stages ; evaporation of volatile matters, ignition, burning of volatile matters, and burning of solid carbon. Burning time of waste tire chips depends on the gas temperature and the initial weight of the chip. However, the environments. In the ceramic matrix burner with a ceramic radiation shield, the burning time of the waste tire chips becomes shorter than that without the shield. This is due to the increase in heat transfer to the tire chips by radiation.

• Journal of Biosystems Engineering
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• v.25 no.6
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• pp.481-488
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• 2000

This study was initiated in order to find alternative fuel substituting for light oil the most common fuel for heating greenhouse. The tire oil used in this research was produced by pyrolysis process, one of the final products besides steel string and carbon black in which waste tires as a form of chopped pieces broken by shredding machine are heated up to 200~30$0^{\circ}C$ with maximum restraining of oxygen supply. In order to justify light oil equivalent qualities in tire oil combustion characteristics were defined in the way of comparing kinetic viscosities in the wide range of temperature flame sizes and exhaust gas components in the various combustion conditions. We found that kinetic viscosity of tire oil was lower than light oil by 1 to 2 cSt in the temperature range showing better flowing mobility in the fuel line of the burner and no significant difference in flame size between the two oils in the all combustion treatments. However much more NO and SO$_2$ were detected from the exhaust gases of tire oil than light oil combustions. In fact tire oil contains more nitrogen and total sulfur, by 25 times and 40 times respectively than light oil according to the composition analysis. Tolerable limit for SO$_2$discharge amount defined by the national air pollution standards is under 540ppm so tire oil combustion satisfies the requirement though. It is desirable if sulfur and nitrogen filtering process shall be added in the tire oil production line. Except the exhaust gas components all greenhouse heating qualities of tire oil including hot air temperature are very identical to those of light oil.

• Clean Technology
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• v.5 no.1
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• pp.42-48
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• 1999

Waste tires have both sides which are contamination and reuse concern with environmental problems. In this study, tire pyrolysis was conducted to convert combustible gases using thermal plasma. Production of combustible gases was found by gas chromatography after thermal plasma pyrolysis of waste tires without oxygen. The combustible gases consist of low molecular hydrocarbons such as $CH_4$, $C_2H_2$, $C_4H_{10}$ etc. As tire feed rate increased, the composition of $CH_4$ in the gases was increased. As plasma power increased, the composition of $C_2H_2$ was increased. $C_2H_2$ and $C_4H_{10}$ were dominant and had the ratio over 70% in the gases. On the other hand the trends of pyrolysis was characterized in the thermal plasma from the results of TG analysis which shows the currents of decomposition of the char according to the temperature.

• Journal of environmental and Sanitary engineering
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• v.15 no.4
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• pp.98-104
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• 2000

Commercial rubber(IR, NR, BR), SBR, and tire were degraded by thermal degradation process. The oil yield of rubbers and tire ranges about 37~86%, it was increased with increase of operation temperature in pyrolysis. And the yield of pyrolytic oil was increased with increase of heating rate. The maximum oil yields of IR, NR, BR, SBR, and tire were 80, 73, 83, 86 and 55% each at $700^{\circ}C$ with a heating rate of $20^{\circ}C$/min, respectively. The pyrolytic oil components were consisted of about 50 aromatic compounds. The calorific value of purolytic oil of commercial rubber, SBR, and tire was measured by calorimeter, it was 39~40 kJ/g. The BET surface area of pyroblack was $47~63m^2/g$. The optimum condition of pyrolysis was operating temperature of $700^{\circ}C$ with heating rate of $20^{\circ}C$. Therefore, the pyrolytic oil and pyroblack are possible to alternative fuel and carbon black.

• 한국신재생에너지학회:학술대회논문집
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• 2008.10a
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• pp.157-160
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• 2008

본 연구에서는 디스크 이동식 폐타이어 열분해 실증 설비(10톤/일)를 설계, 제작 그리고 시운전을 통하여 열분해 설비의 안정적인 연속 운전이 가능함을 확인하였다. 시운전 결과 반응기 내부 온도는 $500{\sim}600^{\circ}C$, 내부 압력은 $-80{\sim}-100mmHg$, 체류시간은 $60{\sim}90min$ 범위에서 안정적인 열분해가 일어났다. 또한 이번 과제 수행을 통해NC 가스의 연소기를 개발 적용하여 NC 가스의 열분해 열원으로 사용 가능성을 확인하였으며, NC 가스 연소 시 대기 측정을 통하여 규제치도 만족함을 확인할 수 있었다. 지금까지 나온 결과는 장기 연속 운전과 scale-up을 위한 기초 자료가 될 것이다.

• Proceedings of the Korean Institute of Resources Recycling Conference
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• 1993.03a
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• pp.13.1-13
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• 1993

• Proceedings of the Korean Society for Agricultural Machinery Conference
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• 2000.07a
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• pp.124-129
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• 2000

• 한국신재생에너지학회:학술대회논문집
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• 2008.05a
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• pp.471-474
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• 2008

The pyrolytic behavior of waste tire under microwave heating was investigated. Experiments were conducted using a lab- and bench-scale system to delineate the effects of microwave output power on the response. As the results of experiments, it was found that as the microwave output power was increased between 0.84 and 3.04 kW/kg, the oil yield and required time rapidly increased and decreased, respectively. With further increase of the microwave output power, the oil yield and required time did not change significantly.

• Resources Recycling
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• v.22 no.2
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• pp.11-17
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• 2013

The recycling technology of carbon residue produced from the process of oil recovery in waste tire pyrolysis is significant in environmental and economical aspects. This study was done to figure out the recycling possibility of carbon residue to activated carbon. For this, the characteristics of the carbon residue obtained from the commercial pyrolysis process of waste tire were studied. Also, the variation of pore structure of carbon residue was studied after 1 hour of carbonization at $600^{\circ}C$ and $800^{\circ}C$ and 3 hours of activation at $950^{\circ}C$. The specific surface area of the carbon residue was $8.0m^2/g$ and it increased to $548.3m^2/g$ after carbonization and activation.