Abstract
Characteristics of pyrolytic gasification were examined for the waste tire and 7 types of waste synthetic resin, using a bench scale experimental facility. the product gas temperature of waste tires was $150~300^{\circ}C$ and the temperature profile in the combustion zone of the lower reactor part tended to be clearly distinguished from that in the gasification zone of the upper part. However, in the case of waste synthetic resins, there were no clear distinction and temperature fluctuation was severe, depending on the reaction time. Product gas quantity, which depends on that of supplied (1st) air, was found to be 105~135% of the 1st air amount at the steady state. The concentration of noncombustible components in product gas was 80~90 vol.% and the high heating value of the product gas calculated from gas compositions was 1,500~3,000 kcal/N㎥ for waste tire, and 300~2,900 kcal/N㎥ for waste synthetic resins, respectively. Heating value of product gas and combustible gas concentration were increased in proportion to 1st air amount when 1st air amount is below $0.35N\textrm{m}^3$/min.
본 연구에서는 150kg/batch(승용차용 타이어 기준) 규모의 건류가스화 장치를 이용하여 페타이어와 7종류의 폐합성수지에 대한 건류가스화 실험을 폐기물 종류별 건류가스화 특성을 파악하고, 건류시간 및 1차 공기량에 따른 건류가스의 발생량과 성분 조성 등의 변화 경향등을 분석하였다. 페타이어의 경우 반응기 내부에서 연소영역과 가스화 영역의 뚜렷한 구별이 확인되었고, 건류용 1차 공기량에 대해 1.05~1.35 배의 비율로 발생되는 생성가스는 비가연성성분 이외에 CO, $H_2$, $C_1$~$C_7$ 범위의 탄화수소로 구성되었으며, 정상상태에서는 1.500~300 kcal/N$\textrm{m}^3$. 종말처리 단계에서는 250~500kcal/N$\textrm{m}^3$의 발영량을 각각 나타냈다. 페합성 수지류는 생성가스의 온도변화가 심하고, $N_2$, $CO_2$, $O_2$의 구성비율이 85%이상인 건류생성가스는 원료폐기물이 가진 열량의 10~35%에 해당하는 300~2,900kcal/N$\textrm{m}^3$ kcal/Nm의 발열량을 보유하였다.
