This study was investigated to the energy recovery by the pyrolysis of waste tyre. the pyrolysis of the waste tyre was rnade by using the pyrolysis charnber for the gasification and the cornbustion charnber for the cornbustion of the pyrolysis gas. 1n batch systern. the arnount of waste tyre was put 150kg in the pyrolysis charnber and the proper air flow rate for the stable production of the pyrolysis gas was O.95N m3 / rnin. the production tirne of the pyrolysis gas was stable above 21Orninutes. andthe stable production rate was above 3.8N m3/ rnin. The production ternperature of pyrolysis gas was 170 C élnd cornbustion ternperature of pyrolysis gas was l.OOO C ‘ The cornbust ible component of washin gas in pyrolysis gas of waste tyre was CO‘ CH4 • C2H6 and C3H8 • and total arnount was 22.7%. Heat value of condensed rnaterial was 9.804Kcal/ kg. The average concentration of air pollutants between cyclone and scrubber was CO 420.4pprn. 50x 349.8pprn. NOx 68.5pprn. HCl 24.4pprn and Du~.t 240.0g / N m . respectively
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