Method for treating combustible waste
A treatment method and waste technology, applied in the field of combustible waste treatment, can solve the problems of limited use of activated carbon, inability to treat with water, heavy metal smelting, etc.
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Embodiment 1
[0059] Used paper (moisture content 15%, ash content 5%, and combustible content 80%) was used as combustible waste. use this old paper figure 1 The electric tube furnace retort shown. exist figure 1 Among them, 1 is a quartz glass tube, 2 is an electric heater, 3 is a thermocouple, 4 is nitrogen, 5 is exhaust gas from dry distillation, 6 is combustible waste, and 7 is a temperature controller. Put the combustible waste (old paper) 6 into the electric heater 2, feed nitrogen 4 at 50ml / min, make the carbonization temperature rise to 1000°C with a heating rate of 10°C / min, and carry out the carbonization treatment for 10 minutes. The temperature is measured with a thermocouple 3 and controlled with a temperature controller 7 . The yield rate of the obtained dry distillation carbide is 22%, the ash content and volatile components measured by JISM8812 are 33% and 3.5% respectively, and the specific surface area measured by BET method is 215m 2 / g. (Example 2)
Embodiment 2
[0060] Sewage sludge (72.9% of water content, 14.7% of ash content, and 12.4% of combustible components) was used as combustible waste. A dry distillate was obtained in exactly the same manner as in Example 1, except that the dry distillation temperature was 1100°C. The yield rate of the obtained dry distillation carbide is 18%, the ash and volatile components measured by JISM8812 are 72% and 0.6% respectively, and the specific surface area measured by BET method is 73m 2 / g. (Example 3)
Embodiment 3
[0061] With 100 parts of combustible waste, add 50 parts by weight of lignite (moisture content 15%, ash content 3.1%, combustible component 81.9%), obtain dry distillate with the method identical with embodiment 2 except this. The yield rate of the obtained dry distillation carbide is 24.7%, the ash and volatile components measured by JIS M8812 are 49% and 0.5% respectively, and the specific surface area measured by the BET method is 149m 2 / g. (Example 4)
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