Multi Purpose Environmental Protection Equipment Automatic ignition Waste Incinerator Machine
- Suitable for: rural household waste, medical waste, pet animal carcasses, industrial waste, etc.
- Calorific value of incineration: mixed calorific value approximately 2800 Kcal/Kg
- Furnace body type: vertical cylindrical type
- Equipment processing capacity: 30-500 kg/h per cycle
- Ignition method: automatic ignition
- Manual ash discharge and feeding
- Auxiliary fuel: liquefied gas (low calorific value 10495 Kcal/Kg)
- Furnace pressure: negative pressure design, no backfire, -3 to -10 mmH₂O column

Shredder, screw conveyor, primary incineration room, secondary incineration room, water mist cooling and dust removal tower, cyclone dust removal tower, dry absorption filter tower, pulse bag filter.
| Supply voltage | 380V/50Hz |
| Total installed power | <50 Kw |
| Processing capacity | 4 T/d |
| Garbage reduction rate | >95% |
| Water consumption | <1 T/h |
| Fuel consumption | Approximately 5-25 kg/h (varies according to waste calorific value) |
| Nitrolime consumption | 6 Kg/h |
| Activated carbon consumption | 2 Kg/h |
| Exhaust emissions | Complies with GB18485-2001 "Pollution Control Standard for Municipal Solid Waste Incineration" |
| Noise | Complies with Class I standard requirements of GB12348-90 "Industrial Enterprise Boundary Noise Standard" |
| Mean time between failures | >3000 h |

Dry garbage enters the shredder from the feed hopper and is processed into fragments approximately 20mm in length, then sent by the screw feeder to the primary incineration chamber for incineration. The primary incineration chamber is combusted by the burner, with temperature controlled at 850-1000°C. After pyrolysis, drying, decomposition, coking and full combustion, the dry waste reduction rate reaches more than 95%, and the remaining ash is automatically discharged.
The high-temperature smoke generated by combustion enters the secondary combustion chamber and is burned again by the burner at temperatures above 1100°C. When the smoke is fully burned, the production of dioxins can be effectively avoided.
After secondary combustion, the flue gas enters the cyclone dust removal tower under the action of the induced draft fan. The dust-containing gas generates centrifugal force during rotation, throwing dust particles with density greater than the gas to the tower wall, removing approximately 75% of the flue gas.
The dust after initial dust removal enters the water mist cooling and dust removal tower, and is fully combined with ultra-fine water mist, quickly cooling the temperature to about 200°C. Through rapid cooling, residual dioxins in the flue gas are effectively eliminated and further dust is removed.
The flue gas then enters the dry absorption filter tower, where it is desulfurized and deacidified through the "spray reactor + activated carbon injection device", and harmful substances are adsorbed to remove odor. The dry dust is further filtered through the pulse bag filter, resulting in no peculiar smell and no foul odor. The smoke is discharged to the atmosphere through the chimney, meeting emission standards.
The remaining ash and dust collected during the treatment process are stored in bags, sealed and buried regularly to prevent soil pollution.

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