Multipurpose kitchen garbage treatment system
A kitchen waste and treatment system technology, applied in the direction of solid waste removal, etc., can solve problems such as unsuitable, rough operation, large floor area, etc., to achieve stabilization, fast processing speed, and reduction Effect
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[0023] Example 1
[0024] The present invention designs a multi-purpose kitchen waste treatment system, including the following steps:
[0025] (1) Garbage collection: Centralized storage of kitchen waste for later use;
[0026] (2) Garbage squeezing: the food waste obtained in step (1) is transported to a hydrolysis tank for hydrolysis, the hydrolysis temperature is 220°C, the time is 10min, and the pressure is 1.2MPa, and the hydrolyzed clinker is transported to Crushing and pressing in the crushing press;
[0027] (3) Garbage sorting: sorting and placing the solid garbage and slurry obtained after pressing;
[0028] (4) Garbage treatment: The solid garbage obtained in step (3) is centrally processed and transferred to an incinerator in which the differential pressure of the internal suspension section is controlled at 700 pa, and the air pressure of the boiler air chamber is controlled at 8000 pa for incineration. After the slurry is precipitated for 10 to 24 hours, The liquid is tran
Example Embodiment
[0034] Example 2
[0035] The present invention designs a multi-purpose kitchen waste treatment system, including the following steps:
[0036] (1) Garbage collection: Centralized storage of kitchen waste for later use;
[0037] (2) Garbage squeezing: The food waste obtained in step (1) is transported to a hydrolysis tank for hydrolysis, the hydrolysis temperature is 120°C, the time is 60min, and the pressure is 0.8MPa, and the hydrolyzed clinker is transported to Crushing and pressing in the crushing press;
[0038] (3) Garbage sorting: sorting and placing the solid garbage and slurry obtained after pressing;
[0039] (4) Garbage treatment: The solid garbage obtained in step (3) is centrally processed and transferred to an incinerator with a differential pressure of 900 pa in the internal suspension section, and an incinerator with an air pressure of 9000 pa in the boiler air chamber. After the slurry is precipitated for 10 to 24 hours, The liquid is transported to the anaerobic digesti
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