A self-sufficient heat self-sufficient municipal sludge continuous hydrothermal carbonization system and method
A technology of municipal sludge and carbonization system, which is applied in pyrolysis treatment of sludge, chemical instruments and methods, water/sludge/sewage treatment, etc. It can solve the problems of reducing volume production capacity, unfavorable utilization of factory environmental products, and biochemical toxic substances High content and other problems, to achieve the effect of easy maintenance of equipment, improvement of equipment processing capacity, and elimination of COD and TN
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Embodiment 1
[0071] The embodiment of the thermal self-sufficient municipal sludge continuous hydrothermal carbonization system of the present invention is as figure 1 , figure 2 as shown, figure 2 The first start-up heater and the second start-up heater are omitted, figure 2 The temperature of the sludge transported by the middle heater to the carbonization reactor is the temperature after the sludge is heated up by the heater and the first start-up heater; , The temperature after the second start-up heater heats up.
[0072] The system includes a carbonization device and a wet heat oxidation device. The carbonization device and the wet heat oxidation device are coupled into a system. The carbonization device provides COD as an energy source for the wet heat oxidation device, and the wet heat oxidation device provides heat and temperature for the carbonization device. The whole system realizes heat self-sufficiency and zero pollution emission.
[0073] Carbonization unit includes s...
Embodiment 2
[0118] The structure of Embodiment 2 of the thermal self-sufficient municipal sludge continuous hydrothermal carbonization system of the present invention is as follows Figure 5 As shown, it is the same as the first embodiment, and the steps of the method are also the same.
[0119] The continuous hydrothermal carbonization method of municipal sludge with self-sufficiency in heat in this embodiment, the specific process is as follows:
[0120] The municipal sludge with water content of 85% and dry basis ash content of 40% is pumped into the sleeve-type preheater by a high-pressure sludge pump at a flow rate of 200t / d, the carbonized slurry is heated to 160°C, and then enters the sleeve-type preheater. In the heater, it is heated to 250°C by the wet heat catalysis completion liquid, and then enters the tubular plug-flow carbonization reactor for reaction. The material stays in the carbonization reactor for about 1 hour to complete the carbonization, and then enters the carboni...
Embodiment 3
[0161] The structure of Embodiment 3 of the thermal self-sufficient municipal sludge continuous hydrothermal carbonization system of the present invention is as follows Figure 8 As shown, it is the same as the first embodiment, and the steps of the method are also the same.
[0162] The continuous hydrothermal carbonization method of municipal sludge with self-sufficiency in heat in this embodiment, the specific process is as follows:
[0163] The municipal sludge with water content of 85% and dry basis ash content of 50% is pumped into the sleeve-type preheater by a high-pressure sludge pump at a flow rate of 200t / d, the carbonized slurry is heated to 150°C, and then enters the sleeve-type preheater. In the heater, it is heated to 230°C by the wet heat catalysis completion liquid, and enters the tubular plug-flow carbonization reactor for reaction. The material stays in the carbonization reactor for about 1 hour to complete the carbonization, and then enters the carbonizatio...
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Abstract
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