Bio-toilet system with subcritical hydrothermal liquefaction as core and fecaluria treatment method
A subcritical water and toilet technology, which is applied in the treatment of black water in toilets, sludge treatment through temperature control, and adaptation to climate change. Low-level problems, to achieve good environmental and economic benefits, complete harmlessness, and ensure biological safety
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Embodiment 1
[0038] Such as figure 1 As shown, an ecological toilet system with subcritical hydrothermal liquefaction as the core disclosed by the present invention includes a material buffer tank 1, a subcritical hydrothermal liquefaction unit 2, a high-temperature heat exchanger 3, a low-temperature heat exchanger 4, a solid-liquid Separator 5, anaerobic influent buffer tank 6, high-temperature anaerobic unit 7, biogas storage and purification device 8, biogas combustion boiler 9, dry granulation unit 10, combined membrane process unit 11, reuse water tank 12 and air cooling tower 14.
[0039] The material buffer tank 1, the subcritical hydrothermal liquefaction unit 2, the high temperature heat exchanger 3, the low temperature heat exchanger 4 and the solid-liquid separator 5 are connected sequentially through pipelines, and the solid outlet of the solid-liquid separator 5 is connected to the drying and granulation unit 10 The solid inlet is connected, the liquid outlet of the solid-liq...
Embodiment 2
[0056] Such as figure 2 As shown, the difference between this embodiment and embodiment 1 is as follows:
[0057] see figure 2 , an ecological toilet system with subcritical hydrothermal liquefaction as the core disclosed by the present invention also includes a heat transfer oil boiler 13; wherein, a biogas combustion boiler 9, a subcritical hydrothermal liquefaction unit 2, a dry granulation unit 10 and a high temperature exchange The oil ports of the heater 3 are connected sequentially through pipelines; the heat transfer oil boiler 13 is heated by electric heating and high-temperature flue gas from the biogas combustion boiler 9 .
[0058] The oil outlet of the heat-conducting oil boiler 13 is connected to the oil inlet of the biogas combustion boiler 9, the oil outlet of the biogas combustion boiler 9 is connected to the oil inlet of the subcritical hydrothermal liquefaction unit 2, and the outlet of the subcritical hydrothermal liquefaction unit 2 The oil port is con...
Embodiment 3
[0070] Such as image 3 As shown, the differences between this embodiment and embodiment 1 and embodiment 2 are as follows:
[0071] When the homogeneous material in the material buffer tank 1 enters the subcritical hydrothermal liquefaction unit 2, a catalyst and an oxidant are added to the subcritical hydrothermal liquefaction unit 2, and the temperature is controlled at 180°C to 260°C to achieve inactivation of pathogens, etc. The molecular level is completely decomposed into CO 2 .
[0072] The harmless mixed material passed through the subcritical hydrothermal liquefaction unit 2 enters the solid-liquid separator 5 and the dry granulation unit 10 for solid-liquid separation and dry granulation of solid matter, and the solid matrix produced is inorganic salt.
[0073] In summary, the present invention uses subcritical hydrothermal liquefaction technology as the core to realize the harmless disposal of toilet excrement; combined with heat transfer oil boiler 13, biogas co...
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