Method and device for recovering waste water from incineration plant
A complete set of equipment and recovery method technology, applied in separation methods, chemical instruments and methods, permeation/dialysis water/sewage treatment, etc., can solve problems such as difficulty in controlling the dosing of exhaust gas treatment, unstable exhaust temperature, and rising costs , to achieve stable and efficient treatment, stable and efficient heat recovery
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Embodiment 1
[0113] exist figure 1 The shown combustible waste incineration plant operates under the following conditions.
[0114] Heat recovery unit 2 outlet temperature: 230°C
[0115] Cooling device 3 outlet temperature: 188°C
[0116] The temperature difference between the outlet temperature of the heat recovery device 2 and the outlet temperature of the cooling device 3: 42°C
[0117] Boiler discharge water, cooling tower discharge water, miscellaneous drainage, domestic drainage, car washing drainage and floor cleaning drainage discharged from the complete set of incineration equipment according to the following flow rates image 3 process to handle.
[0118] Boiler discharge water: 9m 3 / day
[0119] Cooling tower discharge water: 9m 3 / day
[0120] Miscellaneous drainage: 13m 3 / day
[0121] Domestic drainage: 11m 3 / day
[0122] (sum of the above: 42m 3 / day)
[0123] The sum of car washing drainage and floor cleaning drainage: 6.5m 3 / day
[0124] Boiler discharg...
Embodiment 2
[0146] In Example 1, acid gas treatment was performed by adding slaked lime instead of sodium bicarbonate under the following conditions.
[0147]
[0148] Addition amount: 60kg / hr, equivalent ratio: 2.52 (relative to inlet HCl, SOx)
[0149] In the case of slaked lime treatment, the exhaust temperature is preferably 150°C to 170°C. Therefore, the water recovery rate of the RO membrane separation device 12 is set to 65% and the RO concentrated water volume is 0.58m 3 / hr, set the water supply to the cooling device as 0.85m 3 / hr, the temperature at the outlet of the cooling device was controlled to be 170°C (the temperature difference between the outlet temperature of the heat recovery device 2 and the outlet temperature of the cooling device 3: 60°C), and the same process as in Example 1 was performed except that .
[0150] As a result, a slight reheating was required in the catalytic denitration device, but otherwise, the same efficient treatment as in Example 1 was perfor...
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