Organic waste liquid graded denitration device and method
A technology for organic waste liquid and denitrification, which is applied in separation methods, combustion methods, chemical instruments and methods, etc., can solve the problems that the advantages of low nitrogen are not maximized, reduce the denitration efficiency of organic waste liquids, etc., and reduce purification and operation costs. , High denitration efficiency, the effect of avoiding system blockage
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Embodiment 1
[0040] This example is a case of two-step denitrification of low-salt or no-salt organic waste liquid. The denitrification device is as follows figure 2 As shown, according to the hazardous waste low-nitrogen emission graded incineration process of the embodiment of the present invention, the present invention provides a graded denitrification device for organic waste liquid, including a solid waste incineration device, a primary denitrification device, a secondary denitrification device, waste heat recovery system, flue gas purification system. The solid waste incineration device is provided with a solid waste feeding port, an air supply port and a flue gas inlet; the first-stage denitration device is provided with a waste liquid spray gun, a flue gas inlet and a reducing gas outlet; There are vents. The flue gas outlet of the rotary kiln is connected with the flue gas inlet of the primary denitration device, and the reducing gas outlet of the primary denitrification device...
Embodiment 2
[0060] This example is a case of two-step denitrification of high-salt organic waste liquid. The denitrification device is as follows image 3 shown. In this case, the primary denitrification device is divided into two parts, with a flue gas inlet and a slag discharge port at the bottom, where the flue gas inlet is connected to the flue gas outlet of the solid waste incineration device. By setting the internal dimensions of the lower region, the gas flow rate in this region is lower than the free settling velocity of the salt particles contained in the waste liquid. The temperature in the lower area should be lower than the melting temperature of the salt ash contained in the waste liquid. The salt contained in chemical waste liquid is usually represented by NaCl, KCl, Na 2 CO 3 Mainly, the temperature in this region is usually below 800 °C (NaCl salt melting temperature). Control the oxygen content at the outlet of the solid waste incineration flue gas, preferably below 2...
Embodiment 3
[0065] This implementation is a case of treating high-salt and low-salt / salt-free organic waste liquid at the same time. For the denitrification device, see Figure 4 . In this embodiment, the high-salt organic waste liquid is sprayed from the lower area to perform denitrification, thermal cracking and desalination. The temperature in this area should be lower than the temperature corresponding to the melting of the contained inorganic component salts.
[0066] Low-salt / salt-free organic waste liquid is fed from the upper area for denitrification and thermal cracking, and the temperature in this area should be maintained above 850°C.
[0067] All the other steps are similar to Example 2.
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