Dangerous waste rotary kiln flue gas dry deacidification device
A rotary kiln and flue gas technology, which is applied in the field of dry deacidification, can solve the problems of high difficulty in deacidification reactor, high requirements for ultra-low emissions, and low deacidification efficiency, so as to prolong the contact reaction time and avoid secondary Pollution and low operating costs
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Embodiment 1
[0026] A hazardous waste rotary kiln flue gas dry deacidification device, such as figure 1 As shown, it includes: deacidification agent injection device 1, flue gas static mixing mass transfer device 2, connecting pipe, air cannon 3, ash discharge port 4, Venturi acceleration device 5 and deacidification reactor;
[0027] Wherein, the injection ports of the deacidification agent injection device 1 are evenly distributed on the flue before the flue gas static mixing and mass transfer device 2; the flue gas static mixing and mass transfer device 2 is communicated with the Venturi acceleration device 5 through a connecting pipe; The bottom of the pipe is provided with an air cannon 3 and an ash discharge port 4; the Venturi accelerator 5 is communicated with the deacidification reactor. In addition, the deacidification agent spraying device 1 includes a weighing module and an ejecting device, and the bottom of the weighing module is connected with the ejecting device.
[0028] T...
Embodiment 2
[0032] A method for dry deacidification of flue gas from a hazardous waste rotary kiln, comprising:
[0033] Step 1. The reactant is accurately fed through a weighing module such as a screw feeder, and then the reactant is uniformly sprayed into the flue through the deacidification agent spraying device 1 .
[0034] In step 2, the flue gas and the reactant flow into the flue gas static mixing mass transfer device 2 and are mixed.
[0035] In step 2, the flue gas static mixing and mass transfer device swirl plate 201 of the flue gas static mixing and mass transfer device 2 can enhance the mass transfer effect and promote turbulent mixing of the deacidification reactant and the flue gas.
[0036] Step 3. The mixed flue gas and the reactant are reformed by the Venturi accelerator 5 for flue gas flow field reformation.
[0037] In step 3, further effective mixing of the flue gas and deacidification agent is realized, and conditions are prepared for the reaction.
[0038] Step 4:...
Embodiment 3
[0042] The parameters of the exhaust gas produced by a hazardous waste rotary kiln include: the flue gas volume is 7000Nm3 / h, the temperature is 195℃, the dust content is 5000mg / Nm3, the SO2 content is 150mg / Nm3, and the HCl concentration is 300mg / Nm3.
[0043] The above-mentioned waste gas is treated by the hazardous waste rotary kiln flue gas dry deacidification device of the present application, and the baking soda is used as a reactant to enter the flue gas through the deacidification agent injection device 1, and the flue gas and the reactant are mixed in the static mixing mass transfer device 2. After carrying out turbulent reforming in the Venturi accelerator 5, enter the deacidification reactor inner cylinder 6 to carry out preliminary deacidification reaction, and the baking soda and flue gas after the preliminary deacidification reaction enter the deacidification reactor outer cylinder 7 to carry out secondary deacidification. acid reaction. After passing through the...
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