Sodium salt containing fume purification solution treatment process
A technology of flue gas purification and solution treatment, which is applied in the field of flue gas purification, can solve problems such as no solutions have been proposed, and achieve the effects of reducing energy consumption, reducing production energy consumption, and improving economic benefits
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Embodiment 1
[0025] This example proposes a treatment process for flue gas purification solution containing sodium salt. The treatment system is a treatment process for the residual liquid obtained from the crystallizer during the preparation of ammonium sulfate by-product during the preparation of sodium bicarbonate from flue gas purification waste liquid. We know that the process of preparing sodium bicarbonate from flue gas purification waste liquid is that in the wet process using sodium bicarbonate as the desulfurization and denitrification absorbent, the obtained waste liquid is added to ammonium bicarbonate or NH 3 , CO 2 The process in which sodium bicarbonate is produced by reaction is recycled as an absorbent; the preparation process of by-product ammonium sulfate is to add ammonium bicarbonate or NH 3 , CO 2 The process of preparing ammonium sulfate from the liquid obtained after separation, such as figure 1 shown. The above-mentioned remaining liquid is the feed liquid obtai...
Embodiment 2
[0028] The difference between this embodiment and embodiment 1 is as follows:
[0029] The dryer used in this example is a tower structure, and the atomizer installed on the top of the dryer is a centrifugal atomizer. The top of the dryer is also equipped with a hot air distributor connected to the hot air inlet pipe, which can distribute the hot air evenly. into the dryer. The remaining liquid obtained by the crystallization separator is pressurized and transported to the atomizer installed on the top of the dryer. Under the action of high-speed centrifugal force, the atomizer atomizes the feed liquid into fine mist groups, which greatly increases the surface area of the feed liquid , and then in the case of sufficient exchange with hot air, the water evaporates rapidly and dries into small particles.
[0030] The dry gas used in this embodiment is air at normal temperature, and the dry gas is heated to 300° C. by an electric heater.
Embodiment 3
[0032] The difference between this embodiment and embodiment 1 is as follows:
[0033] The dryer used in this embodiment is a box-type dryer, and the atomizer on the top of the dryer is a pressure-type atomizer. into the dryer.
[0034] The dry gas used in this example is coke oven flue gas, which is heated to 250° C. by an electric heater.
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