Method for efficiently desulfurizing and recycling sulfur resources by combining manganese ion aqueous solution with NOx
An aqueous solution, manganese ion technology, applied in separation methods, chemical instruments and methods, dispersed particle separation, etc., can solve problems such as wear and restriction, achieve good effect, less addition, and improve the effect of recycling
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Embodiment 1
[0033] A manganese ion aqueous solution combined with NO x A method for efficient desulfurization and recovery of sulfur resources, comprising the following steps:
[0034] (1) Weigh a certain mass of manganese sulfate and add it into a bubbling reactor with 250 mL of water, and mix evenly by stirring, so that Mn 2+ The mass concentration in water is 0.005 g / L, and it is prepared as an aqueous solution of manganese ions.
[0035] (2) The coal-fired flue gas is introduced into the bubbling reactor and absorbed by the manganese ion aqueous solution. Before coal-fired flue gas enters the bubble reactor, SO 2 The concentration is 2000 mg / Nm 3 , the oxygen content is 8 vol%, NO X The concentration is 30 mg / Nm 3 , the total flow rate of flue gas is 500mL / min, the temperature of manganese ion aqueous solution is 65 ℃, and the stirring intensity is 800 r / min.
[0036] (3) Determination of SO in the flue gas at the outlet of the bubble reactor 2 and NO x concentration, calculat...
Embodiment 2
[0038] A manganese ion aqueous solution combined with NO x A method for efficient desulfurization and recovery of sulfur resources, comprising the following steps:
[0039] (1) Weigh a certain mass of manganese sulfate and add it into a bubbling reactor with 250 mL of water, and mix evenly by stirring, so that Mn 2+The mass concentration in water is 0.1 g / L, and it is prepared as an aqueous solution of manganese ions.
[0040] (2) The coal-fired flue gas is introduced into the bubbling reactor and absorbed by the manganese ion aqueous solution. Before coal-fired flue gas enters the bubble reactor, SO 2 The concentration is 2500 mg / Nm 3 , the oxygen content is 10 vol%, NO X The concentration is 900 mg / Nm 3 , the total flow rate of flue gas is 500 mL / min, the temperature of manganese ion aqueous solution is 45 ℃, and the stirring intensity is 800 r / min.
[0041] (3) Determination of SO in the flue gas at the outlet of the bubble reactor 2 and NO x concentration, calculat...
Embodiment 3
[0043] A manganese ion aqueous solution combined with NO x A method for efficient desulfurization and recovery of sulfur resources, comprising the following steps:
[0044] (1) Weigh a certain mass of manganese sulfate and add it into a bubbling reactor with 250 mL of water, and mix evenly by stirring, so that Mn 2+ The mass concentration in water is 0.8 g / L, and it is prepared as an aqueous solution of manganese ions.
[0045] (2) The coal-fired flue gas is introduced into the bubbling reactor and absorbed by the manganese ion aqueous solution. Before coal-fired flue gas enters the bubble reactor, SO 2 The concentration is 1200 mg / Nm 3 , the oxygen content is 10 vol%, NO X The concentration is 200 mg / Nm 3 , the total flow rate of flue gas is 500 mL / min, the temperature of manganese ion aqueous solution is 20 ℃, and the stirring intensity is 800 r / min.
[0046] (3) Determination of SO in the flue gas at the outlet of the bubble reactor 2 and NO x concentration, calcula...
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