A kind of renewable flue gas desulfurizer and its application
A technology for regenerating flue gas and desulfurizers, applied in the direction of dispersed particle separation, chemical instruments and methods, separation methods, etc., can solve the problems of absorbent loss of absorption, etc.
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Embodiment 1
[0030] Composition (weight percent) of renewable flue gas desulfurizer:
[0031] β-Hydroxyethylethylenediamine: 20%
[0032] Phosphoric acid: 10%
[0033] Citric acid: 2%
[0034] Hydroquinone: 0.2%
[0035] Sodium nitrite: 0.8%
[0036] Deionized water: 67%
[0037] The experimental setup consists of four parts:
[0038] 1) Gas distribution system: The simulated flue gas is controlled by nitrogen, air, carbon dioxide, sulfur dioxide and nitric oxide through a mass flow meter to provide accurate gas flow to the system and form gases with different concentrations. The simulated flue gas is uniformly passed through the mixer and then enters the heating furnace to be heated and mixed with water vapor from another way to 200-300°C and then enters the washing system.
[0039] 2) Washing system: The circulating washing water is extracted from the bottom of the washing tower, and after being measured by the flow meter, it enters the nozzle of the washing tower in two ways to co...
Embodiment 2
[0047] Composition (weight percent) of renewable flue gas desulfurizer:
[0048] 1,4-bis(2-hydroxyethyl)piperazine: 30%
[0049] Sulfurous acid: 18%
[0050] p-Phenylenediamine: 0.5%
[0051] Sodium Phosphate: 0.5%
[0052] Deionized water: 51%
[0053] The experimental device is the same as in Example 1, and the experimental conditions are: absorption temperature 55°C, liquid-gas ratio 0.5kg / m 3 .
[0054] The experimental results are shown in Table 2.
[0055] Table 2 Absorption effect of desulfurizer in Example 2
[0056]
[0057] Shown by the data in table 2: the renewable flue gas desulfurizer of the present invention has an effect on SO in flue gas 2 The content fluctuates between 2000~8200mg / m 3 When fluctuating, it can ensure that the desulfurization rate is above 90%, the regeneration steam consumption is low, and the steam consumption is reduced by more than 30%.
Embodiment 3
[0059] Composition (weight percent) of renewable flue gas desulfurizer:
[0060] 1,4-bis(2-hydroxypropyl)piperazine: 10%
[0061] Hydroxyethylpiperazine: 15%
[0062] Sulfuric acid: 8%
[0063] Sulfurous acid: 7%
[0064] p-Phenylenediamine: 0.5%
[0065] Sodium nitrite: 1%
[0066] Deionized water: 58.5%
[0067] The experimental device is the same as that in Example 1, and the experimental conditions: the absorption temperature is 40°C, and the liquid-gas ratio is 1kg / m 3 .
[0068] The experimental results are shown in Table 3.
[0069] Table 3 Example 3 Desulfurization agent absorption effect
[0070]
[0071] Shown by the data in table 3: the renewable flue gas desulfurizer of the present invention has an effect on SO in flue gas 2 The content is 1500~2500mg / m 3 When fluctuating, the desulfurization rate can be guaranteed to be around 96%, and as the absorption temperature decreases, the consumption of regeneration steam is greatly reduced by nearly 50%.
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