Composite absorbent for flue gas desulfurization
An absorbent and flue gas technology, applied in the separation of dispersed particles, chemical instruments and methods, separation methods, etc., to achieve the effect of rich raw material sources, low viscosity, and high mass transfer coefficient
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Embodiment 1
[0029] A performance evaluation method for the application of composite absorbents for flue gas desulfurization in membrane contactors.
[0030] Operating conditions: room temperature (19-22°C), mixed gas pressure 0.11MPa, membrane mass transfer area 1.5 m 2 , the gas flow rate is 0.5-2 L / min, and the liquid flow rate is 200-500mL / min.
[0031] Such as figure 1 shown, respectively from N 2 Gas cylinder 1-1 and SO 2 After the gas in the gas cylinder 1-2 is measured by the gas quality control instrument 2, it enters the mixing and stabilizing tank 3 to form SO containing 0.1%-0.6% (volume percentage). 2 Mixed gas, the mixed gas after the air flow is stabilized enters the membrane contactor 4, and the SO in the mixed gas 2 It diffuses through the membrane pores to the other side of the membrane, is absorbed by the composite absorbent, and enters the liquid phase. The absorbed gas phase is released from the gas outlet at the other end of the membrane contactor. The absorbent i...
Embodiment 2
[0040] The composite absorbent used for flue gas desulfurization is an aqueous solution of potassium citrate / sodium citrate and ethylenediamine, the total concentration of potassium citrate / sodium citrate and ethylenediamine in the aqueous solution is 0.1~6mol / L, citric acid The molar ratio of potassium / sodium citrate to ethylenediamine is 1: (0.5~2).
[0041] The performance evaluation method in Example 1 is used for detection.
[0042] Process operating conditions: room temperature, gas phase pressure 0.11MPa, mixed gas SO 2 Content 0.1%-0.6% (volume percentage), membrane mass transfer area 1.5m 2 , gas velocity: 0.5-2L / min, liquid velocity: 200-500mL / min.
[0043] The performance evaluation results of various absorbents under various conditions are shown in Table 1.
[0044] Table 1 Performance evaluation results of composite absorbents
[0045]
[0046] The results show that the composite absorbent has high adaptability, not only suitable for low-concentration flue ...
Embodiment 3
[0048] The composite absorbent used for flue gas desulfurization is an aqueous solution of potassium citrate / sodium citrate and methoxyethylamine, and the total concentration of potassium citrate / sodium citrate and methoxyethylamine in the aqueous solution is 0.1~6mol / L, the molar ratio of potassium citrate / sodium citrate to methoxyethylamine is 1: (0.5~2).
[0049] The performance evaluation method in Example 1 is used for detection.
[0050] Process operating conditions: room temperature, gas phase pressure 0.11MPa, mixed gas SO 2 Content 0.1%-0.6% (volume percentage), membrane mass transfer area 1.5m 2 , gas velocity: 0.5-2L / min, liquid velocity: 200-500mL / min.
[0051] The performance evaluation results of various absorbents under various conditions are shown in Table 2.
[0052] Table 2 Composite absorbent performance evaluation results
[0053]
[0054] The results show that the composite absorbent has high adaptability, not only suitable for low-concentration fl...
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