System and method for treating polluted gas
A technology for polluting gases and treatment methods, which is applied in the direction of gas treatment, separation methods, chemical instruments and methods, etc., to achieve stable operation, significant denitrification effect, and cost and energy saving effects
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Embodiment 1
[0033] Please refer to figure 1 . The pollution gas treatment system shown includes: the first chemical looping combustion reactor 101 filled with the oxidation state 107 of the copper-based oxygen carrier, and the second chemical looping combustion reactor filled with the reduced state 108 of the copper-based oxygen carrier 102. Pollution gas pipeline 109, air blower 111, air pipeline 112, reduction reaction product gas pipeline 110, oxidation reaction product gas pipeline 113, and electric three-way valve groups 103-106. The active substance of the copper-based oxygen carrier is CuO, and the carrier is SiO 2. The polluting gas contains NH 3 .
[0034] The polluted gas enters the first chemical looping combustion reactor 101 through the three-way valve 103 on the polluted gas pipeline 109, and undergoes a reduction reaction with the oxidized oxygen carrier 107: the NH in the polluted gas 3 React with the oxidized oxygen carrier 107 to generate nitrogen and water vapor, w...
Embodiment 2
[0043] Please refer to figure 2 . Compared with Example 1, this embodiment differs in that: the oxygen carrier is an iron-based oxygen carrier, and its active material is Fe 2 o 3 , the carrier is Al 2 o 3 . The temperature of reduction reaction and oxidation reaction is 300°C. A sulfur dioxide capture device 200 is arranged on the oxidation reaction product gas pipeline 113 to capture SO in the oxidation reaction product gas 2 , the sulfur dioxide capture device 200 is a wet desulfurization device using limestone or lime slurry as a desulfurizing agent. Pollution gas contains trimethylamine and H 2 S.
[0044] Oxidation states of iron-based oxygen carriers with trimethylamine and H 2 The reduction reaction of S, and the reduced state and iron sulfide with O 2 The reaction equation of the oxidation regeneration reaction and the standard free energy change and reaction heat at the reaction temperature are as follows:
[0045] 63Fe 2 o 3 +2C 3 h 9 N(g)=42Fe 3 o ...
Embodiment 3
[0053] Please refer to figure 2 . Compared with Example 2, this embodiment differs in that: the oxygen carrier is a nickel-based oxygen carrier, its active material is NiO, and the carrier is TiO 2 . The temperature of the reduction reaction and the oxidation reaction is 350°C, and a sulfur dioxide capture device 200 is installed on the oxidation reaction product gas pipeline 113 to capture SO in the oxidation reaction product gas 2 , the sulfur dioxide trapping device 200 is a dry desulfurization device using calcium oxide as a desulfurizing agent. The polluting gas contains methyl mercaptan and toluene.
[0054] Reduction reactions of the oxidized state of nickel-based oxygen carriers with methyl mercaptan and toluene, and the reduced state and nickel sulfide with O 2 The reaction equation of the oxidation regeneration reaction and the standard free energy change and reaction heat at the reaction temperature are as follows:
[0055] 4NiO+CH 3 SH(g)=NiS+3Ni+CO 2 +2H ...
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