Method for removing mercury in flue gas using V2O5/carbon material catalyst
A catalyst and carbon material technology, which is applied in the field of applying V2O5/carbon material catalyst to catalytic oxidation to remove mercury in flue gas, can solve problems such as secondary pollution, and achieve the effects of promoting mercury removal, increasing contact time, and reducing costs.
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Embodiment 1
[0015] 1 gram of activated coke uses 1 ml of 0.1 mol / L NH 4 VO 3 -H 2 C 2 O 4 The solution is immersed for 10 hours, then dried at 110°C for 12 hours, and calcined at 500°C for 2 hours in an argon atmosphere to obtain 1wt% V 2 O 5 / Activated coke catalyst.
[0016] The catalyst was packed in a fixed-bed quartz tube reactor, and both ends were fixed with quartz wool. After the catalyst was heated to 120℃ in the reactor, Hg-containing 0 Simulated flue gas, airspeed 10000h -1 , Constant temperature adsorption for 24h. The composition of the simulated flue gas is: 6.3% O 2 , 6% H 2 O, 1500ppm SO 2 , N 2 For balance gas, Hg 0 The concentration is 420μg / m 3 . Similarly, the mercury removal experiment on activated carbon under the same conditions was carried out as a comparison. The result of the experiment is that the mercury absorption of the catalyst reaches 206 μg / g-catalyst in 24 hours, and the mercury absorption of activated carbon is 19 μg / g-activated carbon.
Embodiment 2
[0018] 1 gram of activated coke uses 1 ml of 0.05 mol / L NH 4 VO 3 -H 2 C 2 O 4 The solution is immersed for 2 hours, then dried at 110°C for 12 hours, and calcined at 450°C for 5 hours in an argon atmosphere to obtain 0.5wt% V 2 O 5 / Activated coke catalyst.
[0019] The catalyst was packed in a fixed-bed quartz tube reactor, and both ends were fixed with quartz wool. After the catalyst was heated to 120℃ in the reactor, Hg-containing 0 Simulated flue gas, airspeed 15000h -1 , Constant temperature adsorption for 24h. The composition of the simulated flue gas is: 6.3% O 2 , 6% H 2 O, 1000ppm SO 2 , N 2 For balance gas, Hg 0 The concentration is 420μg / m 3 . The result of the experiment is that the mercury absorption of the catalyst reaches 140μg / g-catalyst in 24h.
Embodiment 3
[0021] 1 g activated carbon fiber
[0022] Use 1ml 0.5mol / L NH 4 VO 3 -H 2 C 2 O 4 The solution is immersed for 5 hours, then dried at 110°C for 12 hours, and then calcined at 350°C for 10 hours in an argon atmosphere to obtain 5wt% V 2 O 5 / Activated carbon fiber catalyst.
[0023] The catalyst was packed in a fixed-bed quartz tube reactor, and both ends were fixed with quartz wool. After the catalyst was heated to 120℃ in the reactor, Hg-containing 0 Simulated flue gas, airspeed 10000h -1 , Constant temperature adsorption for 24h. The composition of the simulated flue gas is: 6.3% O 2 , 6% H 2 O, 1500ppm SO 2 , N 2 For balance gas, Hg 0 The concentration is 420μg / m 3 . The result of the experiment is that the mercury absorption of the catalyst reaches 234μg / g-catalyst in 24h.
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