Composite smoke denitration catalyst capable of oxidizing zero-valence mercury
A denitrification catalyst and composite technology, which is applied in the field of composite flue gas denitrification catalyst and its preparation, can solve the problems of catalytic oxidation efficiency reduction, activity impact, investment increase, etc.
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Embodiment 1
[0030] Example 1 Preparation of composite flue gas denitrification catalyst capable of oxidizing zero-valent mercury
[0031] The preparation method comprises the following steps:
[0032] (1) Titanium dioxide is mixed with 1.75 times the weight of deionized water, heated at 60°C for 24 hours, dried at 80-100°C for 8 hours, then heated at 120°C for 72 hours, ground and sieved to obtain 60-100 mesh pre-activated titanium dioxide particles.
[0033] (2) Weigh cerium nitrate (Ce(NO 3 ) 3 ·6H 2 O), dissolved in deionized water, adding 75-100g of pre-activated carrier titanium dioxide, adding ammonium carbonate aqueous solution while stirring until Ce(OH) 3 The precipitates were all precipitated and deposited on the carrier TiO 2 on, filtered and washed to obtain Ce(OH) 3 / TiO 2 .
[0034] (3) Weigh ammonium vanadate with a vanadium content of 1.5g and ammonium tungstate with a tungsten content of 8.5g, mix them, dissolve them in deionized water, and mix with t...
Embodiment 2
[0037] Example 2 Preparation of composite flue gas denitrification catalyst capable of oxidizing zero-valent mercury
[0038] (1) Titanium dioxide activation steps are the same as in Example 1
[0039] (2) Weigh cerium nitrate (Ce(NO 3 ) 3 ·6H 2 O), stir with deionized water until completely dissolved, add 75-100 g of pre-activated carrier titanium dioxide, add ammonium carbonate aqueous solution while stirring, until Ce(OH) is generated 3 The precipitates were all precipitated and deposited on the carrier TiO 2 on, filtered and washed to obtain Ce(OH) 3 / TiO 2 .
[0040] (3) Weigh ammonium vanadate with a vanadium content of 1.5g and ammonium molybdate with a molybdenum content of 8.25g, mix them, dissolve them in deionized water, and mix with the material obtained in step (2), at 60-80°C Heat and stir to make it impregnated in Ce(OH) 3 / TiO 2 surface until the moisture evaporates and then tumble dry.
[0041] (4) Dry the material obtained in step (3) at 60-1...
Embodiment 3
[0043] Example 3 Preparation of composite flue gas denitrification catalyst capable of oxidizing zero-valent mercury
[0044] The SCR denitrification catalyst V for coal-fired power plants customized according to the following weight ratio was purchased from the supplier 2 o 5 -WO 3 / TiO 2 : 1.25 parts by weight of element V, 8.0 parts by weight of element W, TiO 2 It is 75~100 parts by weight, then through the following steps:
[0045] (1) Weigh cerium nitrate with 3 parts by weight of Ce element; add the commercial SCR catalyst into the cerium nitrate aqueous solution, and heat at 60-80°C until the water evaporates.
[0046] (2) Dry the SCR catalyst impregnated with cerium nitrate at 100-120°C.
[0047] (3) Heat up to 350-450°C at a rate of 8-20°C / min, and bake for 5 hours to obtain the composite SCR catalyst of the present invention: 1.25V 2 o 5 -3CeO 2 -8.0WO 3 / TiO 2 , pressed into 20-40 mesh particles, the catalyst code is C.
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