SCR Flue Gas Denitration Catalyst Honeycomb Catalyst

HoneycombSCRCatalyst1.SCRtechnologyisarecationatuseofthedenitrationcatalystatacertaintemperature(270-400degree),thatNOXinthefluegasmixedwithammoniagasfromthereducingagentsupplythesystemaftertheoccurenceoftheselectivecatalyticreductionreactionofnitrogenandwater,therebyreducingNOXemissions,andreducingsmokepollutiontotheenvironment.
Thechemicaleauationforaselectivecatalyticreactionprocessis:
4NO+4NH3+O2→4N2+6H2O6NO2+8NH3→7N2+12H20
NO+NO2+2NH3→2N2+3H202.Atpresent,commercialSCRcatalystbasicallytoTiO2forthesubstratetoV2O5asthemainactiveingredientinWO3,MoO3foranti-oxidation,anti-drugofauxiliaryingredients.
3.basedonself-rennovation,YuanchenContinuestoseekcomprehensivecooperationwithwellknownenterprisesofadvancedtechnolgyfrombothhomeandabroad.thecompanyhascooperatedwithEE&E,G&G,NE,CCIContheadvancedSCRtechnologyinrentyears,whileestablishedstablerelationshipswithfamousEPDISpowerconstructioncompaniesandequipmentsmanufacturersaswell.
4.HighperformancehoneycombSCRCatalystfeaturesa:highactivity&NOXremovalefficiencyb:lowSO2conversionratec: lowNH3slipd:excellentresistancetoposioning&abrasiome:highdurability&stabilityf:smallvolume,highspecificsurfacearea,economicalandpractical.
5.theCapacityofourProductionofHoneycombSCRCatalystofourcompanyis8000m³/year.
6.Catalystspecificationtable
HoleNumber
Section(mm)
Wallthickness(mm)
Opening(mm)
Percentageopenarea(%)
ApValue(m2/m3)
15*15
150*150
1.35
8.45
71.4
338
18*18
150*150
1.1
7.1
72.6
409
20*20
150*150
1.15
6.25
69.4
445
21*21
150*150
0.95
6.1
72.9
478
22*22
150*150
0.9
5.8
72.4
499
25*25
150*150
1.00
4.90
66.7
544
30*30
150*150
0.80
4.13
68
660
35*35
150*150
0.55
3.65
72.5
795
40*40
150*150
0.5
3.20
72.8
910
45*45
150*150
0.5
2.78
69.5
1000