12.07.2015 Views

Boreskov Institute of Catalysis SB RAS, Novosibirsk, Russia

Boreskov Institute of Catalysis SB RAS, Novosibirsk, Russia

Boreskov Institute of Catalysis SB RAS, Novosibirsk, Russia

SHOW MORE
SHOW LESS
  • No tags were found...

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

OP-2-20EFFECT OF Ag DOPING IN La-Mn PEROVSKITES FOR THECATALYTIC FLAMELESS COMBUSTION OF METHANEBuchneva O. 1 , Rossetti I. 1 , Kryukov A. 2 , Forni L. 11 Dip. Chimica Fisica ed Elettrochimica, Università di Milano, v. C. Golgi, 19, 20133Milano, Italy. Fax: +39-02-50314300, e-mail: ilenia.rossetti@unimi.it2 D.I. Mendeleev University <strong>of</strong> Chemical Technology <strong>of</strong> <strong>Russia</strong>, Miusskaya sq. 9,125047, Moscow, <strong>Russia</strong>Samples with nominal composition La 1–x Ag x MnO 3 with x=0, 0.05, 0.1 wereprepared by flame pyrolysis (FP) and by the so-called sol-gel «citrate method» (SG).Lower specific surface area was obtained with the SG-prepared catalysts than withthe FP ones. Silver introduction increased the surface area in all cases. However, noclear relationship between surface area and silver loading was observed. Due to thepoor solubility <strong>of</strong> silver in the perovskite lattice, reflections <strong>of</strong> metallic silver weresometimes observed for the doped samples on XRD spectra, with increasingintensity at high Ag loading. Almost all our samples exhibited a very high activity forthe catalytic flameless combustion (CFC) <strong>of</strong> methane. Indeed, under the adoptedreaction conditions full methane conversion was attained below 600°C. The SGpreparedLaMnO 3 catalyst represented an exception, reaching a maximum 65%methane conversion at 600°C. The activity <strong>of</strong> FP-prepared catalyst was alwayshigher than that <strong>of</strong> SG-prepared ones with identical nominal composition. Partialsubstitution <strong>of</strong> Ag for La led to increasing activity both for SG and FP preparedcatalysts and the catalytic activity increased with increasing the Ag substitution.The resistance to sulphur poisoning was checked for all catalysts, in view <strong>of</strong> theirapplication for the CFC <strong>of</strong> biogas. Catalyst poisoning [1,2] was done in operando at450°C by injecting several doses <strong>of</strong> tetrahydrothiophene. All samples lost part <strong>of</strong> theirinitial activity after poisoning. Silver substitution did not change the resistance topoisoning for FP prepared samples, whereas a more severe activity loss wasobserved for the poisoned Ag-doped samples than for the unsubstituted one whenprepared by SG. However, due to the great positive effect <strong>of</strong> Ag on the initial activityinitial activity, the residual conversion after poisoning <strong>of</strong> all the doped samples wasstill higher than for undoped LaMnO 3 .[1]. I. Rossetti, O. Buchneva, C.Biffi, R. Rizza. Appl. Catal. B: Environmental, 89 (2009) 383.[2]. O. Buchneva, I. Rossetti, C. Biffi, M. Allieta, A. Kruykov, N. Lebedeva. Appl. Catal. A: General 370(2009) 24.64

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!