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. 2016 Jun 13;2(6):424–429. doi: 10.1021/acscentsci.6b00139

Table 1. Catalytic CH4 Oxidation Rates for Various Zeolite Topologiesa.

material framework cage shape cage size (Å)26 channel size (Å)27 Si/Alnomb Si/Altotc Cu/Altotd specific activitye STY (h–1 × 10–3)f
H-ZSM-5 MFI     5.3 × 5.6 11.5 13.2 0.31 1.79 ± 0.02 5.2 ± 0.05
        5.1 × 5.5          
H-Beta BEA     6.6 × 6.7 12.5 13.3 0.30 0.80 ± 0.01 2.4 ± 0.04
        5.6 × 5.6          
MCM-41 MCM-41     30 12 16.1 0.74 0.36 ± 0.02 0.6 ± 0.03
H-ZSM-5 MFI     5.3 × 5.6 11.5 13.9 0.13 0.84 ± 0.02 6.0 ± 0.17
        5.1 × 5.5          
H-mordenite MOR     6.5 × 7 10 11.1 0.14 0.84 ± 0.01 4.6 ± 0.08
        2.6 × 5.7          
H-ferrierite FER     4.2 × 5.4 10 10.6 0.12 0.44 ± 0.01 2.7 ± 0.04
        3.5 × 4.8          
Na-ZSM-5 MFI     5.3 × 5.6 11.5 13.6 0.37 0.88 ± 0.02 2.2 ± 0.04
        5.1 × 5.5          
Na-Y FAU spherical 9.6 × 9.6 7.4 × 7.4 5.1 4.6 0.45 0.30 ± 0.01 0.3 ± 0.01
Na-SAPO-34 CHA ellipsoidal 9.4 × 9.4 × 12.7 3.8 × 3.8 0.3 0.6 0.02 0.84 ± 0.03 7.9 ± 0.29
Na-SSZ-13 CHA ellipsoidal 9.4 × 9.4 × 12.7 3.8 × 3.8 15 13.8 0.50 3.12 ± 0.01 6.1 ± 0.03
CuOx-MFIg MFI     5.3 × 5.6 0 0
        5.1 × 5.5          
CuOx-BEAg BEA     6.6 × 6.7 0 0
        5.6 × 5.6          
H-ZSM-5g MFI     5.3 × 5.6 11.5 12.9 0 0 0
        5.1 × 5.5          
a

Catalyst pretreatment: 5 h at 823 K under flowing O2, cooled to 483 K under O2 flow and then purged under He for 0.5 h. Initial CH4 oxidation: 0.5 h under 2400 mL h–1 gcat–1 CH4 at 483 K. Reaction conditions: T = 483 K, WHSV = 2400 mL h–1 gcat–1, PCH4 = 98.1 kPa, PH2O = 3.2 kPa, PO2 = 0.0025 kPa (25 ppm).

b

Si/Alnom denotes the nominal silicon to aluminum ratio in the zeolite based on commercial figures or ratios of SiO2 to Al2O3 in synthesis procedures.

c

Si/Altot denotes the ratio of silicon to aluminum atoms ratio within the zeolite calculated using data from inductively coupled plasma mass spectrometry (ICP-MS) measurements.

d

Cu/Altot denotes the ratio of copper to aluminum atoms within the zeolite calculated using ICP-MS.

e

Specific activity = μmolCH3OH h–1 gcat–1.

f

Site time yield (STY) defined as mol CH3OH (mol Cu)−1 h–1.

g

T = 483 K, WHSV = 2400 mL h–1 gcat–1, PCH4 = 93.1 kPa, PH2O = 3.2 kPa, PO2 = 0.051 kPa. The ± symbol denotes 95% confidence intervals.