Table 4 Estimated heats of adsorption and activation energies, relative to E3f.

From: Kinetic modelling of catalytic N2O removal

Parameter

Sample 1

Sample 2

Sample 3

\(\Delta {H_{{O_*}}}\)

-1.0

-1.8

-0.80

\(\Delta {H_{N{O_*}}}\)

-0.21

-2.6 × 10− 6

-0.49

\(\Delta {H_{N{O_{2*}}}}\)

-6.7 × 10− 3

-3.4 × 10− 6

-3.0 × 10− 4

\(\Delta {H_{{N_2}{O_*}}}\)

-0.11

-4.8 × 10− 7

-5.1 × 10− 2

\(\Delta {H_{N{H_{3*}}}}\)

-0.28

-1.7 × 10− 7

-0.71

\(\Delta {H_{{H_2}{O_*}}}\)

-7.6 × 10− 6

-2.9 × 10− 2

-3.6 × 10− 5

\(E{a_{k3,f}}\)

1.0

1.0

1.0

\(E{a_{k3,r}}\)

0.36

0.56

0.38

\(E{a_{k6}}\)

0.76

1.4

0.24

\(E{a_{k8}}\)

-6.4 × 10− 2

-0.15

-3.5 × 10− 2

\(E{a_{k9}}\)

0.10

0.19

-0.24

\(E{a_{k10}}\)

-0.12

-1.8 × 10− 2

-0.12

\(E{a_{k11}}\)

0.28

0.53

0.34

\(E{a_{k12}}\)

-0.29

0.25

0.26

\(E{a_{k14}}\)

0.28

0.22

0.58

\(E{a_{k15}}\)

-2.0

-0.44

4.3