Analytical thermal model for cylindrical DBD reactors: how to obtain a reliable gas temperature distribution, and why is it so important | The European Physical Journal Applied Physics (EPJ AP)

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Table 2

Main reactions, with their rate coefficient, involved in NOx treatment.

		No.	Rate coefficient	References
Favorable reduction NO → N₂	$e + N_{2} \to e + N^{} + N^{}$	R1	$f (\frac{E}{N})$	[35]
Favorable reduction NO → N₂	$N^{} + NO \to N_{2} + O^{}$	R2	$8.2 \times 10^{- 11} \exp (- \frac{3409}{R T_{g} (x)})$	[36]
Undesirable oxidation NO → N₂	$e + O_{2} \to e + O^{} + O^{}$	R3	$f (\frac{E}{N})$	[15]
	$O^{*} + NO \to {NO}_{2}$	R4	$3.0 \times 10^{- 11} {(\frac{T_{g} (x)}{298})}^{- 0.75}$	[37]
	$O^{*} + {NO}_{2} \to NO + O_{2}$	R5	$6.5 \times 10^{- 12} \exp (- \frac{998}{R T_{g} (x)})$	[37]
	$O^{*} + O_{2} \to O_{3}$	R6	$5.6 \times 10^{- 34} (\frac{300}{T_{g} (x)})$	[38]
	$O_{3} + NO \to {NO}_{2} + O_{2}$	R7	$1.0 \times 10^{- 31} (\frac{300}{T_{g} (x)})$	[38]

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