(173e) Modeling of Fast Cycling NOx Storage and Reduction – Effect of Reductants, Thermal Effect, and HC-Intermediate Mechanism | AIChE

(173e) Modeling of Fast Cycling NOx Storage and Reduction – Effect of Reductants, Thermal Effect, and HC-Intermediate Mechanism

Authors 

Harold, M. - Presenter, University of Houston
Balakotaiah, V. - Presenter, University of Houston
Ting, A. W. L., Caterpillar

Modeling
of Fast Cycling NOx Storage and Reduction – Effect of Reductants, Thermal
Effect, and HC-intermediate mechanism

Allen Wei-Lun Ting, Michael P. Harold
and Vemuri Balakotaiah

Department of Chemical & Biomolecular Engineering,
University of Houston, Houston, TX 77204, USA

Abstract

A modeling study of fast cycling NOx
storage and reduction (NSR) with C3H6 and H2
for emission control of lean burn gasoline and diesel vehicles is carried out
using 1-D two phase catalytic monolith reactor model including the washcoat
diffusion. Our recent experimental study shows that when cycling time is
reduced from 70 s to 7 s the thermal effect and impact of reductants, including
HC-intermediate pathway, may be minor factors in enhancement of NOx conversion comparing
to the better utilization of sites. This work proposed a global kinetics for modeling
previous mentioned experimental results and providing mechanistic insights
through calculated spatio-temporal site coverages, species concentrations and
temperature profiles.

At temperature higher than 350 oC,
negligible difference in NOX conversion between H2 and C3H6
is observed under slow cycling, and under fast cycling the C3H6
outperforms H2 by 7 % (Fig. 1a) at temperature higher than 450 oC
due to higher molecular diffusivity of H2, which results in larger
NOx puff (Fig. 1b.)

This work proposed a simplified
mechanism for HC-intermediate (selected as C2H3NCO)
NOx
reduction pathway:

2 C3H6 + Ba(NO3)2,fà
(C2H3NCO)2-BaOf + 3 H2O                                                                  (R1)

(C2H3NCO)2-BaOf
+ 15/2O2à 6CO2 + 3 H2O + N2 +
2 BaOf,                                                 (R2)

This HC-intermediate pathway can
predict the formation of double peaks of N2 (Fig. 2), while it show
little enhancement in NOx conversion. This pathway requires ~2.5 times C3H6
(compared to traditional pathway) to reduce same amount of stored NOx to N2.
Due to this stoichiometry in NOx reduction, HC-intermediate pathway may decrease
the ignition temperature by 30 oC but reduce NOx conversion by ~5%
at temperature higher than 450 oC (Fig. 3), due to larger NOx puff
resulting from insufficient reductant (Fig. 1b). This estimates the maximum
effect of HC-intermediate pathway on NOx conversion because simpler
intermediates (like NCO) from C3H6 may not perform beyond
this prediction, as long as no other reactions dominate.

Modeling results are also used to distinguish
NOx reduction pathways when using C3H6. From predicted
spatio-temporal analysis, actual regeneration of stored NOx occurs at
temperature 30 – 45 oC lower than cyclic averaged mid monolith
temperature. At temperature higher than 350 oC, most reductants are
completely oxidized by oxygen stored on ceria sites during/where most stored
NOx is reduced, while most of CO and H2 measured at later time are actually
spectator that don’t react with stored NOx. This makes it difficult to
distinguish what pathway NOx is reduced through, but selectivity of the spectator
H2 and CO may help estimate.

Fig.
1 (a) Comparison of the experimental (marker) predicted (line) cyclic
averaged NOx conversion between slow cycling (solid line and circle marker) and
fast cycling (dashed line and triangle marker) with anaerobic rich feed and with H2
(black) and C3H6
(red). (b)
comparison of the experimental (solid line) predicted (dashed line) NOx
effluent concentration under fast cycling with anaerobic rich feed and with H2
(black), C3H6 (red), C3H6 w/o
HC-intermediate mechanism (blue) at feed temperature of 488 oC.

Fig.
2 Comparison of the model predicted double peak N2 effluent
concentration (line) and experimental m/e = 28 signal (circle) under slow (a)
and fast (b) cycling at feed temperature of 326 oC with H2
(black) and C3H6 (red).

Fig.
3 Comparison of model predicted NOx (a) and C3H6 (b) conversion
between with (solid line) and without (dashed line) proposed HC-intermediate mechanism
during slow (black) and fast cycling (red).