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![Page 1: Experimental characterization and molecular simulation of nitrogen complexes formed upon NO–char reaction at 270 °C in the presence of H2O and O2](https://reader038.fdocuments.us/reader038/viewer/2022100421/57501ede1a28ab877e92d459/html5/thumbnails/1.jpg)
Carbon 42 (2004) 1507–1515
www.elsevier.com/locate/carbon
Experimental characterization and molecular simulationof nitrogen complexes formed upon NO–char reaction
at 270 �C in the presence of H2O and O2
Pilar Garc�ıa a, Juan F. Espinal a, Concepci�on Salinas Mart�ınez de Lecea b,*,Fanor Mondrag�on a,*
a Institute of Chemistry, University of Antioquia, A.A. 1226 Medell�ın, Colombiab Department of Inorganic Chemistry, University of Alicante, A.A. 99-E-03080 Alicante, Spain
Received 27 September 2003; accepted 26 January 2004
Available online 16 March 2004
Abstract
Surface nitrogen complexes formation upon reaction of coal char with NO at 270 �C in the presence or absence of O2 and/or H2O
was studied by XPS. Complexes such as pyrrolic-N type, pyridine-N-oxide, pyridinic-N and –NO2 were observed. The major
increment was in pyridinic-N. Water had a partial inhibition effect while oxygen promotes the formation of the nitrogen complexes
probably due to char gasification. The gasification level in mixtures with O2 varied according to the presence or not of H2O. TPD
was used to quantify reversible NO adsorption and oxygen surface groups formed on the char during reaction. Molecular modeling
was applied to determine the thermodynamics of the reactions. Mechanisms are proposed to explain the formation of pyridinic and
–NO2 complexes at low temperatures.
� 2004 Elsevier Ltd. All rights reserved.
Keywords: C. Chemisorption, Computational chemistry, X-ray photoelectron spectroscopy; D. Catalytic properties, Surface oxygen complexes
1. Introduction
Acid rain, the depletion of stratospheric ozone layer
and photochemical smog caused by nitrogen oxidesemissions have resulted in strict regulations to control
the release of these polluting gases. Nitrogen oxides are
formed in several industrial processes such as power
generation units, waste incinerators, nitric acid manu-
facture as well as in mobile sources. Improvement of
these industrial processes and engine designs are neces-
sary to mitigate emissions of nitrogen oxides [1] like
nitric oxide, one of the polluting gases produced inconventional fossil fuel combustion systems.
Many catalytic processes have been extensively stud-
ied to reduce nitric oxide to N2 [2,3]. Moreover, NO
reduction using carbon materials has been widely
investigated with important findings. At temperatures
*Corresponding authors. Tel.: +57-421-056-59; fax: +57-426-382-
82.
E-mail addresses: [email protected] (C. Salinas Mart�ınez de Lecea),
[email protected] (F. Mondrag�on).
0008-6223/$ - see front matter � 2004 Elsevier Ltd. All rights reserved.
doi:10.1016/j.carbon.2004.01.065
higher than 400 �C, NO is chemisorbed on the solid
carbon surface forming C(N) and C(O) complexes. Then,
the C(N) complexes react with NO forming N2 [4–6].
Carbon gasification at these temperatures creates newactive sites which promote NO chemisorption. Since
molecular oxygen increases the carbon gasification, its
presence enhances NO reduction [7,8]. The role of sur-
face nitrogen complexes in NO reduction has been
investigated with the aid of computational chemistry [9–
11]. However, some of the complexes suggested by this
method are different from those identified by XPS
[1,7,12,13]. Fig. 1 presents the most important nitrogencomplexes observed on char surfaces after reaction with
NO at temperatures higher than 400 �C [7]. They are (1)
pyridinic complex (N-6, Fig. 1(A)) where the N1s elec-
tron binding energy used for its characterization by XPS
is 398.7 ± 0.3 eV, (2) pyrrolic complexes (N-5, Fig. 1(B)),
binding energy at 400.2 ± 0.3 eV [7,13], (3) pyridone (Fig.
1(C)) and nitroso complexes (–NO, Fig. 1(D)) which
have XPS binding energies equal to that of N-5 [13–15],(4) complexes found in minor quantities such as qua-
ternary-N (N-Q) in the ‘‘centre’’ position at 399.2 eV
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H
ON
O-
HO
N+
O
N
NN
NN
NN N
OH
O
(B)(C)(A) N-6
(D)
N-X
+
(H)
N-Q(F)(E) (G)
-NO2(I)
N-5
Fig. 1. Schematic representation of the most commonly found carbon
surface nitrogen complexes.
1508 P. Garc�ıa et al. / Carbon 42 (2004) 1507–1515
(Fig. 1(E)) and in the ‘‘valley’’ position at 401.7 eV (Fig.
1(F)) [13]. Another type of N-Q complexes assigned to
the signal at 401.7 eV are those of pyridinic-N with a
positive formal charge due to strong interaction with
oxygen functionalities [14–17] or with the hydrogen of
OH groups (Fig. 1(G)) [7,13,15], (5) pyridinic-N-oxide
complexes at 403.1 ± 0.3 eV (N-X, Fig. 1(H)), and lastly,(6) nitro type complexes (–NO2), identified at 406.1 eV
(Fig. 1(I)) [7,13,17].
In the NO–carbon reaction, the identification of
intermediates is an important step towards under-
standing the reduction mechanism. However, this is a
difficult task to carry out at high temperatures due to the
fast transformations that the intermediate structures can
undergo. To overcome this problem, reactions at lowtemperatures can be used to obtain information on some
of these complexes. By doing this, it is assumed that
some of the active sites capable of forming nitrogen
complexes at high temperatures are similar to those
found at low temperatures, as has been proposed by
Suuberg et al. [8,18]. In a recent study on the reaction of
NO–char at 100 �C [19], it was observed that –NO2 and
N-6 surface complexes were the ones predominantlyformed.
Although in the reduction of NO by carbon, the
formation of surface nitrogen complexes could be af-
fected by all of the other components in the combustion
effluents, our interest in the present research was to
study only the effects of O2 and H2O on the interaction
of NO with the carbon surface. It is known that at high
temperatures the O2 enhances the rate of NO reductionby the char and that the N-complexes formed on the
solid surface (mainly pyridinic and pyrrolic) are similar
to those formed in an oxygen free atmosphere [7,12]. In
addition, the presence of O2 decreases the NO reduction
temperature [12]. Studies on the effect of water on the
reaction system are rather scarce [8,20,21] and therefore
there is little information on how water interferes or
promotes the formation of nitrogen complexes.
Our objective in this research was to investigate the
reaction of NO with carbon surfaces at 270 �C in
the presence of water and molecular oxygen. After the
reaction, the surface was characterized by XPS and bytemperature programmed desorption of the complexes.
A complementary molecular modeling study was carried
out in order to obtain thermodynamic data and to ex-
plain the formation mechanisms of the N-complexes
experimentally observed.
2. Experimental
2.1. Reaction conditions and sample characterization by
XPS
The char used in the experiments described here wasprepared from a subbituminous coal (mesh 100/200)
collected from the Amag�a mine in Colombia. The coal
sample was pyrolyzed at 700 �C for 2 h under N2
atmosphere. The NO reduction reaction was carried out
in a tubular quartz reactor using 0.4 g of char. The
temperature was monitored with the aid of a thermo-
couple attached to the reactor external wall, completely
imbibed in the sample bed. Before each experiment, thesample was heat treated at 700 �C under a N2 flow of
620 mL/min for 30 min to partially clean the surface
oxides formed by exposure of the char to air during
handling. The reactor was then cooled down to the
reaction temperature, 270 �C; and the N2 was switched
to the reaction mixture: NO, NO/H2O, NO/O2 or NO/
H2O/O2, maintaining the same flow of 620 mL/min. The
gas concentrations used in the experiments were: NO,2000 ppm; O2, 5%; balance N2. For the reactions with
H2O, the gas mixture was passed through a water bub-
bler held at 60 �C (PVH2O ¼ 150 mmHg). The conduc-
tion line from the bubbler until the reactor entrance was
kept at 80 �C. At the reactor exit, a vapor trap was
placed to collect the nitric acid formed during the
reaction, the concentration was followed by the varia-
tion of the pH of the solution thus formed. After leavingthis trap, the product gases passed through a second
cold trap kept at )5 �C to condense water which could
interfere with the gas detectors, Fisher–Rosemoun
NDIR/UV gas analysers, BINOS-100 for CO and CO2,
BINOS-1004 for NO and NO2 and BINOS 1001 for O2.
After 2 h of reaction, the reactor was cooled under N2
flow to room temperature. After this, the quartz tube
with the sample under N2 was taken to the XPS foranalysis. The apparatus used was a VG-Microtech
Multilab Electron spectrometer with a Mg Ka (15 kV,
20 mA). The C 1s 284.6 eV value was taken as reference
for the binding energy.
In order to obtain a reference point for comparison of
the results, the unreacted char was heat treated at 700 �Cfor 30 min in N2 and then the surface complexes were
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P. Garc�ıa et al. / Carbon 42 (2004) 1507–1515 1509
characterized by XPS as described above. The formation
of oxygen complexes was also followed by temperature
programmed desorption (TPD). For this purpose, each
reaction was repeated and then the sample thus pro-duced was heat treated under N2 atmosphere at 10�/min
up to 900 �C. The evolved gases (NO, NO2, CO and
CO2) were monitored with the gas detectors.
2.2. Computational details
A molecular modeling study of the reactions which
could explain the N-complexes formation under our
reaction conditions was carried out. Calculations were
done in order to obtain thermodynamic information
that fits the experimental data. A finite cluster of a single
graphene layer, shown in Fig. 2, represented our charmodel. The edge atoms on the upper side of the model
are unsaturated to simulate active sites while the other
edge carbon atoms are terminated with hydrogen atoms.
It has been shown that the use of H to terminate the
boundaries of finite graphite models is a good choice
[22]. A five six-member rings model was selected since
previous research has shown that carbon chemisorption
properties depended more strongly on the local structureof the active site than on the size of the graphene layer
used for the simulation [22–24]. In order to study the
proposed reactions, each structure of the reactants,
intermediates and products was fully optimized. All
models were optimized in their electronic ground state.
This was achieved by performing single-point energy
calculations at the same level of theory for several
electronic states of a given species; the ground state ta-ken as the one with the lowest energy. Furthermore,
frequency calculations were done in order to confirm
their stability. All calculations (energies, optimizations,
and frequencies) were carried out at B3LYP density
functional theory level (DFT), using the 6-31G(d) basis
set. In a previous study, it was shown that with this level
of theory spin contamination is small for carbonaceous
models [25]. All calculations were done using theGaussian 98 program [26].
H
H
H
HH
H
H
H
Fig. 2. Char model used to simulate the NO adsorption. Carbon
atoms without hydrogen represent active sites.
3. Results and discussion
The dissociative chemisorption of NO is an important
step during its reduction to N2 on a carbon surface [4–6].Therefore, the identification of nitrogen complexes
formed during the reaction can help understand the
reduction mechanism. The amount of active sites capa-
ble of forming N-complexes can be increased if the
gasification of the solid takes place [4,8,27–29]. If gasi-
fication does not occur, some of the active sites remain
blocked by oxygen complexes [8,30]. In order to select
the reaction temperature, preliminary experiments underisothermal conditions between 200 and 400 �C were
carried out. At 270 �C we observed gasification of the
char during reaction with NO/O2. However, we did not
observe any gasification in the reaction with NO alone.
Such a difference was the principal criterion to select 270
�C as the reaction temperature.
Cleaning of the surface by the in situ heat treatment
of the sample generates active sites that facilitate theformation of surface complexes during the NO–char
reaction. This procedure was particularly important in
the case of the reactions with NO and NO/H2O where
no gasification takes place at 270 �C.
3.1. Nitrogen complexes formation
Fig. 3 shows the XPS N1s spectra of the char after
partial cleaning of surface oxides at 700 �C in N2
atmosphere (Fig. 3(A)), and after reaction with NO
(Fig. 3(B)), NO/O2 (Fig. 3(C)), NO/H2O (Fig. 3(D)),
and NO/H2O/O2 (Fig. 3(E)). The y-axis is the same for
all figures. In general, all the spectra show similarcomplexes but in different proportions depending on the
reaction mixture. In order to make them comparable,
the signal intensities should be normalized with regard
to the corresponding area below the C 1s signal. C 1s
spectra are not presented here. The area ratios are cor-
rected by the atomic sensitivity factor [15].
The samples were introduced into the XPS chamber
under a high flow of He to partially prevent oxidation byair. The oxygen to carbon ratio observed in the cleaned
char was O/C¼ 670 · 10�4 which is lower than the one
present in the untreated char (O/C¼ 1450 · 10�4).
Therefore, since before each reaction all the samples
were thermally treated under similar conditions, the
char identified in Fig. 3(A) was named initial char and
was taken as reference to establish the relative changes
in nitrogen and oxygen complexes.Fig. 3(B)–(E) show substantial differences when
compared to the spectrum of the initial char (Fig. 3(A)).
The effects of the reaction mixtures on the nitrogen
complexes are presented as their comparative incre-
ments in Fig. 4. The values of the y-axis (in arbitrary
units) correspond to the subtraction of the N-complex/C
ratio of the initial char from the corresponding ratio of
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395 400 405 410
N-Q
N-6
N-5
N-X
E
395 400 405 410
A
N-6
N-5
N-Q
N-X
Initial char
395 400 405 410
BN-6
N-5
N-X
N-Q
-NO2
-NO2
-NO2
-NO2
N-5
395 400 405 410
C
N-6
N-XN-Q
N-5
395 400 405 410
DN-6
N-X
N-Q
N-5
Fig. 3. Deconvoluted XPS data of nitrogen complexes on char. (A) Surfaces complexes remaining after thermal treatment at 700 �C. Surfacecomplexes formed on the char surface after reaction at 270 �C with (B) NO, (C) NO/O2, (D) NO/H2O, (E) NO/H2O/O2.
N-Q -NO2 N-5 N-X N-6
(arb
itrar
y un
its)
NONO/H2ONO/O2NO/H2O/O2
[N-c
ompl
exes
/C]
∆
pyridones-No
Fig. 4. Variation of the surface nitrogen complexes obtained from the
XPS data referred to the initial char.
1510 P. Garc�ıa et al. / Carbon 42 (2004) 1507–1515
the char after reaction. The x-axis shows the complexes
which experienced changes in their concentrations.
Fig. 4 shows that after reaction the most significant
increments were in the N-6 complexes and the smallest
variations were in the N-Q complexes. The reaction
mixture had a noticeable effect on the magnitude of thechanges and this effect was observed in the nitrogen
complexes. In general, the reaction in NO/H2O gave the
smallest variations, suggesting that at 270 �C water can
compete for the same active sites on the carbon surface
where the NO can react. This can be seen as a partial
inhibition of the NO reaction as will be discussed below
in the analysis of the effect of the reaction mixture in the
formation of nitrogen complexes.–NO2 complexes formation. The presence of –NO2
complexes on the carbon surface (Fig. 3(B)–(E)) even in
experiments with mixtures without O2, indicates that
these complexes can be formed by NO chemisorption on
adjacent sites to oxygen complexes. It is important to
mention here that stable oxygen complexes like semi-
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Table 1
Desorbed species up to 900 �C by TPD under N2 before reaction in
NO, NO/H2O, NO/O2 or NO/H2O/O2; heating rate: 10 �C/min
Reaction
mixture
Complexes desorbed by TPD (lmol/gC)
NO NO2 CO CO2
NO 5 – 300 165
NO/H2O – – 500 220
NO/O2 20 – 690 720
NO/H2O/O2 20 – 1150 890
P. Garc�ıa et al. / Carbon 42 (2004) 1507–1515 1511
quinone (complex a in R1) have been suggested to form
in the NO–char reaction, even at low temperatures [30–
32]. In experiments carried out at 100 �C [19], an
important increment was observed in –NO2 complexes.
These complexes, however, decreased by about 70%
after reaction at 270 �C showing that they are very la-
bile.
The thermal instability of –NO2 coincides with thedrastic reduction of reversible NO chemisorption when
the reaction temperature was increased to 270 �C. Forexample, while the reversible NO chemisorption was
between 80 and 170 lmol/gC after the reaction at 100
�C [19], the maximum amount at 270 �C was 20 lmol/
gC (see Table 1).
The formation of –NO2 (complex c) can be explained
by reaction R1. Our theoretical calculations show thatthe chemisorption of NO on an active site located be-
tween two semiquinone complexes is an exothermic
process. The energy released is sufficient to favor the
endothermic rearrangement to produce the –NO2
(complex c).
H
H
HHH
H
H
H
O O
H
H
HHH
H
H
H
O ONO
H
H
HHH
H
H
H
O ON
O
∆E = -145 kJ/mola b
NO
∆E = 98 kJ/mol c
ðR1Þ
Theoretical calculations done by Zhu et al. [9] show
similar tendency, although different energy values, per-
haps due to the use of different levels of theory in their
calculations. Zhu et al. [9] reported that a complex like c
does not lead to the cleavage of N–O bond of the
originally chemisorbed NO molecule. Rather these
complexes are able to desorb again as NO by heating, in
accordance with steps c, b and a in R1. They also foundthat the oxygen complexes, like semiquinones, make the
NO chemisorption in the Ndown position more favorable
than the molecular oxygen chemisorption on the same
structure [9]. Therefore, NO molecules can compete for
the char active sites in the presence of high concentra-
tions of molecular oxygen and therefore they can be
preferentially chemisorbed on oxidized surfaces.
Another possibility for the formation of the –NO2
complex is the reaction between NO2 formed in the
gaseous phase (reaction R2) with the carbon surface.
This reaction takes place at low temperatures and can becatalyzed by the char surface [9,33–35] as was observed
in some of our blank experiments.
2NOþO2 ! 2NO2 ðR2Þ
The reaction of NO2 with organic compounds has been
observed [36]. In the case of carbon surfaces, NO2 can
be chemisorbed forming surface complexes through the
sequence presented in R3. In fact, NO2 is reduced to NO
by carbon [37] probably after a chemisorption step.
Theoretical calculations show that reaction R3 is ther-
modynamically favorable with an exothermicity of 360kJ/mol. Experimentally, a large increase of –NO2 com-
plexes on char after reaction in mixtures of NO with
oxygen (Fig. 4) was observed. Reaction R3 shows one of
the mechanisms that could account for the –NO2 com-
plexes formation.
H
H
HHH
H
H
H
OH
H
HHH
H
H
H
ON
OO
H
H
HHH
H
H
H
O ON
O
∆E = -279 kJ/mol
NO2
c∆E = -81 kJ/mol
d e
ðR3ÞN-5, pyridones or nitro complex formation. The N1s
bonding energy at 400.2 eV can be assigned to pyrrolic
(N-5 complexes) [7,13,15], pyridones [17] and nitrocomplexes (–NO) [17,38] (Fig. 1(B)–(D)). The most
important increment in this group of complexes was
observed after the reaction with NO/H2O/O2 (Fig. 4),
where the gasification tendency was the highest,
according to the amount of CO and CO2 evolved in the
TPD (Table 1). As the O2 concentration in both NO/O2
and in NO/H2O/O2 mixtures was the same (5%), an
equal degree of char oxidation can be expected. How-ever, this was not the case as can be seen in Table 1. The
largest char oxidation observed in the latter mixture can
be associated with the formation of HNO3 (R4 reac-
tion). The low pH value of the condensed vapor at the
exit of the reactor (a pH¼ 2 for the reaction with char
sample and a pH¼ 5 for a blank experiment using only
quartz wool) was evidence for the reaction in NO/H2O/
O2. Since the formation of the acid requires the previousformation of NO2 (R2 reaction), it is assumed that in
this mixture NO2 is also present and therefore the fol-
lowing reacting systems can take place.
4NO2 þ 2H2OþO2 ! 4HNO3 ðR4Þ
2HNO3 þ C ! H2OþNOþNO2 þ CO2 ðR5Þ
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1512 P. Garc�ıa et al. / Carbon 42 (2004) 1507–1515
NO2 and the nitric acid decompose on the char surface
forming oxygenated complexes accompanied by simul-
taneous gasification of the solid (R5 reaction)
[7,37,39,40]. These reactions could explain the highestincrement of oxygenated complexes after the reaction in
NO/H2O/O2 (Table 1). Such results show the synergistic
effect when NO, O2 and H2O are present in the reaction
at low temperatures (R5 reaction).
Since char gasification was more pronounced in NO/
H2O/O2, we would have an increase in the possibility of
nitrogen complexes formation [8] such as that observed
in the increments of the N-5 group and N-6 (Fig. 4). Thehighest increment in the N-5 group in this mixture could
be associated with the pyridones formation, preceded by
N-6 (the N-6 formation will be presented later). Some of
the N-6 complexes could be oxidized forming pyridones,
considering that in the strongest oxidant mixture the
H2O could contribute with OH group to its formation.
Pyridine-N-oxide formation. Results in Figs. 3 and 4
show that there is a significant increment in the pro-duction of N-X complex particularly in the case of the
reaction with NO alone. When other gases are present in
the gas mixture, the N-X is drastically reduced. In
reactions where gasification was not observed, the
nitrogen incorporation on carbon structures can take
place on the active sites generated during the thermal
treatment of the char [8,41]. The work of Montoya et al.
[42,43] has shown that the energy barrier for COdesorption from complexes like f and for NO desorption
from complexes like h (reaction R6) are similar (�350
and �330 kJ/mol, respectively). It has been proposed
that these desorptions produce a five-member ring
(structure g in R6) [42,44,45]. The five-member ring
structure thus generated is a susceptible site where the
NO molecule can be chemisorbed at low temperatures to
give the N-oxide complex. Here we propose that thepyridine-N-oxide (N-X complex) formation at 270 �Coccurs in sites left by CO desorption during the thermal
treatment at 700 �C as presented in reaction R6. Addi-
tionally, the theoretical calculations results show that
this is a process with an exothermic heat of )143 kJ/mol,
which indicates that this reaction is thermodynamically
feasible. Therefore, reaction R6 can be used to explain
the N-oxide complexes formation with and withoutgasification during the carbon–NO reaction.
H
H
HHH
H
H
H
OH
H
HHH
H
H
H
NH
H
HHH
H
H
H
O
gf∆E = 151 kJ/mol
-CO700 °C
NOT>100 °C
∆E = -143 kJ/molh
ðR6ÞThe drastic reduction in the proportion of N-X (Fig.
4) when O2 and H2O are present in the reaction mixture
suggests the existence of possible competing reactions
for the same carbon active sites that could lead to the
formation of pyridine N-oxides complexes.
NH
H
HHH
H
H
H
C OO
O
NH
H
HHH
H
H
O
∆E = -364 kJ/mol
CO2
∆E = -14 kJ/mol
i j
NH
H
HHH
H
H
H
O
OONH
H
HHH
H
H
H
O
-CO2
DE = -14 kJ/mol kl
ðR7Þ
NH
H
HHH
H
H
H
O
NH
H
HHH
H
H
H
NH
H
HHH
H
H
H
∆E = -256 kJ/mol
NO
∆E = -10.5 kJ/mol
CO+ CO2
+ NO2m
n
n
ðR9Þ
N-pyridine formation. Pyridine ring, or N-6 com-
plexes, had the most important increment after reaction
at 270 �C in mixtures with O2 and water (Fig. 4). These
were 45% and 85% higher with NO/O2 and NO/H2O/O2
respectively, than the increments observed in the same
reaction system at 100 �C [19]. In the mixtures without
oxygen, the increments in N-6 were similar to the values
observed at lower temperatures [19]. This suggests thatthe small amount of char gasification promoted by O2 at
this temperature enhances the incorporation of pyridinic
nitrogen as observed by other researchers in reactions
with NO at high temperatures [7]. Here we propose three
reaction mechanisms, R7–R9, that can lead to the for-
mation of a pyridine ring. All of them have the pyridine
N-oxide as the starting complex.
ðR8Þ
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0
50
100
150
200
250
NO NO+H2O NO+O2 NO+H2O+O2
∆(O
/C)x
103
Fig. 5. Variation of the surface oxygen concentration incremental as
determined by XPS after reaction with different gas mixtures at 270 �Creferred to the initial char.
P. Garc�ıa et al. / Carbon 42 (2004) 1507–1515 1513
Reaction R7 is based on the adsorption of a CO2
molecule, produced during gasification, in two active sites
next to a pyridine-N oxide complex to produce a lactone
group. Lactones have been reported to be produced byreadsorption of CO2 (complex j) [44,46]. The CO2
adsorption energy on the nitrogen containing model used
here has an exothermicity of )364 kJ/mol. The lactone in
complex j can be converted into a new lactone (complex k)
through an exothermic process of )14 kJ/mol. This lac-
tone group should be more labile and therefore should
desorb as CO2 in a process with an exothermicity of )14kJ/mol. Step j-k-l in R7 form a possible reaction path dueto the characteristics of the N–O bond, which is a single
bond with a negative charge on the oxygen atom. The net
reaction would appear as a 1–3 migration of the oxygen
atom of the N-oxide complex. Since reaction R8 requires
the presence of CO, it should be more likely to take place
at high temperatures where gasification is relevant and
the CO concentration is large. However, in the low tem-
perature regime, for the carbon–nitric oxide reaction,small amounts of CO have been reported to desorb at
temperatures as low as 250 �C [30]. The CO thus pro-
duced can promote the production of pyridine rings from
the pyridine N-oxide complexes. Reaction R9 is the other
plausible route for the production of the pyridine ring
which will give NO2 as one of the products.
Formation of quaternary nitrogen. The variations in
N-Q complexes (Fig. 4) were too small to establish anycorrelation with the reaction gas mixture. The slight
variations could be associated with weak interactions of
some N-pyridine with oxygen complexes [7,13,16].
3.2. Variations in the surface char oxygen complexes
Fig. 5 shows the oxygen increments according to the
XPS analysis. The data are presented as changes re-ferred to the initial char. The y-axis values correspond to
the subtraction between the O/C ratio of the initial char
and the corresponding ratio of the char after the reac-
tion with the different gas mixtures. In all cases, oxygen
increments were one to two orders of magnitude higher
than those of nitrogen. Note that in the case of the
reaction with only NO, this effect is due to the fact that
the NO molecule is dissociatively chemisorbed formingN2 and/or N2O. A similar effect was observed at 100 �C[19]. The scheme presented in R10 has been proposed to
explain the N2 formation [10].
H
H
H
HH
H
H
NO
H
H
H
HH
H
H
NO ON
H
H
H
HH
H
H
O O
NO - N2
o p q
ðR10Þ
The N–O bond of the first chemisorbed molecule splits
and facilitates the chemisorption of other NO molecule
forming the complex p. Then, the complex p dissociates
to give N2 [10]. An alternative mechanism was proposed
by Teng and Suuberg [30] to explain the large incre-
ments of C(O) over C(N) complexes and the evolution
of N2 at low temperatures. This mechanism involves theformation of NO dimers, complex r. Reaction R11 im-
plies the simultaneous formation of molecular nitrogen
and formation of oxygen bonds on the carbon surface
[30,31].
OO N N OO N2
r s
ðR11Þ
The population of CO and CO2 precursors on the car-
bon surface after the NO/H2O reaction is higher than
that obtained in the reaction with just NO as can be seen
in the TPD data (Table 1). This result implies that the
H2O molecules may be able to oxidize a wider number
of active sites. Nevertheless, the XPS analyses show
oxygen increments higher after reaction in NO than inthe NO/H2O reaction (Fig. 5). The apparent discrepancy
between these results is related to the characteristics of
these analyses. The XPS can analyze only the most
external surface while the TPD analysis involves data
from the external surface as well as from the inner pore
surface. As the largest area is inside the pores, the TPD
data suggest that water might be reacting preferentially
inside the pore network of the char particle. ReactionR12 [46] can explain the fact that the oxygen increment
observed by XPS (Fig. 5) in the reaction with NO/H2O
was lower than that in the NO reaction. The decom-
position of the chemisorbed H2O can neutralize active
sites with hydrogen atoms. Such an effect partly explains
the inhibition observed in the nitrogen complexes
increments after reaction in NO/H2O (Fig. 4).
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1514 P. Garc�ıa et al. / Carbon 42 (2004) 1507–1515
H
H
H
HH
H
H
O
H
H OH
H
H
H
HH
H
H
H O
H
H
H
HH
H
H
H H
t u v
ðR12ÞThe surface oxygen increase observed by XPS after the
reaction with NO/O2 (Fig. 5) is an unexpected result for
which we do not have a clear explanation. In the inves-tigation of the nature of carbon-oxygen complexes by
Hall et al. [47] using different oxidizing agents, it was
found that the O2–carbon reaction takes place mainly
inside the pore structure of the carbon particle while the
NO–carbon reaction is restricted to the external surface
area. These results can partly explain our findings.
However, the information collected here is not sufficient
to explain the reason for the apparent inhibition of thesurface NO–carbon reaction in the reaction of NO and O2
with carbon surface, as can be observed in Fig. 5. In the
case of the reaction inNO/H2O/O2 the large proportion of
surface oxygen is probably due to the effect of the nitric
acid, a strong oxidizing agent, formed during the reaction.
4. Conclusions
The reactions of coal char with NO at 270 �C forms
stable nitrogen and oxygen complexes on the char sur-face. The presence of O2 and H2O in the reacting mix-
ture affects the formation of these complexes. Water
inhibits the formation of nitrogen complexes through
neutralization of active sites with hydrogen atoms. In
the mixtures with O2, there is gasification of the solid
carbon and this facilitates the nitrogen incorporation
into the solid matrix, mainly as N-pyridinic. The dif-
ference in the gasification effect by NO/O2 and NO/H2O/O2 mixtures is associated with NO2 formation in the first
case, and additionally, HNO3 formation in the latter
case. Theoretical calculations show that five member
ring structures are susceptible to chemisorb NO giving
pyridine-N-oxide at temperatures where gasification is
not relevant. These complexes can be transformed into
N-pyridine in a reaction that can be assisted by CO, CO2
or NO. –NO2 complexes can be formed by NO chemi-sorption on adjacent sites to oxygen complexes or by
chemisorption of NO2 present in the gas mixtures that
contain oxygen. These complexes are responsible for the
NO reversible desorption.
Acknowledgements
The authors would like to acknowledge the financial
support from Colciencias and the University of Antio-
quia, project 1115-05-11504, the University of Antio-
quia, project IN-5216CE, and the University of Alicante
project PPQ2002-01025. P. Garc�ıa wishes to thank the
University of Antioquia and the University of Alicantefor her visiting scholarship.
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