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Testing of Reaction Mechanisms for the Combustion of NH3/H2 Mixtures Using a Large Amount of Experimental Data

Authors:

Abstract

Introduction Ammonia (NH3) is a promising carbon-free fuel because it can be used in a sustainable and recyclable loop for energy production. It is often blended with other fuels in practical applications. One of the most often used co-fuels is hydrogen (H2). Accurate chemical kinetic models are needed that can describe the combustion of fuel mixtures containing NH3 under typical conditions of industrial applications. In this work, we compare the performance of 18 reaction mechanisms against a large amount of experimental data on the combustion of neat NH3 and NH3/H2 fuel mixtures. This work is an extension of our previous work on the same combustion system (Szanthoffer et al., Appl. Energ. Combust. Sci. 14 (2023) 100127.).
András Gy. Szanthoffer*, István Gy. Zsély, László Kawka, Máté Papp, Tamás Turányi
Testing of Reaction Mechanisms
for the Combustion of NH3/H2Mixtures
Using a Large Amount of Experimental Data
Introduction
Ammonia (NH3) is a promising carbon-free
fuel because it can be used in a sustainable and
recyclable loop for energy production.
It is often blended with other fuels in practical
applications. One of the most often used co-fuels
is hydrogen (H2).
Accurate chemical kinetic models are needed
that can describe the combustion of fuel mixtures
containing NH3under typical conditions of
industrial applications.
In this work we compare the performance of 18
reaction mechanisms against a large amount
of experimental data on the combustion of
neat NH3and NH3/H2fuel mixtures.
This work is an extension of our previous work on
the same combustion system [1].
Acknowledgments
This work was supported by
NKFIH grant OTKA K132109
of the Hungarian National
Research, Development and
Innovation Office.
References
Institute of Chemistry, ELTE Eötvös Loránd University, Budapest, Hungary
Experimental data and simulations
Experimental data were utilized from
46 publications from the literature:
Reaction mechanisms investigated Visual mechanism comparison
Exp. typea
XML/Ds./Dp.b
T/ K p/ atm φ
ST-IDTc41/41/315
1023
2489
1.01
41.65
0.50
2.07
JSRd44/153/2348 5001452
1.00
1.40
0.01
1.50
FRe23/87/1125 4511973
1.00
98.69
0.00
2.44
LBVf
188/188/3329
295584g
0.50
36.58
0.40
2.00
Overall:
296/469/7117
a: Type of experiment
b: Number of XML data files/data series/data points
c: Shock tube ignition delay time measurements
d: Concentration measurements in jet stirred reactors
e: Concentration measurements in flow reactors
f: Laminar burning velocity measurements
g: Cold side temperatures of the flames Quantitative mechanism comparison Results, discussion, conclusions
Experimental data were encoded in
ReSpecTh Kinetics Data (RKD)
version 2.4 format XML files [2].
1
Program Optima++ [3] read the XML data
file, set up the simulation environment, and
called OpenSMOKE++ [4] simulation code
to carry out the simulations.
2
All simulations were carried out with
OpenSMOKE++ [4] using a
0D (ST-IDT, JSR, FR) or 1D (LBV) models.
3
Error function
Quantitative assessment of
mechanism performance was based on the
evaluation of an error function:
N
: number of data series
Nf
: number of XML data files
Nfs
: number of data series in the f-th XML data file
Nfsd
: number of data points in the s-th data series of the f-th XML data file

:fsd-th experimental result

:fsd-th simulation result

 : standard deviation of 

E
= 9 3
error on average
Mechanism ID
Species Reactions Ref.
Mathieu
-2015 33 160 [7]
Otomo
-2018 32 213 [8]
Li
-2019 34 252 [9]
POLIMI
-2020 31 203 [10]
Han
-2020 32 163 [11]
KAUST
-2021 34 262 [12]
Konnov
-2021 36 298 [13]
Dai
-2021 33 211 [14]
Bertolino
-2021 31 203 [15]
CEU
-2022 32 140 [16]
Sun
-2022 36 229 [17]
Tang
-2022 33 211 [18]
Shrestha
-2022 33 270 [19]
Zhou
-2023 33 233 [20]
Glarborg
-2023 34 228 [21]
POLIMI
-2023 31 205 [22]
KAUST
-2023 32 243 [23]
Shrestha
-2023 34 283 [24]
[1] A. Gy. Szanthoffer et al., Appl. Energ. Combust. Sci. 14 (2023) 100127.
[2] T. Varga et al., ReSpecTh Kinetics Data Format Specification v2.4, 2022.
http://ReSpecTh.hu/
[3] M. Papp et al., Optima++. http://ReSpecTh.hu
[4] The CRECK Modeling Group (POLIMI), OpenSMOKE++.
https://www.opensmokepp.polimi.it/
[5] T. Nagy, T. Turányi, ECM 2021,1415 April, Naples, Italy. Paper 336.
[6] K. N. Osipova et al., Fuel 310 (2022) 122202.
[7] O. Mathieu and E. L. Petersen, Combust. Flame 162 (2015) 554570.
[8] J. Otomo et al., Int. J. Hydrog. Energy 43 (2018) 30043014.
[9] R. Li et al., Fuel 257 (2019) 116059.
[10]A. Stagni et al., React. Chem. Eng. 5 (2020) 696711.
[11] X. Han et al., Combust. Flame 213 (2020) 113.
[12] X. Zhang et al., Combust. Flame 234 (2021) 111653.
[13] X. Han et al., Combust. Flame 228 (2021) 1328.
[14]L. Dai et al., Combust. Flame 227 (2021) 120134.
[15] A. Bertolino et al., Combust. Flame 229 (2021) 111366.
[16] S. Wang et al., Combust. Flame 236 (2022) 111788.
[17] Z. Sun et al., Combust. Flame 243 (2022) 112015.
[18] R. Tang et al., Combust. Flame 240 (2022) 112007.
[19]K. P. Shrestha et al., Fuel Comm. 10 (2022) 100051.
[20] S. Zhou et al., Combust. Flame 248 (2023) 112536.
[21]P. Marshall and P. Glarborg, J. Phys. Chem. A 127 (2023) 26012607.
[22]A. Stagni et al., Proc. Combust. Inst. (2022)
[23] X. Zhang et al., Fuel 341 (2023) 127676.
[24] M. V. Manna et al., Proc. Combust. Inst. (2022)
[25] X. Han et al., Combust. Flame 206 (2019) 214226.
[26] V. J. Wargadalam et al., Combust. Flame 120 (2000) 465478.
A quantitative indicator is more useful
to assess the performance of mechanisms
on a large collection of experimental data.
ST-IDT measurement by Mathieu et al. [7] LBV measurement by Han et al. [25]
JSR measurement by Zhang et al. [12] FR measurement by Wargadalam et al. [26]
Mechanism ID
EST-IDT EJSR EFR ELBV
KAUST
-2023 17.7 48.4 19.4 14.1 24.9
POLIMI
-2020 9.8 53.8 23.4 14.3 25.3
Bertolino
-
2021
7.8 56.2 22.7 15.0 25.4
KAUST
-2021 21.3 48.6 18.2 14.9 25.7
POLIMI
-2023 10.4 55.4 23.7 14.2 25.9
Tang
-2022 6.6 44.8 23.5 32.0 26.8
Han
-2020 4.7 64.0 27.6 14.8 27.8
Otomo
-2018 6.5 54.9 25.9 24.0 27.8
Konnov
-2021 6.7 67.6 27.6 15.9 29.5
CEU
-2022 6.7 65.2 31.6 15.0 29.6
Mathieu
-2015 7.7 58.5 22.3 31.2 29.9
Sun
-2022 17.3 51.3 21.6 29.4 29.9
Li
-2019 11.9 63.0 31.4 19.3 31.4
Shrestha
-
2022
18.3 62.1 24.4 25.2 32.5
Shrestha
-
2023
16.1 48.0 34.0 33.6 32.9
Glarborg
-
2023
11.6 58.1 26.4 41.6 34.4
Dai
-2021 14.1 48.2 21.7 65.8 37.5
Zhou
-2023 67.8 59.0 28.3 13.5 42.1
E:
< 9
<
16
<
25
<
36
<
49
< 64
Estimation of the standard deviation of experimental data
To estimate 
 , both the uncertainty reported by
the experimenters (
exp,
fsd
)and the estimated statistical
scatter of the fs-th data series (
fit,
fs
) were considered:
fit,
fs
was obtained by fitting a trendline (spline or
polynomial function) to the data points of the fs-th dataset
using the code Minimal Spline Fit [5]. Experimental data: Osipova et al. [6]
* Email address:
andras.gyorgy.szanthoffer@ttk.elte.hu





 




  
 
  
 

 

Averaged Evalues
Comparison of the mechanisms by
computing their averaged Evalues for each
type of experiment and overall.
Smaller Evalue
better mechanism performance.
The performance of a mechanism changes
significantly with the type of experiment.
Distribution of Efsd values
Comparison of the mechanisms based on the
distribution of the 



 values
stacked bar plot.
More data points within the 3σlimits (Efsd < 9) →
better mechanism performance.
Conclusions
The best-performing mechanisms are
almost the same in both cases.
The performances of the investigated models are
very different.
None of the models has Eaverage value smaller than 9
further mechanism development is necessary!
ResearchGate has not been able to resolve any citations for this publication.
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One of the most important problems of modern energy industry is the transition to carbon free fuels, which can mitigate the negative environmental effects. This paper presents experimental data on ammonia and ammonia/hydrogen blends oxidation in an isothermal jet-stirred reactor over the temperature of range 800–1300 K. Experiments were performed under atmospheric pressure, residence time of 1 s, various equivalence ratios, and with argon dilution at ≈0.99. It was revealed that hydrogen addition shifts the onset temperature of ammonia oxidation by about 250 K towards the lower region. A detailed chemical kinetic model which showed the best predictive capability was used to understand the effect of hydrogen addition on ammonia reactivity. It was shown that hydrogen presence results into higher concentrations of H, O and OH radicals. Moreover, these radicals start to form at lower temperatures when hydrogen is present. However, the change of the equivalence ratio has only slight effect on the temperature range of ammonia conversion.
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Autoignition delay times of ammonia/dimethyl ether (NH3/DME) mixtures were measured in a rapid compression machine with DME fractions of 0, 2 and 5 and 100% in the fuel. The measurements were performed at equivalence ratios φ=0.5, 1.0 and 2.0 and pressures in the range 10–70 bar; depending on the fuel composition, the temperatures after compression varied from 610 K to 1180 K. Admixture of DME is seen to have a dramatic effect on the ignition delay time, effectively shifting the curves of ignition delay vs. temperature to lower temperatures, up to ~250 K compared to pure ammonia. Two-stage ignition is observed at φ=1.0 and 2.0 with 2% and 5% DME in the fuel, despite the pressure being higher than that at which pure DME shows two-stage ignition. At φ=0.5, a reproducible pre-ignition pressure rise is observed for both DME fractions, which is not observed in the pure fuel components. A novel NH3/DME mechanism was developed, including modifications in the NH3 subset and addition of the NH2+CH3OCH3 reaction, with rate coefficients calculated from ab initio theory. Simulations faithfully reproduce the observed pre-ignition pressure rise. While the mechanism also exhibits two-stage ignition for NH3/DME mixtures, both qualitative and quantitative improvement is recommended. The overall ignition delay times for ammonia/DME mixtures are predicted well, generally being within 50% of the experimental values, although reduced performance is observed for pure ammonia at φ=2.0. Simulating the ignition process, we observe that the DME is oxidized much more rapidly than ammonia. Analysis of the mechanism indicates that this ‘early DME oxidation’ generates reactive species that initiate the oxidation of ammonia, which in turn begins heat release that raises the temperature and accelerates the oxidation process towards ignition. The reaction path analysis shows that the low-temperature chain-branching reactions of DME are important in the early oxidation of the fuel, while the sensitivity analysis indicates that several reactions in the oxidation of DME, including cross reactions between DME and NH3 species presented here, are critical to ignition, even at fractions of 2% DME in the fuel.
  • A Gy
  • Szanthoffer
A. Gy. Szanthoffer et al., Appl. Energ. Combust. Sci. 14 (2023) 100127.
  • O Mathieu
  • E L Petersen
O. Mathieu and E. L. Petersen, Combust. Flame 162 (2015) 554-570.
  • J Otomo
J. Otomo et al., Int. J. Hydrog. Energy 43 (2018) 3004-3014.
  • R Li
R. Li et al., Fuel 257 (2019) 116059.
  • A Stagni
A. Stagni et al., React. Chem. Eng. 5 (2020) 696-711.
  • X Han
X. Han et al., Combust. Flame 213 (2020) 1-13.
  • X Zhang
X. Zhang et al., Combust. Flame 234 (2021) 111653.