Reaction Balance of Thermal and Catalytic Decomposition of Nitrogen-Based Ionic Monopropellant
Transcript of Reaction Balance of Thermal and Catalytic Decomposition of Nitrogen-Based Ionic Monopropellant
Reaction balance of thermal and catalytic
decomposition of nitrogen-based ionic
monopropellants
K. Farhat*, Y. Batonneau, C. Kappenstein
LACCO, Université de Poitiers (France)
And M. Ford
ESA-ESTEC, Keplerlaan, 2200 AG Noordwijk ZH, the NetherlandsESA-ESTEC, Keplerlaan, 2200 AG Noordwijk ZH, the Netherlands
� INTRODUCTION
• Energetic ionic liquids
• Previous results at LACCO
� EXPERIMENTAL PART
• HAN preparations and characterization
• Flow reactor
OUTLINE
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• Flow reactor
�RESULTS
• HAN – thermal and catalytic decomposition
• ADN - thermal and catalytic decomposition
• AN - thermal and catalytic decomposition
� CONCLUSIONS / PERSPECTIVES
Introduction Experimental Part Results Conclusions/Perspectives
Energetic ionic liquids (oxidizer + fuel + solvent)
Oxidizer Oxygen balance Formula Density /g.cm-3 Solubility, 20°°°°C
HAN 33.3 % [NH3OH]+[NO3]
- 1.84 95 %
ADN 25.8 % [NH4]+[N(NO2)2]
- 1.81 78 %
AN 20.0 % [NH4]+[NO3]
- 1.73 56 %
HNF 13.1 % [N2H5]+[C(NO2)3]
- 1.91 53 %
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HNF 13.1 % [N2H5]+[C(NO2)3]
- 1.91 53 %
HN 8.4 % [N2H5]+[NO3]
- 1.69 -
• Support resistant at high temperature (1400 °C)
• Active phase���� propellant decomposition at low temperature
• Good selectivity in thermodynamic products
fuel association appropriate catalyst
Introduction Experimental Part Results Conclusions/Perspectives
Previous Results at LACCO
DTA-TGABatch Reactor
Best catalyst:Pt/Al2O3Si – active at room temperature
R. Eloirdi, L. Courteoux, D. Amariei,
thesis, University of Poitiers, 2001, 2004, 2006
- fast exothermic decomposition
- pressure increase lower than expected for thermodynamic products:
HAN-water decomposition:
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thermodynamic products:
NH3OHNO3(aq) = O2(g) + N2(g) + 2 H2O(l)
These methods are unable to determine the nature of decomposition products
need to establish the mass balance of the decomposition of HAN-water solutions
Introduction Experimental Part Results Conclusions/Perspectives
NH2OH (aq) + HNO3 (aq) � [NH3OH]+[NO3]-(59wt.-%) (aq)
HAN synthesis
Evaporation
87 wt-% HAN
10
12
HNO3 65%
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2
4
6
8
0 5 10 15 20 25 30 35
pHVolume de HNO3 (mL)
NH2OH 50%
T < 4 °C
Ice
pH
stirrer
Introduction Experimental Part Results Conclusions/Perspectives
HAN characterization
- Acid-base titration - RAMAN spectroscopy
1.5 104
2 104
2.5 104
3 104
1051
Inte
nsit
y / u
.a
8
10
12
14
NO3-
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0
5000
1 104
1.5 104
0 500 1000 1500 2000 2500 3000 3500 4000
720
1012
31472992
27161417
1606
1183 3488
Raman shift / cm -1 In
tens
ity
/ u.a
2
4
6
8
0 5 10 15 20 25
pH
Volume (NaOH 1 mol/L) / mL
NH3OH+
N-OH
NO3-
Introduction Experimental Part Results Conclusions/Perspectives
Analysis of the decomposition products: flow reactor
OvenThermocouple
Vector gas flow
controller
Electronic flow controller
He vector gas
Pressure gauge
Quartz reactor
Septum or gascalibration
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Identification of gaseous decomposition products: N2, O2, NO, N2O, NO2
Y. Batonneau, L. Courthéoux, P. Esteves, L. Pirault-Roy, S. Rossignol, C. Kappenstein, N. Pillet, AIAA Papers, (2004) 3835.
Mass spectrometer (MS) (gas products)Extractor
He vector gas
Silica column cold trap ( RAMAN spectroscopy and acid-base titration)
Introduction Experimental Part Results Conclusions/Perspectives
Analysis of the decomposition products: flow reactor
Catalyst mass: 160 mg
Propellant volume: 100 µµµµL Reactor pre-heated at a given T
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Catalyst used during this study:Pt/Al2O3Si –powder (laboratory)
essentially Developed for HAN decomposition
Introduction Experimental Part Results Conclusions/Perspectives
HAN – Thermal decomposition at 220 °C
4
6
8
10
12
14
Gas
per
cent
age
/ %
N2
N2ON O
2*100O
2*10
N O
Gaseous decomposition products (MS results)
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0
2
4
200 300 400 500 600 700 800 900
Gas
per
cent
age
/ %
T im e / s
222
Experimental estimationN2 : NO : N2O = 3 : 1 : 1
���� PRIMARYN2 (major) NO (medium)NO2(traces)
O2 (traces) – air impurities
���� SECONDARYN2O (medium)NO2 (traces)
Rel
ativ
e in
tens
ity
Trapped solution
RAMAN spectroscopy
Introduction Experimental Part Results Conclusions/Perspectives
HAN (87 wt.-%) – Thermal decomposition at 220 °C
NO3- (1050 cm-1)
N-OH (1012 cm-1)
NO3- (720 cm-1)
Analysis of trapped productsAcid-base titration
6
8
10
12
14
pH
H+
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Raman shift / cm-1
HAN 86.6 wt.-%
Trapped solution
HNO3 39 wt.-%
0
2
4
0 2 4 6 8 10Volume (NaOH 1 mol/L) / mL
�Total HAN decomposition:- Absence of the peak at 1012 cm-1 in collected solution- One acid-base equivalent point
Same results for catalytic decomposition
� The collected solution contains
nitric acid ( HNO3 , 42 wt.-%).
�Molar ratio HNO3 / HANdec ~ 0.4 to 0.5
Formation of primary N2 and NO: redox reaction between [NH3OH]+ and NO3
- ions
6 NH3OHNO3(aq) = 3 N2(g) + 2 NO(g) + 10 H2O(g) + 4 HNO3(g) (1)
6 NH3OHNO3(aq) = 2 N2(g) + 2 NH4NO3(s) + 6 H2O(g) + 4 HNO3(g) (2)
HAN – Thermal and catalytic decomposition –Proposal for the reaction balance
N2 excess and NH4NO3 formation: disproportionation reaction of [NH3OH]+ cation
Introduction Experimental Part Results Conclusions/Perspectives
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Decomposition of NH4NO3: formation of N2O
2 NH4NO3(s) = 2 N2O(g) + 4 H2O(g) (3)
���� Complete balanced equation - linear combination: (1) + 1.5x(4)
15 NH3OHNO3(aq) = 6 N2(g) + 2 NO(g) + 3 N2O(g) + 25 H2O(g) + 10 HNO3(g)
6 NH3OHNO3(aq) = 2 N2(g) + 2 N2O(s) + 10 H2O(g) + 4 HNO3(g) (4)
Combining equations (2) and (3)
Introduction Experimental Part Results Conclusions/Perspectives
Gaseous decomposition products
10
15
20
Gas
per
cent
age
/ %
N2
NO*10
ADN (50 wt.-%)– Thermal decomposition at 320 °C
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0
5
1000 1100 1200 1300 1400 1500 1600 1700 1800
Gas
per
cent
age
/ %
Time / s
N2O
NO2*100O
2*10
���� PRIMARYN2 (major) O2 (traces) – air
impurities
���� SECONDARYN2O (medium)NO2 (traces)NO (traces)
8
10
12
pH
Introduction Experimental Part Results Conclusions/Perspectives
ADN (50 wt.-%)– Thermal decomposition at 320 °CAnalysis of trapped products
NH4+
Collected solution
Reactor walls solidRel
ativ
e in
tens
ity NO2
- (828 cm -1)NO2
- (1330 cm -1)
NO3- (720 cm -1)
NO3- (1048 cm -1)
Acid-base titrationRAMAN spectroscopy
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4
6
0 0.5 1 1.5Volume (NaOH 1 mol/L) / mLVolume (NaOH 1 mol/L) / mL
Reactor walls solid
AN solid
ADN solid
Rel
ativ
e in
tens
ity
Raman shift / cm-1
� Total ADN decomposition
2 NH4N(NO2)2 (aq) ���� NH4NO3(aq) + 2 N2(g) +N2O(g) + 2 H2O(l) + O2(g)
� The collected solution contains ammonium nitrate
Introduction Experimental Part Results Conclusions/Perspectives
Gaseous decomposition products
ADN (50 wt.-%)– Catalytic decomposition at 250 °C
10
15
20
Gas
per
cent
age
/ %
N2
O2 NO*10
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�Decomposition in 2 steps:
0
5
1000 1200 1400 1600 1800 2000
Gas
per
cent
age
/ %
Time / s
N2O
NO2*100
�Second: major products: N2, N2O, NO and NO2
�First: major products: N2 and O2
Rel
ativ
e in
tens
ity
Collected solution
Introduction Experimental Part Results Conclusions/Perspectives
ADN (50 wt.-%)– Catalytic decomposition at 250 °CAnalysis of trapped products
8
10
12
pH
NH4+
NO3- (720 cm -1)
NO3- (1048 cm -1)NO2
- (1330 cm -1)
NO2- (828 cm -1)
RAMAN spectroscopy Acid-base titration
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Rel
ativ
e in
tens
ity
Raman shift / cm-1
Collected solution
AN solid
ADN solid
HNO3 39 wt.-%
0
2
4
6
0 0.5 1 1.5 2 2.5 3Volume (NaOH 1 mol/L) / mL
H+
�The collected solution contains: NH4+, H+, NO3
- and NO2-
ADN – Thermal and catalytic decomposition –Proposal for reaction balance
Introduction Experimental Part Results Conclusions/Perspectives
5
10
15
20
Gas
per
cent
age
/ %
N2
NO2*100
O2 NO*10
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NH4N(NO2)2 (aq) ���� 2N2(g) + 2H2O(g) + O2(g)
6NH4N(NO2)2 (aq) ���� 4N2(g) + 3H2O(g) + 3N2O(g) + 4NH4NO3(g) + 2HNO3(g)
0
5
1000 1200 1400 1600 1800 2000
Gas
per
cent
age
/ %
Time / s
N2O
NO2*100
NH4NO3 ����N2O(g) + 2 H2O(g)
NH4NO3 ����NH3(g) + HNO3(g)
0.4
0.6
0.8
1
Gas
per
cent
age
/ % N2
N2O
NO *100
Introduction Experimental Part Results Conclusions/Perspectives
AN (56 wt.-%)– Thermal decomposition at 450 °C
8
10
12
14
pH
Acid-base titration of trapped solution Gaseous decomposition products
NH4+
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0
0.2
0.4
3200 3300 3400 3500 3600 3700 3800 3900 4000
Gas
per
cent
age
/ %
Time / s
NO2*100
O2*10 NO*10
4
6
8
0 2 4 6 8 10Volume (NaOH 1 mol/L) / mL
Very slight decomposition of NH4NO3 in these conditions
NH4NO3(l,s)���� NH3(g) + HNO3(g) ���� NH4NO3(g) ���� NH4NO3(l) ���� NH4NO3(s)
Introduction Experimental Part Results Conclusions/Perspectives
AN (56 wt.-%)– Catalytic decomposition at 320 °C
10
15
20
25
Gas
per
cent
age
/ %
N2
N2O*10O
2*10
NO*10
Analysis of trapped products Gaseous decomposition products
Presence of characteristic vibrations peaks of NO3
-
RAMAN spectroscopy:
Acid-base titration
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0
5
1500 1600 1700 1800 1900 2000 2100 2200
Gas
per
cent
age
/ %
Time / s
2NO
2*100
NH4NO3(l,s)���� NH3(g) + HNO3(g) ���� NH4NO3(g) ���� NH4NO3(l) ���� NH4NO3(s)
Partiel AN decomposition
The trapped solution contains NH4
+
NH4NO3 ����N2(g) + 2 H2O(l) + 0.5 O2(g)
NH4NO3 ����N2O(g) + 2 H2O(l)
Introduction Experimental Part Results Conclusions/Perspectives
Conclusions
1) Thermal and catalytic decomposition of HAN - water mixtures
� primary products: major N2 and HNO3, medium NO
� secondary products: medium N2O and traces NO2
2) Thermal decomposition of ADN - water mixtures
� primary products: major N2 and NH4NO3
� secondary products: medium N2O and NO, traces NO2
3) Catalytic decomposition of ADN - water mixtures
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3) Catalytic decomposition of ADN - water mixtures
Decomposition in 2 steps:
� First: primary products: major N2 and O2
� Second: primary products: major N2 and HNO3
secondary products: medium N2O, medium NO and traces NO2
4) No thermal decomposition of AN-water mixtures
5) Catalytic decomposition of AN - water mixtures
�primary products: major N2 and medium NO
�secondary products: medium N2O and traces NO2
Introduction Experimental Part Results Conclusions/Perspectives
� Find an adequate catalyst to decompose selectively HAN-water mixture in thermodynamic products
� Find a good catalyst to decompose ADN-water mixture in one step (first step)
Perspectives
HEM – Arcachon, October, 1-3, 2007 20/21
� Decomposition study of ammonium nitrate
� Thermal and catalytic decomposition study of HNF and HN