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This is the accepted version of:
F. Maggi, S. Dossi, C. Paravan, L.T. De Luca, M. Liljedahl
Activated Aluminum Powders for Space Propulsion
Powder Technology, Vol. 270, 2015, p. 46-52
doi:10.1016/j.powtec.2014.09.048
The final publication is available at
https://doi.org/10.1016/j.powtec.2014.09.048
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© 2015. This manuscript version is made available under the CC-BY-NC-ND 4.0 license
FilippoMaggi a,1,
∗
,Stefano Dossi a,1 , Christian Paravan a,1 , LuigiT. DeLu a a,1 , Mattias Liljedahl b,2 aPolite ni o diMilano, 34,viaLaMasa,20156 Milan, Italy b
SwedishDefen eResear h Agen y,FOI, SE-14725Tumba,Sweden
Abstra t
Aluminum powders are ommonly used in solid propellants to enhan e the
performan e of spa e propulsion systems. During ombustion, a fra tion of
the fuel metal parti les, whi h emerge from the bulk, tends to merge into
aggregates. These stru tures eventually leave the ombustion surfa e in the
shapeofpartiallymoltenagglomerateswhi h anrea hthesizeofhundredsof
mi rons. These ondensed ombustionprodu ts partakeinnozzleexpansion
andhinderthedeliveredspe i impulseofthero ketunit. Theenhan ement
of original parti le rea tivity improves ombustion quality and may redu e
sensibly agglomerate size and relevant losses.
More rea tive aluminum fuel an be obtained by a tivation of
mi ron-sized powders, without resorting to the use of nano-metals. One of the
methods onsists of a hemi al treatment with a pro essing solution whi h
alters the standard oxide layer at the surfa e of the parti les. Su h
modi- ations grant lowerignition temperatureand faster propellantburningrates
∗
Correspondingauthor,Tel. +390223998287
Email addresses: filippo.maggipolimi.it(FilippoMaggi),
stefano.dossimail.polimi.it(StefanoDossi), hristian.paravanpolimi.it
(ChristianParavan),luigi.delu apolimi.it(Luigi T.DeLu a),
mattias.liljedahlfoi.se(MattiasLiljedahl) 1
Department of Aerospa e S ien e and Te hnology, Spa e Propulsion Laboratory
(SPLab) 2
rea tion.
The present paper ompares the features of three bat hes of aluminum
parti les whi h were treated with uorine-based a tivating solutions of
dif-ferent on entration. The bat hes were supplied in the frame of HISP FP7
European Proje t. The hara terization fo used on physi al, hemi al and
thermalproperties,lookingattherea tivity ofthe samplesand atthe
alter-ations introdu ed by the hemi al pro essing. Finally, a tivated aluminum
bat hes were tested inlab-s alepropellants,monitoring the variationof
bal-listi properties with respe t toa referen e formulation.
Keywords: aluminum parti les, hemi ala tivation, rea tivity, solid
propellant,metal fuel
Nomen lature
A ronyms
BET Brunauer-Emmett-Teller
DTA Dierentialthermal analysis
ESD Ele tro Stati Dis harge
FCC fa e- entered ubi
SEM S anning ele tron mi ros opy
TGA Thermalgravimetri analysis
TMD Theoreti al mean density
XPS X-ray photoele tron
spe -tros opy XRD X-ray dira tion Greek symbols
α
Degree of transformation∆x
Variation of xρ
Density,g/cm
3
Roman symbolsC
AlA tive metal fra tion
D
4,3
Mass-mean diameterm
Mass, kgSubs ripts and supers ripts
in Initial ondition
zK Ref. to the temperature of z
Kelvin
1. Introdu tion
Gravimetri and volumetri spe i impulseofsolidro ketmotors anbe
enhan ed by using energeti additives [13℄. Among the others, Aluminum
hasbeenadopted insolidspa epropulsionforde ades,intheshapeof
mi ro-metri metal powders, thanks to its appealing energeti ontent (30 kJ/g),
stability intime, non-toxi ity, and relatively low ost. Typi alparti le sizes
range from 5to 50mi rons[4, 5℄.
Afra tion of themetal embeddedin apropellant tendstoaggregate and
agglomerate during ombustion. Drops of molten aluminum with an oxide
ap leave the burning surfa e [6, 7℄. These ondensed ombustion produ ts
generate a multiphase ow whi h expands through the nozzle. Performan e
losses are the order of 2-5% of the ideal spe i impulse, depending on size
and amount of the parti ulate [8, 9℄. In this respe t, the improvement of
metal fuel ignition and ombustion is envisaged in order to obtain ner
ag-glomerates, or noagglomerationatall [3,10℄.
Aluminumparti lesare overed by anaturaloxide layer, assoonasthey
get in onta t with oxygen- ontaining environments. This passivation shell
represents a strong shield against further degradation by the atmospheri
oxygen. At the same time, it represents an obsta le to rea tivity. Under
burning onditions, ignitiono urswhen the passivating aluminashell fails,
enabling fast oxidation of the metal ore. The melting temperature of the
par-as 1300 Kwere re orded in presen e of some kindsof a tive media (namely,
ombustionprodu tsinsidero ket oreow)[11℄. Ignitiontemperatureis
be-low900-1000K,fornanometri powders. Parti lestakeadvantage ofsample
spe i surfa e and a tive oating layers, if any [12℄.
Literature data agree on the fa t that the use of nanometri parti les
inpropellantsimprovesignitionand ombustionproperties, preventing from
largeagglomerates[1315℄. However,theredu tionofparti lesizeintrodu es
somedrawba ks. Therelativeamountofaluminumoxidewithrespe ttothe
total parti le mass an be ome relevant in the nanometri range, sin e the
thi kness of the oxide layer (about 2.5-3 nm) does not s ale with parti le
size [16℄. The onsequentredu tionof thea tivemetal ontentdepresses the
available oxidation enthalpy and, in turn, propulsion performan e (namely,
ideal spe i impulse). Moreover, mixing and asting of a propellant
on-taining nanometri ingredients may represent a te hnologi al issue due to
high vis osity, redu ed pot life, ESD (Ele tro Stati Dis harge) and impa t
hazards aswell as ost of the manufa tured ompound [17℄.
Spe i a tivation pro esses an be performed on metal parti les to
im-prove ignition and ombustion properties, without de reasing the diameter
tothesub-mi rometri range. Me hani alballmilling, oatingwithproperly
hosen metals, or hemi al weakening of the external oxide layer represent
some examples. Me hani al milling operates amodi ationof parti le
mor-phology by high-energy impa t with pro essing spheres. Synthesis of
amor-phouspowders,stru ture hange,produ tionofmetal- erami s,orin lusions
of rea tants (metal oxides or uorides) an be a hieved [1821℄. Coating of
parti les through deposition of metals an improve ignitionand ombustion
ride a ts assolventfor alumina,lowering the meltingpointof the prote tive
aluminumoxidelayeraswellasa eleratingthediusionof gaseousoxidizer
towards the metal ore [25, 26℄.
Thepresentpaperfo usesontheee tsprodu edbya hemi ala tivation
pro ess. Aluminum powder treated with three dierent a tivating solutions
of varying on entrations are onsidered. Physi al, hemi al, and thermal
hara terizations, typi ally applied to nanometri powders, are performed
to evaluate rea tivity and nal quality of the material[13, 27℄. Comparison
withoriginalnon-treatedmi ron-sizedAlaswellaswithsomerepresentative
literature data for nanoaluminum and mi roaluminum is arried out.
Com-bustionanalysisofsolidpropellantsamples ontaininga tivatedpowdersare
presented.
2. Experimental
Three bat hes of a tivated aluminum powders (A-Al01, A-Al02 and
A-Al03)havebeenprodu ed, followingapro eduresimilartotheonedes ribed
by Hahma[25,28℄. Theinitialaluminumwas ValimetH3powder(bat h
07-8002). The produ er rated 99.0% of minimum metal ontent and parti le
size of 4.5
µ
m [29℄. The a tivation pro ess was a omplished by auorine-basedsolution,whose on entrationwasvariedtomodifythestrength ofthe
treatment. The bat h A-Al01 was assumed as referen e for the pro essed
family. The on entration of the solution was the half for A-Al02 and 1.5
timesforA-Al03. Powderpro essingwas ondu tedatFOI(SwedishDefen e
Resear h Agen y), aspartof the HISP(HighPerforman e SolidPropellants
for In-Spa e Propulsion) FP7 proje t.
s ans. Dierent omposite solid ro ket propellants were ompounded and
their ballisti properties were experimentallytested. Moreover, the
ontra -tion of ideal performan e, followingthe depletion of metalli aluminum
dur-ing a tivation, was monitored by means of thermo hemi al analysis [30℄.
2.1. Physi al hara terization
SEM mi rographs, reported in Figure 1, show a omparison between
Valimet H3 and all a tivated bat hes. Parti les appear mainly spheri al.
The external surfa e is smooth for the original powders and rough for the
pro essed ones. The a tivated parti lesalsofeature some irregulardeposits,
notpresentintheoriginalmaterial,whosesizeseemstofollowthe
on entra-tionofthea tivatingsolution. Namely,thespots overingtheA-Al03surfa e
rea h the size of about 100 nm, whereas smallerdimensions are observed in
the other ases. A pre ise estimation is di ulttosupply.
[Figure1 about here.℄
Parti lesizewasmeasuredbymeansofaMalvernMastersizer 2000using
airdispersion withS iro o dryunit. Mass-meandiameter
D
4,3
,span of thedistribution, and evaluation for the spe i surfa e, derived from geometri
onsiderations, are reported in Table 1. Valimet H3 and a tivated powders
do not demonstrateappre iable dieren es. All parti leshave a omparable
mass-weighted diameterranging between 5.1 and 5.5
µ
m and similardistri-bution shape and relevant span. For all a tivated powders, mean parti le
diameter grows few hundreds of nanometers. Representative distribution
Table1: Parametersforphysi al parti le hara terization. LiteraturedataofALEX and ASD-4are reportedforreferen e. Spe i
surfa eareasderivefrombothBETmethodandparti lesize analysis.
Id. H3 (baseline) A-Al01 A-Al02 A-Al03 ALEX
TM a
ASD-4 b
A tivatingsolution relative on entration 0 1.0 0.5 1.5 -
-D4,3, µm
5.1 5.5 5.4 5.5 0.1 9.0Span 1.78 1.66 1.68 1.64 -
-Spe i surfa e area,
m
2
/g
(BET) 1.2 2.6 2.2 3.3 11.8 0.38
Spe i surfa e area,
m
2
/g
(parti lesize) 2.5 2.1 2.1 2.0 - -a Ref.[31℄ b 7ner than 1
µ
m diameter, presumably lost during the hemi al pro ess, isobserved.
[Figure2 about here.℄
A more representative evaluation of the powder spe i surfa e is
a - omplished using the BET te hnique [33℄. The estimation is based on the
quantityofadsorbed inertgasonthesurfa eofasample. Theresultdepends
onboth geometri aspe t of the parti lesand onthe pe uliaritiesof the
sur-fa e (namely,roughness) [35℄. A ording toBarret, parti le hara terization
isa omplishedwhensize,shapeandnishareaddressed[36℄. Bouwmanand
o-authorsstressonthefa tthatsurfa eroughnessandshapearedi ultto
denesin etheir distin tionderives,ingeneral,from onsiderationson
har-a teristi dimensions whi h, in turn, depend on the observation s ale [37℄.
In this respe t, the spe i surfa e measurement using the BET te hnique
is a ondensed and omprehensive value, whi h in ludes all ontributions.
This kind of analysis has been adopted in the past to hara terize ne and
ultra-ne metal powders, alsoforenergeti purposes. The measurementwas
onsidered a reliableindex of rea tivity [10, 34℄.
The resultingtrendamongthe testedbat hes is orrelated with the
on- entration of the a tivating solution. The spe i surfa e from BET
analy-sis is in remented by the a tivation pro ess. The referen e A-Al01 doubles
the spe i surfa e, if ompared to the original H3 supply. A-Al02 features
the lowest BET improvement while A-Al03 has the highest value,
respe -tively less-than-double and almost three times the value of H3 bat h. Laser
granulometry assessed that the mean diameter of the parti les was almost
un hanged by the hemi al pro essing so the variation of spe i surfa e is
attributed to porosity in rement. These results are in agreement with SEM
The quanti ation of the metalli aluminum in the powder, after the
hemi al pro essing,is performed by hydrolysis. The moles ofH
2
developedby samples,on e in onta t with water, are monitored in time till
stabiliza-tion is obtained. A solution of NaOH (10% on entration by mass) is used
to dissolve the external oxide shell and fa ilitate the pro ess. Following a
standard volumetri method[38℄, the assumed stoi hiometri rea tionis
Al + 3 H
2
O → Al(OH)
3
+ (3/2)H
2
↑
+
heat (1)The moles of rea ted metal fromthe evolved hydrogen an be determined.
This hemi ala tivationpro ess hastheunwel omeee t todepletepart
of the aluminum from the powder. The metal ontent of the initialpowder
bat h was quantied in more than 98%. Tests on a tivated samplesshowed
a onsistent ontra tion of the Al ontent. The de rement was only in part
dependent on the on entration of the a tivating solution. For the powder
whi hunderwentthestrongesta tivation(A-Al03),only90%ofparti lemass
was estimated tobea tivealuminum. For A-Al01 and A-Al02, the fra tion
was around 93%.
X-ray analyses were alsoperformed onthe samples. Forall the powders,
XRD identiedthe presen eof aluminum only,infa e- entered ubi (FCC)
rystalline form,regardless of the a tivation. The dira tionpatternfor the
A-Al01sampleis reported inFigure3. The resultindi atesthatthe
super- ial hemi al treatment did not generate dete table quantities of rystalline
ompounds. The sampleswere furtheranalyzed withXPS, foridenti ation
of surfa e elemental omposition. Dierent atomi spe ies were introdu ed
by the a tivation pro ess, su h as uorine, present with a 13.0% atomi
17.0% and oxygen 58.0%.
[Figure3 about here.℄
2.3. Thermogravimetri analysis
The ee ts of enhan ed parti le rea tivity on intensive oxidation onset
and other related parameters were analyzed by means of TGA/DTA in air
atambientpressure. S answereperformedon10mgsampleswith10K/min
heatingrate,up to1273K(1000
◦
C).As representatives, the s ansof A-Al01
and of H3 baseline are reported in Figure 4, using the same s ales on the
axesfor immediate omparison. Overallresultsare reportedinTable 2. The
DTA tra e of A-Al01 shows an oxidation peak, overlapped to the melting
of the aluminum ore, in proximity of 933 K. The rea tion is forerun by an
initial exothermi release. From the analysis of peak positions for dierent
a tivated materials, it appears that stronger a tivation does not anti ipate
the oxidation onset towards lower temperatures. The baseline H3 powder
did notshowproofsoffastoxidationinthe samerangeoftemperature. This
behavior is in line with past experimental ndings, available in the open
literature. The ignition of standard mi rometri powders is size-dependent
and, for therange of interest,fast oxidationis expe tedto o ur above1273
K (1000
◦
C). [39℄.
The degree of transformation
α
an be quantied via TGA data. Thevalue of
α
represents the fra tion of the a tual aluminum ontent in theini-tialsamplemass
m
inwhi hturnedintoitsoxide. Themeasureisbasedonthe
re orded massin rement
∆m
TGAand onthe initiala tivemetalfra tion
C
Alof therespe tivebat h,quantiedwiththe volumetri methoddes ribed
onversion of Al into
Al
2
O
3
is assumed.α (Al → Al
2
O
3
) =
∆m
TGA0.889
1
m
inC
Al (2)In onsiderationof TGAresults,the degreeof transformationwas evaluated
at three referen e temperatures and, namely,
α
933K
at 933 K for aluminummelting,
α
973K
at973 K on e the Al meltingpeak isover, andα
1273K
at thenals anningtemperature1273K.A orrelationbetweena tivationstrength
and degreeof metaloxidation was missingeven though a generalin rement
of the oxidized fra tion was observed at the end of the test for a tivated
powders.
When DTA/TGA tra es for A-Al01 and H3 are ompared (see Figure
4), a dierent rate of weight in rement and, as onsequen e, of oxidation
an be observed. The H3 sample progressively in reased its mass during
the whole TGA s an. Rather, A-Al01 showed an abrupt in rement during
the exothermi peak, indi atinga fast oxidation rea tion. However, most of
the metal-oxide onversion o urred while thealuminum ore wasalready in
liquidstate, meaningthat metal onsumptionatparti leignitionwasrather
limited.
[Figure4 about here.℄
2.4. Appli ation in propellants
The inuen e of powder a tivation on solid propellant properties was
assessed. Four aluminized formulations based on AP oxidizer and HTPB
binderwere produ ed, using dierent bat hes of metalfuel. The same
Table2: Parameters for hemi alandthermalparti le hara terization. ALEX andASD-4properties,available fromtheliterature,
arereportedfor omparison.
Id. H3 (baseline) A-Al01 A-Al02 A-Al03 ALEX
TM a
ASD-4 b
A tivemetal, % 98.3
±
0.7 93.9±
0.9 93.7±
0.5 90.5±
0.5 89 98.5DTA oxidationpeak,K N.A.
934 K 943 K 939 K 876 1093 (onset)
∆m
TGA at1273 K,% +39 +41 +52 +54 + 66-α
933K
, % 8 4 6 5 - 2.5α973K
, % 15 25 17 12 --α
1273K
,% 44 49 62 67 82 41 a Ref.[31℄ b Ref.[32℄ 12derswhilethebaselineformulation ontainedtherawH3non-a tivatedmetal
fuel. The hara terizationa tivity onsistedofthemeasurementofbulk
den-sity, porosity,and relevant ballisti data redu tion.
[Table 1 about here.℄
Propellantdensity
ρ
p
wasassessed by means of buoyan y te hnique. Itsdif-feren e
∆ρ
p
fromthe orrespondingideal value(mainly duetoporosity)wasevaluated using the formula
∆ρ
p
= (ρ
p
−
ρ
id
) /ρ
T M D
. Propellantombus-tion tests were arried out in a losed ombustion hamber, equipped with
automati pressure ontrol system, in a range between 5 to 40 bar.
Burn-ingratewasassessed throughopti alte hniqueusing theSPLab proprietary
software Hydra. The ensembleof resultsisreportedinTable 4while graphi
omparison of burningrate urves is available in Figure5.
[Figure5 about here.℄
[Table 2 about here.℄
Theuse ofa tivated metalfuelsimproved ballisti propertieswithout
in-trodu ing pe uliar issues for propellant ompoundingand uring. Low level
porosity wasdete ted. The presen e of the a tivation layer did not intera t
with uring pro esses or generated internal bubbling, at the mixing
tem-perature of 36
◦
C. These observations are in line with binder-fuel vis osity
analyses re entlypublished bythe sameresear hgroup[41℄. For ombustion
tests,anin reaseofburningrateintheorderofabout
+20%
,withrespe t tothe original non-a tivated powders, was observed. The in rement was
irre-spe tive of the typeof a tivation. Onlyminor dieren es were found among
data andrelevantttingsare reportedinFigure5. The urvesforP-A-Al01,
P-A-Al02, and P-A-Al03 are overlapped, suggesting that the dierent
on- entrationlevelsofthe a tivating solution,tested inthis framework,did not
modify the ombustion behaviorof the propellants.
3. Dis ussion
Theimprovementof parti lerea tivityafterthe hemi ala tivation
pro- ess is registered by both the in rement of the spe i surfa e area (visible
from BET analysis) and by the redu tion of parti le ignition temperature
below1273 K(observed inTGA/DTA tra es). The improvementof the
for-mer rea tivityparameteris ausedby thegenerationofsuper ialroughness
and is partially responsible of earlier parti le ignition. However, the latter
benets also from oxide layer weakening. It is not possible to weight the
dierent ontributions, so far. In this respe t, BET analysis re ords
par-tiallythe signi ant role of the a tivating solutionand the knowledge of the
ignition temperature supplements the hara terization.
Thea tivationpro ess ausedonlyasurfa e modi ation ofthe raw
ma-terial. XRD dira tionpatterns did not reveal any in-depth modi ation of
the rystalline stru ture, being the ore stillaluminum. XPS dataidentied
several atomi spe ies, laid by the hemi al pro essing on a thin super ial
layer.
It was veried that the amount of the a tive metal ontent was redu ed
even down to 90%. This latter aspe t be omes ru ial from a propulsion
pointof view. The enhan ement of powder rea tivity is performed with the
purpose to redu e metal agglomeration during ombustion and alleviate a
mounts the potentialgain for a better ombustion and more e ient nozzle
expansion. A quanti ationof su h ee t is reported inFigure6. The ideal
spe i impulse for the referen e propellant formulation, reported in Table
3,is omputedthroughthermo hemistry[40℄. Expe ted ontra tionisabout
1-2%, depending on a tivation strength and depleted metal. The redu tion
of two-phase owlosses annotbeassessed in this ontext ,nevertheless the
performan e detriment is quantied in the open literature as 3-5%. That
is, the improvement delivered by hemi al a tivation of aluminum may be
omparabletothenegativeee t ausedby the ontra tionofthe aluminum
ontent. Carefulevaluationof formulationingredients isenvisaged.
[Figure6 about here.℄
TheTGA/DTA s ans withlowheatingrate inoxidizing atmosphere(air
inthe present ase)indi atethe improvementofrea tivityfor a tivated
alu-minum parti lesathigh temperature. Exothermi peaksare obtained about
themeltingpointofaluminum. Atthesametimesampleweightin rementis
promptly re orded. Su h events are not visible for unpro essed H3 powder,
in agreement with the literature. Available data suggestthat fast oxidation
rateshouldbea hieved beyond1273K(experimentallimitofthispaper),for
unpro essed powders having similar size and shape. In general, aluminum
parti leignition,under ombustion onditions, istriggered bythe disruption
of the oxide layer. This event o urs after the melting of the oxide shell
(around 2300 K) for the mi rometri range, or is aused by the expansion
of the parti le bulk for the nanometri size [39℄. In this ase, the
exother-mi peak and the onsequent fast oxidation rate from DTA/TGA s ans are
overlapped with the melting of the aluminum. It is possible that the oxide
the powder whi hdid not grant enoughspe i surfa e area.
A tivated aluminum powders result in intermediate properties, globally
ranking their rea tivity above omparable mi ron-sized aluminum, though
still far from nano-sized parti les. Tables 1 and 2 report some relevant
lit-erature data, along with results from the present paper. ALEX TM
refers
to a nominally 100 nm aluminum produ ed by ele tri al explosion of wire
(EEW). ASD-4isami rometri Russianprodu t, omparabletoH3[31,32℄.
Bothpowdersarenaturallypassivatedbyairandare ommer iallyavailable.
A tivated aluminum stillhave lower initialoxide ontent than the referen e
nanoaluminumbut loses5-8% ofmetalwith respe t tothe initialingredient.
Resultingideal spe i impulsedata arereported inFigure6. The
tempera-turesof therst oxidationpeakforthe A-Alfamily,dete tedbyDTA/TGA,
are signi antly lower with respe t to the behavior of mi rometri ASD-4
sample and approa h the features of the nanometri ALEX TM
powder. The
degree of metal-oxide onversion atthe end of the TGA s an in rementsfor
samplestreatedwith stronger powder a tivationandis intherange 50-70%.
Similarly, spe i surfa e area (BET analysis) is in remented with respe t
to ASD-4 and H3, but the value is still 5 to 10 times lower than ALEX TM
.
The burningrate analysis onrms ageneral
+20%
,aftermetalfuelpro ess-ing. The reader should note that the benet is ve times less than the one
obtained by using anALEX TM
nano-sized aluminum [10℄.
Finally, experimental ndings suggest that only minor dieren es exist
among the a tivated powders fromthe rea tivity viewpoint. TheBET
anal-ysis identied about
±0.5m
2
/g
variationof spe i surfa e area among the
lots, whi h is rather limited for sensible reper ussions. Similar assessments
lants are very similar. The result is more meaningful if we onsider that
heatingratesdierfromea hotherinmagnitude (10K/minforDTA/TGA,
and above 1000 K/s for propellant ombustion).
4. Con lusions
Chemi al a tivation of metal parti les is a te hnique that fosters
rea -tivity. The pro ess is able to enhan e ignition apability and in rement the
spe i surfa e area through a solutionof varying on entration. Both
mor-phology and hemi al omposition of the external surfa e are modied by
the hemi al treatment, resulting in in reased roughness and enri hed with
uorine-based ompounds. The metalli ore is unaltered, but a onsistent
aluminum depletion redu es the a tive metal ontent of about 5-7%, for
tested ases.
For the tested lots, the a tivation a omplished a general in rement of
parti le rea tivity. The spe i surfa e area was more than doubled and
DTA/TGA oxidation peak was anti ipated at the melting of the aluminum
ore. However, the degree of metal-oxide onversion at ignition was slow.
Most of the oxidation o urred at higher temperatures. Also the ballisti
hara terization onrmedthein rementedrea tivity. Uniformimprovement
of the burning rate was observed for all lots, showing negligible dieren es
among tested a tivation strengths.
Ingeneral,powderpropertiesobtained after hemi altreatmentare
simi-lartotherea tivityparametersofner uts,butarestillfarfromthebehavior
of nano-sized ingredients. In rement in burning rate an be obtained when
these advan edfuelsare usedinenergeti materials. Alsoredu tionofmetal
investiga-the depletion of the a tive metal ontent, whi h is a dire t onsequen e of
the treatment.
5. A knowledgements
The authors a knowledge the nan ial support of the European FP7
Proje tHISP (Highperforman e solid propellants for In-Spa ePropulsion),
Grant Agreement No. 262099. The authors wish tore ognize and
a knowl-edgethesigni ant ontributionoftheResear hCenterforNonConventional
Energy, EniDonegani Institute (Novara, Italy).
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1 SEM of virgin and a tivated aluminum powders.
Magni a-tion: 15,000x. . . 26
2 Granulometri distributionobtainedbylasers atteringof
sam-ples H3 and A-Al01. . . 27
3 XRD spe trum of A-Al01 powder. Aluminum onlyis dete ted. 28
4 TGA/DTAanalysisinairofH3andA-Al01powders. Sample
weight 10mg, temperatureramp 10K/min. . . 29
5 Steadyburningratevs. pressureofpropellantsembedding
a -tivated aluminum. Baseline formulation is in luded for
om-parison. . . 30
6 Ideal spe i impulse for the formulation reported in Table
3. Computations are performed under the assumptions of 70
bar ombustion pressure, expansion ratio of 40, dis harge in
( ) A-Al02 (d)A-Al03
(b)ValimetH3
Figure 4: TGA/DTA analysis in airof H3and A-Al01 powders. Sample weight10 mg,
1
10
100
Pressure, p
c
, bar
1
10
Burning rate, r
b
, mm/s
P-Valimet
P-A-Al01
P-A-Al02
P-A-Al03
Figure5: Steadyburningratevs. pressureofpropellantsembeddinga tivatedaluminum.
are performed under theassumptions of 70 bar ombustion pressure,expansion ratioof
1 Parameters for physi al parti le hara terization. Literature
data of ALEX
TM
and ASD-4 are reported for referen e.
Spe- i surfa e areas derivefrombothBET methodand parti le
size analysis. . . 7
2 Parametersfor hemi alandthermalparti le hara terization.
ALEX TM
and ASD-4properties,availablefromtheliterature,
are reported for omparison. . . 12
3 Nominalpropellant ompositionforballisti analysis(
ρ
T M D
=
1.761g/cm
3
). Mixingwasperformedat36
◦
C; atin-based
ur-ing atalyst was used.. . . 33
4 Details of propellant hara terization. Un ertainty was
Table 3: Nominal propellant omposition for ballisti analysis (
ρ
T MD
= 1
.761g/cm
3
).
Mixingwasperformedat36
◦
C;atin-based uring atalystwasused.
Ingredient Mass fra tion Notes
AmmoniumPer hlorate 58% Coarse: 200
µ
mnominalAmmoniumPer hlorate 10% Fine: 10
µ
m nominalMetal fuel 18% Aluminum: standard ora tivated
onden e level. Propellant Powder