Cold compaction of iron powders—relations between powder morphology and mechanical properties
Transcript of Cold compaction of iron powders—relations between powder morphology and mechanical properties
Cold compaction of iron powders—relations between powder
morphology and mechanical properties
Part I: Powder preparation and compaction
D. Poquillon*, J. Lemaitre, V. Baco-Carles, Ph. Tailhades, J. Lacaze
CIRIMAT, UMR CNRS/UPS/INPT 5085, ENSIACET, 31077 Toulouse, France
Received 1 May 2001; received in revised form 1 January 2002; accepted 30 January 2002
Abstract
The effect of morphology of iron powders on their compaction behaviour has been studied in the case of compacts with a final relative
density below 0.8. Two powders, one with spherical grains and the other with spongy grains, have been synthetized in order to prepare green
compacts under pressures ranging from 100 to 350 MPa. The compaction behaviour of both powders has been experimentally described by
the relation between the applied compaction pressure and the relative density of the material. Different stages have been identified at
increasing compaction pressure: (i) fully elastic behaviour (Stage I), (ii) particle sliding (Stage II), (iii) particle irreversible deformation (Stage
III). Spongy powder-based compacts achieved greater density at the same compaction pressure than spherical powder-based compacts.
Models are proposed to describe the compaction behaviour of both powders. D 2002 Elsevier Science B.V. All rights reserved.
Keywords: Iron powder; Compaction; Particles morphology; Oxalate precursor; Compaction model
1. Introduction
Powder metallurgy (PM) is a highly developed method
of manufacturing reliable ferrous and non-ferrous parts. The
PM process is cost-effective because it minimises machin-
ing, produces good surface finish and maintains close
dimensional tolerances. Generally, the PM-forming process
includes cold compaction, sintering and finishing. The
successful compaction of the powder is the first step of
the process, which is also the last one in the case of green
compacts. The compacted part combines high porosity (20–
35%) and reasonable strength. This porosity can be a means
to lower structural weight in aeronautical applications (e.g.
shape magnets for sensors and motors) or to create oil-
retaining bearings, which are often referred to as self-
lubricant bearings.
Mechanical properties of materials prepared with such a
process are strongly influenced by the characteristics of the
powder (particle size and size distribution, particle shape,
structure and surface characteristics) and by the way com-
paction is carried out. Compaction induces very complex
states of stress in the powder. Lubrication, powder height in
the die, compaction rate and stress triaxiality strongly
influence the compaction process and, thus, affect the
properties of the products obtained [1]. Accordingly, opti-
misation of mechanical properties of green compacts
requires a better knowledge of the relation between powder
characteristics and mechanical behaviour of the material
during compaction (grain sliding and rearrangement, grain
deformation). Furthermore, the mechanisms for the devel-
opment of green strength during compaction are generated
by two phenomena, namely (i) particle sliding and inter-
locking and (ii) plastic deformation [2]. The initial stage of
compaction leads to rearrangement of the powder from a
loose array to close packing. As the pressure increases, the
contact area between the grains increases and particles
undergo extensive plastic deformation [3]. Green strength
has been found to be related to the contact area between
particles [3].
Generally, PM studies take into account particle size,
but neglect morphological parameters of powder grains as
they are more complex to define, measure and modify.
Grain size can be changed by simple grinding, but the
shape of the particles and their surface aspect results from
the chemical processes of powder preparation. In a pre-
vious study [4], it was shown that compacts of commercial
spherical or irregular iron powders have green strength up
0032-5910/02/$ - see front matter D 2002 Elsevier Science B.V. All rights reserved.
PII: S0032 -5910 (02 )00034 -7
* Corresponding author.
E-mail address: [email protected] (D. Poquillon).
www.elsevier.com/locate/powtec
Powder Technology 126 (2002) 65–74
to five times lower than those prepared from iron powder
with a spongy rough surface. To get a better understanding
of this phenomenon, we have chosen to study the influence
of such morphological parameters. Thus, two iron powders
were prepared to study the correlation between powder
morphology and mechanical properties (compaction and
three-point bending tests). The results obtained are pre-
sented in this paper and in a companion paper [5] devoted
to bending tests. In this first paper, the preparation of small
particles of metal with two different morphologies is
detailed. Compaction tests are then carried out on both
powders and the results are discussed in terms of micro-
structural effects. A model is proposed to simulate the
experimental curves relating the density of the compacts to
the compaction pressure. It is worth emphasising that most
of the previous investigations focused on the high relative
density range ( > 0.85). In this study, we were interested in
compacts with significant porosity, i.e. of relative density
under about 0.7.
2. Experimental data
2.1. Preparation and characteristics of the powders
Iron powders were prepared by reduction [6] of two
FeC2O4 � 2H2O oxalate particles having different morpho-
logical characteristics. These differences resulted from the
precipitation methods used. To get spherical shaped oxalate
particles (Fig. 1a), ferrous iron was precipitated by ammo-
nium oxalate in aqueous solution. The second type of
FeC2O4 � 2H2O oxalate was obtained with the reaction of
ferrous iron with oxalic acid in hydro-alcoholic medium
(Fig. 1b).
The preparation of the iron powders was then achieved
through direct decomposition of the oxalic precursors un-
der pure H2 (99.995%) in a specially designed furnace
(Type: ELTI 1731/S, volume close to 110 l). The rate of
gas flow was 580 l h� 1. The temperature was first held at
150 jC for 3 h to eliminate H2O from the ferrous oxalate
FeC2O4 � 2H2O. Afterwards, thermal decomposition of
ferrous oxalate with spherical morphology was performed
at about 500 jC. Fig. 2a shows the typical shape of the
powder thus obtained. This powder is made of more or less
spherical grains. This powder will be denoted powder S.
The average particle size is 15 Am. It can be seen in Fig.
2a that each grain is an agglomerate of small crystallites
with a typical size of about 0.5–1 Am. A processing
temperature higher than 500 jC has been tried, but resulted
in the growth of individual crystallites, and the final
roughness of the spherical powder particles decreased. The
thermal decomposition of the acicular ferrous oxalate was
performed also under pure H2, for a processing tempera-Fig. 1. Photograph of the oxalate precursors: (a) spherical ferrous oxalate
precursor; (b) Acicular ferrous oxalate precursor.
Fig. 2. Photograph of the iron powder: (a) S, spherical morphology; (b) E,
spongy morphology.
D. Poquillon et al. / Powder Technology 126 (2002) 65–7466
ture of about 600 jC. The resulting powder, denoted
powder E, appeared like agglomerates of tangled acicular
metallic crystallites. Fig. 2b shows a typical micrograph of
powder E. The grains are more irregular in shape than
those of powder S; they are rough and spongy and are
composed of crystallites of about 1–2 Am in size. The
average grain size is about 30 Am.
Various experiments were performed to characterise the
two types of powder after their preparation. The specific
surface area of the powders was measured following the
Brunauer, Emmet and Teller method [7] of adsorption of a
single layer of N2 at the surface of the powder grains. This
was made with a MICROMERITICS FLOWSORB II 2300
device. The specific surface area obtained for powder S was
2 m2 g� 1, whereas the specific surface area measured for
powder E was 0.6 m2 g� 1. Also, the apparent density of the
powders was evaluated by measuring the mass of powder
filling a container of known volume. This measurement was
performed without vibration of the powder. The mass of
powder divided by this volume defines the apparent density
of the powder. The values found were 1.173 g cm� 3 for
powder E and 1.169 g cm � 3 for powder S. The actual
density of the powders was evaluated through a He pycn-
ometer MICROMERITICS ACCUPYC 1330. The meas-
ured values were 7.73 g cm� 3 for powder E and 7.64 g
cm � 3 for powder S. These values are to be compared to the
density of pure body-centered cubic Fe which is 7.86 g
cm � 3. This difference is mainly due to surface oxidation of
the powder. This point is evidence by thermogravimetric
analysis detailed in the next paragraph.
The difference between the estimated apparent density of
the powders and that of iron was investigated by oxidising
the powders to evaluate their metallic Fe content. This was
performed by thermogravimetric analysis (TGA) on 20 mg
samples with an automatic thermobalance SETARAM
TGA92 under air during one heating up to 1000 jC at
3 jC/h. The iron content was calculated according to the
following oxidation reaction:
ð1� xÞFeþ xFe3O4 þ3
4� 1
2x
� �O2Z
1
2þ x
� �Fe2O3:
The content (in weight) of metallic Fe obtained with this
method was about 96.3% for powder E and 93.4% for
powder S. Assuming that the remaining mass is due to
Fe3O4, we obtained the following value of density 7.71 g
cm � 3 for powder E and 7.60 g cm� 3 for powder S. These
TGA results are found to be in agreement with the previous
estimates of the density (He pycnometer); thus, closed
porosity can be neglected for both powders.
The morphology of the powders is thought to be
responsible for the difference in Fe3O4 content because
the specific surface area of powder S was much higher than
that of powder E as indicated above. The larger average
size of both powder particles and constitutive crystallites of
powder E can explain its smaller specific surface area with
respect to powder S even if the grains of powder S
appeared more compact as illustrated in Fig. 2. These
differences in size are coherent with the difference in
specific surface area previously noted. Thus, powder S
with a larger specific surface area is more reactive than
powder E during storage in air. Consequently, powder S
presents a larger ability to develop Fe3O4 at its surface.
Finally, it was thought useful to have a quantitative
parameter to compare the ‘‘roughness’’ of the two mor-
phologies. It was found that the angle of repose for the
powders could conveniently provide such an information.
This quantity is frequently used in soil mechanics to
quantify the ability of sand or clay to flow. Angles of
repose below 45j indicate a good ability of the material to
flow and, as a consequence, the use of such material as an
embankment is not adequate. A triplicate test of the angle
of repose was performed under the standard AFNOR NF
A95-113 to compare the sliding and rearrangement facili-
ties of the powders. Powder S exhibited a 38F 0.5j angle
of repose, indicating a good ability of the grains to slide
and rearrange, whereas powder E exhibited a 52F 0.5jangle of repose, indicating that the irregular shape of the
grains should obviate easy interparticle sliding.
2.2. Compaction tests
A uniaxial SPECAC press was used to carry out the
compaction tests. As only the lower punch could move,
single-end pressing was carried out. The load imposed
was measured, but not the load transmitted to the upper
punch. This is unfortunate as this would have allowed us
to quantify the wall friction effects. Furthermore, the
elastic compliance of the apparatus was not taken into
account. Two different types of green compacts were
produced: cylindrical specimens and bars. Both types of
specimens were pressed at room temperature. The final
compaction pressure was varied between 100 and 350
MPa. Zinc stearate in acetone solution was used as die
lubricant. Compactions were performed in air, i.e. no
vacuum or controlled atmosphere was imposed during
compaction. The bars were designed to be used for the
three-point bending tests. Those tests are detailed and
described in a companion paper [5], but the correspond-
ing density data will be detailed in the present paper. Iron
powders were compacted in a hardened steel rectangular
die, which was 32.36 mm in length and 13.28 mm in
width. These dimensions are comparable to those of
normalised rupture tests (MPIF standard 15). Each speci-
men corresponded to about 6 g of iron powder. The
uncertainty about their final density due to the uncertain-
ties on dimensions and weight is 0.5%. The die used to
compact the cylindrical specimens was 10 mm in diam-
eter. The initial surface finish of the die walls and of the
punch was below 1 Am. Each cylindrical specimen
required less than 1 g of powder. The compaction of
the cylindrical specimens was followed with a MITU-
TOYO comparator.
D. Poquillon et al. / Powder Technology 126 (2002) 65–74 67
At the end of each compaction, the final pressure was
maintained for 2 min before the ejection of the green
compact. After compaction, the compacts were weighed
with an uncertainty of F 0.001 g and their dimensions
measured with a micrometer calliper to F 0.01 mm. The
relative density of the compacts was then estimated from
these values, with a total uncertainty of 0.5% for the bars
and 2% for the cylinders. From the final height of the
compact and from the displacement of the lower punch in
the case of the cylinders, it was, thus, possible to evaluate
the curve giving the applied pressure vs. density. It is worth
noting that, because of this method, the uncertainty in the
density is larger at the lower applied pressures. Every
experiment has been repeated two or three times under a
strict procedure. Although the lower punch displacement
was manual, it was found that the compaction curves were
highly reproducible.
Table 1 gives the main characteristics of the green
compact bars, whereas Table 2 lists those of the cylindrical
specimens. In these tables, the relative density is defined as
the apparent density divided by the actual density measured
with the He pycnometrer. Two main tendencies were noted:
(i) the cylindrical samples achieved generally lower relative
density than bars; (ii) powder E had better compressibility
than powder S. It is well known that die wall friction
depends on the compact height and on the die geometry
even when a lubricant is used [1,8,9]. The difference in
compressibility observed during compaction between bars
and cylindrical specimens could have been investigated by
an analysis of the transmitted load which could not be made
with the rig employed during this study.
Fig. 3 compares the green densities achieved with the
final compaction pressure for the bars and cylinders.
Although powder S had a slightly higher density than
powder E before compaction and also had a lower angle of
repose, it is observed that powder S had a slightly lower
compressibility in the range of pressures studied. This could
mean that the morphological differences between the two
powders affect compaction only at low pressures, i.e. when
grain sliding controls the changes in density. Fig. 3 shows
also that the density is a linear function of the compaction
pressure for relative density lower than about 80%. This
result is in agreement with previous data obtained for copper
[10], iron [11] and aluminium [12] powders, which have
been also plotted in Fig. 3.
The compaction response of the powders is shown in
Fig. 4, where it is observed that all the curves show the
same features. The response of the powders during single-
end pressing can be divided into three different stages,
whatever the powder morphology (E or S) is. During Stage
I (0 to 15 MPa), densification increases very slowly; then in
Stage II, densification increases abruptly until the start of
the Stage III where the densification rate decreases. The
limit between Stages I and II is the end of linearity of the
first part of the curve. This limit seems to depend on the
initial relative density of the powder. The denser the initial
Table 1
Green compact (bar specimen) characteristics
Compact
label
Compaction
pressure (MPa)
Relative
density (%)
Weight
(g)
Height
(mm)
S100.1 100 48.86 6.010 3.75
S100.2 100 48.65 5.919 3.71
S100.3 100 48.65 5.915 3.70
S150 150 54.21 6.113 3.43
S200.1 200 58.66 6.108 3.17
S200.2 200 58.86 6.321 3.27
S250 250 62.10 6.227 3.05
S290.1 290 65.72 6.232 2.89
S290.2 290 65.57 6.307 2.93
E100.1 100 54.96 5.959 3.27
E100.2 100 52.02 5.991 3.47
E150 150 59.95 6.192 3.11
E200.1 200 59.86 6.554 3.29
E200.2 200 59.75 6.507 3.28
E250 250 64.44 6.265 2.93
E290.1 290 71.29 13.017 5.50
E290.2 290 71.44 13.056 5.50
Table 2
Green compact (cylindrical specimens) characteristics
Compact
label
Compaction
pressure (MPa)
Relative
density (%)
Weight
(g)
Height
(mm)
PS200.1 200 55.7 0.694 2.07
PS200.2 200 55.6 0.694 2.08
PS350.1 350 64.1 0.815 2.12
PS350.2 350 62.4 0.795 2.10
PE200.1 200 60.3 0.595 1.62
PE200.2 200 59.8 0.595 1.64
PE350 350 68.4 0.802 1.93
Fig. 3. Relative density of compacts vs. the final pressure applied.
Comparison of the results obtained during this study with results obtained
for copper [10], iron [11] and aluminium [12] powders.
D. Poquillon et al. / Powder Technology 126 (2002) 65–7468
powder is, the lower the limit between Stages I and II.
However, as the initial density of powder E is on average
lower than that of powder S, it is difficult to separate the
effects of morphology from those of the initial density.
The end of Stage II and, thus, the beginning of Stage III, is
less easy to determine on the curves. We fixed it at
P1 = 35 MPa, where densification rate has clearly started
to decrease.
Compaction of iron powders during Stages I and II is
comparable to soil compaction, e.g. clays [13–16]. This
type of behaviour is due to elastic deformation of the
particle heap during Stage I and to particle rearrangement
by interparticle sliding during Stage II. Stage I is totally
reversible. While intense irreversible particle sliding and
rearrangement occur during Stage II, it is assumed to
correspond to negligible plastic deformation and energy is
mainly dissipated by interparticle friction. The transition
from Stage I to Stage II is related to an abrupt increase of
densification. Stage III starts when particle interlocking
generates plastic deformation, which is first localised at
the contact areas between particles [2,8].
SEM observations of the surface of the green compacts
were performed in order to compare the morphology of the
grains after compaction at pressures between 100 and 290
MPa. Fig. 5a and b provides a comparison of the micro-
structure of powder S after pressing at 100 and 290 MPa,
respectively. Interparticle porosity seemed to be reduced and
the contact area between grains to be increased with
increased pressure. In Fig. 5c, it is seen, however, that the
shape of the grains is still identifiable. Also, it seemed that
the decrease of the porosity with increasing compaction
pressure proceeded through localised plastic deformation at
the contact zone between grains. Fig. 5d shows the micro-
structure of powder E after compaction at 290 MPa. In this
case, it appears impossible to identify the initial powder
grains because of large interlocking. The contact zones
between grains were less localised and involved more
crystallites than in the case of powder S. Observations made
on compacts pressed at various pressures showed that
particle interlocking was dominant and increased with
compaction pressure in the case of powder E. These differ-
ences between powder E and powder S can be correlated
with the higher density obtained for the former one than for
the latter at a given compaction pressure. Moreover, the
effects of wall friction during compaction were evidenced
for the specimens compacted at 290 MPa as experimental
observations indicated noticeable shear stress near the wall.
Intense and localised plastic deformations were observed in
the first 150 Am, under the surface in areas in contact with
either the lateral wall or the punches.
3. Numerical simulation of the compaction tests
The three-compaction stages depicted in the preceding
part have been described by means of two different mod-
Fig. 4. Relative density of the compacts vs. the applied compaction pressure.
D. Poquillon et al. / Powder Technology 126 (2002) 65–74 69
els: the CAM-CLAY model for Stages I and II, and a
power law model for Stage III. The CAM-CLAY model
was initially devoted to soils science and developed to
simulate the behaviour of clays, accounting for voids and
water content [13–16]. This model is intended to consider
elastic deformation as well as sliding of the grains between
each other. The CAM-CLAY approach has an excellent
ability to be transposed from soil mechanics to cold
compaction of spherical commercial iron powders [17–19].
The power law used in the model selected to describe Stage
III is supposed to take into account the plastic deformation of
the contact area between grains.
The parameters entering the constitutive equations of
both models were identified by means of a phenomenolog-
ical approach, i.e. by looking for the simplest expressions
allowing for fitting the experimental curves. The main
features of these models as well as the results for the three
successive stages of the compaction are described below.
As no quantitative experimental data was available to
access die wall friction, calculations were performed assum-
ing uniform compression in the die. Accordingly, the stress
state in the sample was assumed to be homogeneous with
axial symmetry.
The tensorial equations of the CAM-CLAY model have
been described previously [16]. As only homogeneous
uniaxial compression is considered, the mechanical equa-
tions can be simplified. The only possible deformation
occurs along the compression axis (let it be denoted z) so
that the strain tensor ¯e is constant throughout the sample
thickness. It has the following expression in axi-symmetric
coordinates: ¯e ¼ ezzez � ez , where ezz is the deformation
along the z-axis, ez is the unit vector in the axial direction
and � stands for the tensorial product. If q0 is the initial
relative density and q the current relative density of the
compact, the strain evolution during compaction is simply
given by: ezz=(q0/q)� 1. It is common practice in soil
mechanics to replace the relative density by the void ratio,
e, for materials with high porosity. This parameter is
defined as e=(1� q)/q and was adopted for the present
analysis. By substitution, ezz= q0(e� e0), where e0 stands
for the initial void ratio. In the following analysis, the
pressures are to be expressed in MPa.
The response of the material according to the CAM-
CLAY model depends on five parameters. Two parameters
are related to the initial state of the material, namely the
initial voids ratio, e0, and the yield pressure, Pi0. The
three other parameters are material intrinsic characteristics.
They are denoted M, j (the loading–unloading slope) and
k (the loading slope on the yield surface). The yield
surface is a function of the mean stress, p, and of the
deviatoric stress, q. Its shape is elliptical in a p–q graph.
It presents a maximum at the point ( pm, qm). M is the
Fig. 5. Observation of the lateral surface of compacts: (a) Powder S, final pressure 100 MPa; (b) Powder S, final pressure 290 MPa; (c) Powder S, final pressure
290 MPa; (d) Powder E, final pressure 290 MPa.
D. Poquillon et al. / Powder Technology 126 (2002) 65–7470
slope of the critical state line and is defined by M= qm/pm.In the CAM-CLAY model, this value is constant and
independent of the yield pressure, Pi0, reached. As only
uniaxial tests had been performed, triaxiality aspects of the
behaviour of the powders were not investigated. As a
consequence, the M parameter was not evaluated.
Fig. 6 shows schematically the response of the material
according to the CAM-CLAY model. It is seen that the
void ratio first decreases slowly from e0 as the compaction
pressure increases. During this first stage, only elastic
deformation of the grains is involved. Thus, during unload-
ing, the material should follow the same curve. The sur-
face roughness of the grains prevents interparticle sliding
and reversible strain comes from skeletal elastic deforma-
tion of the particle arrangement. As the yield pressure, Pi0,
is reached, the rate of change in void ratio increases
abruptly. This is intended to reproduce the sliding of the
grains between each other during Stage II. In the case of
unloading, the compacts have an elastic response with the
same slope as that during Stage I. However, the overall
deformation due to sliding is not reversible as illustrated in
Fig. 6.
To describe Stage I, it was found convenient to relate e
and log10(PC) according to the linear relation: e = e0�jlog10(PC), where PC is the compaction pressure. More-
over, the value j = 0.2 was found to allow fitting of the
Fig. 6. Schematic representation of the evolution of the void ratio with the
compaction pressure according to the CAM-CLAY model. Definition of the
slopes j and k.
Fig. 7. Predicted evolution of the void ratio with the applied compaction pressure during stages I and II (curves with small symbols). Comparison to
experimental measurements (large symbols). The interrupted line represents the limit between stages I and II.
D. Poquillon et al. / Powder Technology 126 (2002) 65–74 71
curves whatever the initial density and the shape of the
powder grains. A comparison between predicted and meas-
ured curves is shown in Fig. 7. The end of Stage I
corresponds to a compaction pressure equal to the yield
pressure, Pi0. By means of an iteration procedure, it was
found convenient to set Pi0 = 12 + e0 for all cases. This limit
between Stages I and II is also drawn on Fig. 7. It is clearly
seen that during initial compaction, the start of grain sliding
depends either on the initial void ratio or on the shape of the
grains, or else on both of them. Unfortunately, the present
results were not sufficient to determine the actual effect of
each of these quantities.
To describe Stage II, a linear relation between e and
log10(PC) was considered as for Stage I. Moreover, it was
thought convenient to introduce the initial void ratio e0 as
Stage I did not lead to significant compaction. It was finally
found that most of the features of the curves could be
satisfactorily reproduced by considering the following
expression for the irreversible compaction:
e ¼ eðPi0Þ � klog10Pc
Pi0
� �,
with:
k ¼ e0 � 3:5
1:48� log10ðPi0Þ:
It is worth noting that the slope k depends on e0 in such a
way that particle sliding increases as the initial void ratio is
increased. The critical value e0 = 3.5 could correspond to
compacts initially so dense that compaction should start
directly in Stage III. Moreover, it should be emphasised that
the selected expressions of e and k could be chosen as
identical for both powders. This may come from the fact that
powder S had initially a relative density higher than powder
E. As it was mentioned previously, there is not enough
experimental information to separate the effects of particle
size and those of particle shape. However, Fig. 7 shows that
a quite good agreement between simulations and experi-
mental data could be obtained for Stage II also.
The beginning of Stage III was fixed at P1 = 35 MPa,
where densification rate has clearly started to decrease.
Modelling of Stage III was achieved with the following
power law q = q1 + a(P�P1)n, where q1 and P1 are the
relative density and the compaction pressure, respectively,
Fig. 8. Evolution of the relative density of the compacts during stage III. Comparison of the predicted evolution (dotted lines) with measurements
(symbols).
D. Poquillon et al. / Powder Technology 126 (2002) 65–7472
at the end of Stage II. a characterises the material’s ability
to be deformed, while n is equivalent to a hardening
coefficient. Both parameters were considered as constants
to be fitted to experimental data. The best fit between
calculated and experimental curves showed that the value
of n could be the same for powders S and E. This would
mean that the mechanism for dissipation of the energy
related to plastic deformation should be the same for both
powders. It was, thus, decided to use one single value of n
for this model parameter, which was set equal to 0.55 for
all simulations.
Given the value of n, the best value for a was found to be
1.69� 10� 2 MPa � 0.55 for powder S and 1.94� 10� 2
MPa � 0.55 for powder E. This difference relates to the
higher densification achieved with powder E than with
powder S. Fig. 8 compares the calculated and experimental
curves. It is seen that a satisfactory agreement is obtained
for the whole range of pressure, which means that this
simple model is able to reproduce most of compaction
process when simulated as a uniaxial compression.
4. Conclusion
The effect of morphology of iron powder on their
compaction behaviour has been studied in the case of
compacts with final porosity higher than 0.3. Two pow-
ders, one with spherical grains and the other with spongy
grains, have been synthetized in order to prepare green
compacts under pressures ranging from 100 to 350 MPa. It
was found that the density of the compacts varied linearly
with the compaction pressure in the range investigated,
with a higher ability to be compacted for the spongy
powder than for the spherical one. As the sliding of the
grains is easier for the spherical powder, such a difference
relates to a larger plastic deformation of the spongy
powder particle. This was clearly evidenced by SEM
observations of the compact surface. The compaction
behaviour of both powders has been experimentally
described by the relation between the applied compaction
pressure and the relative density of the material. The
curves show that compaction proceeds along three succes-
sive stages involving elastic deformation of the grains
(Stage I), interparticle sliding with elastic deformation
(Stage II) and, finally, plastic deformation of the grains
(Stage III). It was observed that particle sliding and
rearrangement occurs at higher pressure in the case of
spongy powder-based compacts. These green compacts
achieved a slightly higher density at a given compaction
pressure than spherical powder-based compacts. These
observations are in agreement with the higher angle of
repose and higher capability for plastic deformation of the
spongy powder than the spherical one.
The whole compaction process has been simulated with
two models, the CAM-CLAY model for Stages I and II and
a power law model for Stage III. It is worth emphasising
that calculations were made with the same values of the
model parameters for both powders, apart from a, whichcharacterises the deformation capability of the powder.
Quantitative differences were, thus, accounted for only
through the initial void ratio which was higher for the
spongy powder than for the spherical one. A better
description of Stage III would rely on a characterisation
of the evolution of the porosity during compaction and,
particularly, in separating interparticle and intraparticle
voids. Ozkan and Briscoe [9] have performed such a study
by means of laser profilometry on powders of a alumina.
This could be applied to the powders investigated in this
study. It could also be of great interest to confirm the
validity of the three successive stages assumed for model-
ling. For example, the beginning of plastic deformation
during compaction could be checked by acoustic emission
[20].
The behaviour of powders during uniaxial compaction
did not allow us to identify the yield surface of the CAM-
CLAY model (coefficient M ), which is effected by inter-
locking and grain sliding. It may be guessed that powders E
and S would have a more different behaviour during shear
test (or isostatic compaction) than during uniaxial compac-
tion. This could be investigated by means of the exper-
imental rig developed by Pavier and Doremus [21], who
showed shear stress to be more favourable to compaction
than hydrostatic stress. Knowledge of the yield surface of
the powders would allow further description of be the
transition from grain sliding to particle interlocking and
the beginning of plastic deformation. The heterogeneities in
the compacts could then be simulated.
References
[1] B.J. Briscoe, S.L. Rough, The effects of wall friction in powder com-
paction, Colloids and Surfaces, A: Physicochemical and Engineering
Aspects 137 (1998) 103–116.
[2] J.A. Lund, Origins of green strength in iron P/M compacts, Interna-
tional Journal of Powder Metallurgy & Powder Technology 18 (2)
(1982) 117–127.
[3] I.-M. Moon, J.-S. Choi, Dependence of green strength on contact area
between powder particles for spherical copper powder compacts,
Powder Metallurgy 28 (1) (1985) 21–28.
[4] V. Baco-Carles, J. Lemaıtre, D. Poquillon, Ph. Tailhades, J. Lacaze, A.
Rousset, Correlations entre la morphologie de poudres de fer metal-
lique, leur aptitude a la compaction et la resistance mecanique en
flexion de compacts crus, Colloque ‘‘Science et Technologie des Pou-
dres’’, Nancy, France, 3–5 Avril, 2001, For publication in Recents
Progres en Genie des Procedes.
[5] D. Poquillon, V. Baco-Carles, Ph. Tailhades, E. Andrieu, Cold com-
paction of iron powders—relations between powder morphology and
mechanical properties: Part II : Bending tests, results and finite ele-
ment analysis, Powder Technology, companion paper.
[6] V. Carles, P. Alphonse, Ph. Tailhades, A. Rousset, Study of thermal
decomposition of FeC2O4 � 2H2O under hydrogen, Thermochimica
Acta 334 (1999) 107–113.
[7] S. Brunauer, P.H. Emmet, E. Teller, The adsorption of gases in
multimolecular layers, Journal of the American Chemical Society
60 (1938) 39.
D. Poquillon et al. / Powder Technology 126 (2002) 65–74 73
[8] H. Lippmann, V. Mannl, R. Iankov, O. Beer, Numerical simulation of
density distribution during compaction iron powders, Archive of Ap-
plied Mechanic 67 (1991) 191–199.
[9] N. Ozkan, B.J. Briscoe, The surface topography of compacted ag-
glomerates; a means to optimize compaction conditions, Powder
Technology 86 (1996) 201–207.
[10] I.-H. Moon, K.-H. Kim, Relationship between compacting pressure,
green density, and green strength of copper powder compacts, Powder
Metallurgy 27 (2) (1984) 80–84.
[11] G.W. Halldin, K.T. Yung, T.H. Tsai, A new analysis of compressibility
and green strength of metal powder, Progress in Powder Metallurgy 37
(1982) 383–393.
[12] C.G. Tu, I.T. Chen, The pressure–density– strength relationships of
aluminium alloy powder compacts, Journal of the Chinese Institute of
Engineers 13 (3) (1990) 259–271.
[13] K.E. Roscoe, A.N. Schofield, C.P. Wroth, On the yielding of soils,
Geotechnique 9 (1968) 71–79.
[14] A.N. Schofield, C.P. Wroth, Critical State Soil Mechanics, McGraw-
Hill, New York, 1968.
[15] I.B. Burland, K.E. Roscoe, On the generalized stress–strain behaviour
of wet clay, Engineering Plasticity, Heyman-Leckie, Cambridge,
1968.
[16] F. Darve, Manuel de rheologie des geomateriaux, Ed. by Presses de
l’ENPC Paris, 1987.
[17] E. Pavier, P. Doremus, Mechanical behaviour of lubrificated iron
powder, Metal Powder Report 52 (10) (1997) 40–47.
[18] PM-Modnet-Computer-Modelling-Group, Comparison of computer
models representing powder compaction process. Powder Metallurgy,
Powder Metallurgy 42 (4) (1999) 301–311.
[19] X.K. Sun, S.J. Chen, J.Z. Xu, L.D. Zhen, K.T. Kim, Analysis of cold
compaction densification behaviour of metal powder, Materials Sci-
ences & Engineering, A: Structural Materials: Properties, Microstruc-
ture and Processing 267 (1999) 43–49.
[20] N. Parida, B.B. Pani, B.R. Kumar, Acoustic emission assisted com-
paction studies on iron, iron–aluminium and iron-cast iron powders,
Scripta Materialia 37 (11) (1997) 1659–1663.
[21] E. Pavier, P. Doremus, Triaxial characterisation of iron powder
behaviour, Powder Metallurgy 42 (4) (1999) 345–352.
D. Poquillon et al. / Powder Technology 126 (2002) 65–7474