POLYMERS FOR ADVANCED TECHNOLOGIES
Polym. Adv. Technol. 2008; 19: 1914–1921
Published online 2 September 2008 in Wiley InterScience (www.interscience.wiley.com) DOI: 10.1002/pat.1231
Microencapsulation of ammonium polyphosphate with
PVA–melamine–formaldehyde resin and its flame
retardance in polypropylene
Kun Wu1, Lei Song1, Zhengzhou Wang1,2* and Yuan Hu1*
1
2
State Key Laboratory of Fire Science, University of Science and Technology of China, Anhui 230026, P.R. China
School of Materials Science and Engineering, Tongji University, Shanghai 200092, P.R. China
Received 30 April 2008; Accepted 17 June 2008
With a shell of PVA–melamine–formaldehyde resin, microencapsulated ammonium polyphosphate
(VMFAPP) is prepared by in situ polymerization and characterized by FTIR and XPS. Microencapsulation gives VMFAPP better water resistance and flame retardance compared with APP in PP.
Thermal stability and fire resistance behavior have been analyzed and compared. The LOI value of
the PP/VMFAPP composite is higher than that of the PP/APP composite. The UL 94 ratings of most of
the PP/VMFAPP composites are V-0, whereas PP/APP gives no rating at the 30% additive level. The
water resistant properties of the PP composites are studied. Results of the cone calorimeter
experiment show that VMFAPP is an effective flame retardant in PP compared with APP. The
thermal degradation behaviors of APP and VMFAPP have been studied using TG and dynamic FTIR.
Copyright # 2008 John Wiley & Sons, Ltd.
KEYWORDS: microencapsulation; ammonium polyphosphate; intumescent flame retardation; thermal degradation; PVA; melamine–
formaldehyde; PP
INTRODUCTION
There has been enormous loss of materials and high rates of
human mortality due to the weak flame resistance properties
of polymers. Intumescent flame retardants (IFRs) have
attracted considerable attention in recent years because they
are more environmentally friendly than the traditional
halogen-containing flame retardants. IFR systems contain
three active ingredients: an acid source (e.g. ammonium
polyphosphate (APP), etc.), a carbonization agent (e.g.
pentaerythritol, polyurethane, etc.), and a blowing agent
(e.g. melamine). Bourbigot and co-workers have carried out
extensive studies on the APP IFR system in polyolefins1–3
and have reviewed recent developments of IFR systems in
great detail.4 But these systems are not durable due to the
weak water resistance and low compatibility with organic
materials of APP. In order to overcome this problem,
microencapsulation is a good choice.
Melamine–formaldehyde (MF) resin is commonly used in
microencapsulation of red phosphorus,5 n-octadecane,6 etc.
Poly(vinyl alcohol) (PVA) is used for the microencapsulation
of di-ammonium hydrogen phosphate (DAHP) using
coacervation and the interfacial polymerization technique,
and the shell can be used as a charring agent in the flame
retardance of polymers.7,8 PVA, with many O–H groups,
*Correspondence to: Z. Wang and Y. Hu, State Key Laboratory of
Fire Science, University of Science and Technology of China,
Anhui 230026, P.R. China.
E-mail: wwang@uste.edu.cn and yuanhu@ustc.edu.cn
readily reacts with low molecular weight compounds and
various functional polymers can be obtained with relative
ease.9
Our group has recently microencapsulated APP with a MF
and urea–melamine–formaldehyde (UMF) resin shell.10,11
Compared with APP, the microencapsulated APP (MCAPP)
coated with MF or UMF resin can be dispersed well in the PP
matrix and has lower water solubility. Because of the scarcity
of the carbonization agent in MCAPP, there are no ratings in
the UL 94 test for the PP composites containing MCAPP
although the LOI values of the PP composites containing
MCAPP are higher than those of the PP composites
containing APP at the same content. To solve the problem,
we developed a different approach to microencapsulate APP
with a PVA modified MF resin shell. Our aim is to synthesize
microcapsules which contain the three ingredients of a
typical IFR system: acid source (APP), carbonization agent
and blowing agent (PVA–melamine–formaldehyde (VMF)).
The advantage of this is that it is possible to synthesize an
intrinsic flame retardant which may have better flame
retardance and higher water resistance in the polymer,
compared with APP.
In this paper, microencapsulated APP (VMFAPP) with a
VMF resin shell was prepared by in situ polymerization and
characterized by water solubility, Fourier transform infrared
(FTIR), thermogravimetry (TG), and X-ray photoelectron
spectroscopy (XPS). The use of VMFAPP as a flame retardant
in PP is evaluated by limiting oxygen index (LOI), UL-94, TG,
cone calorimetry, and scanning electron microscopy (SEM),
Copyright # 2008 John Wiley & Sons, Ltd.
Microencapsulation of APP with VMF resin
1915
1
and the results from VMFAPP and APP are compared.
Moreover, the water resistant properties of the PP composites containing VMFAPP (or APP) are studied by LOI test
and water leaching rate. The thermal degradation behaviors
of APP and VMFAPP were also studied using TG and
dynamic FTIR, and the results from both samples are
compared.
heating rate of about 108C min . Dynamic FTIR spectra were
obtained in situ during the thermal degradation of the
samples.
EXPERIMENTAL
Solubility in water
Materials
1
PP (F401) with a melt flow index (MFI) of 2.3 g/10 min
(2308C/2.16 kg) was provided by Yangzi Petroleum
Chemical Company. APP with average degree of polymerization n > 1000 was purchased from Hangzhou JLS Flame
Retardants Chemical Corporation. PVA (polymerization
degree ¼ 1750, degree of alcoholysis ¼ 98–99%) was kindly
supplied by Shanghai DongCang International Trading Co.,
Ltd. (China). Melamine and formaldehyde were purchased
from Shanghai Chemical Reagent Corporation.
XPS spectra
The XPS spectra were recorded with a VG ESCALAB
MK II spectrometer using Al ka excitation radiation
(hn ¼ 1253.6 eV).
The sample (about 10 g) was put into 100 ml distilled water
and stirred for 60 min at different temperatures. The
suspension was then filtered, 50 ml of the filtrate was
removed and dried to constant weight at 1058C, permitting
the calculation of solubility.
SEM
The SEM micrographs of the PP composites were obtained
with a scanning electron microscope AMRAY1000B. The
specimens were cryogenically fractured in liquid nitrogen,
and then sputter-coated with a conductive layer.
Preparation of microencapsulated APP
Content of the VMF resin measurement
Synthesis of prepolymer: PVA (6, 9, 12, 15, or 18 g), melamine
(4 g), and distilled water (200 ml) were put into a threenecked bottle with a stirrer. The mixture was adjusted to
pH 4–5 with acetic acid, heated to about 908C, and kept
at that temperature for 1.5 hr. Then the pH was adjusted to
pH 8–9 with 10% Na2CO3 solution, then 4 g melamine and
10 ml 37% formaldehyde solution were added into the
system. The temperature was kept at 908C for 1 hr. The
prepolymer solution was then prepared and it was ready for
the next step.
Preparation of microencapsulated APP: 40 g APP was first
dispersed in 100 ml ethanol with a stirrer (1000 rpm, 5 min).
The prepolymer solution obtained from the above step was
added to the mixture, and the pH of the mixture was adjusted
to pH 4–5 with sulfuric acid. The resulting mixture was heated
at 808C for 3 hr with stirring (300 rpm). After that, the mixture
was filtered, washed with distilled water, and dried at 808C,
and the VMFAPP powder was finally obtained. The D50 value
of the microcapsules was about 20 mm.
Some APP or VMFAPP powder was dissolved in nitric acid
at 1508C, and inductively coupled plasma atomic emission
spectrometry (Atomscan Advantage, Thermo Jarrell Ash
Corporation, USA) was used to measure the phosphorus
content of APP or VMFAPP. The symbols PVMFAPP% and
PAPP% represent the percentage of phosphorus in VMFAPP
and APP, respectively.
Assuming that the content of phosphorus remains
constant in the process of the microencapsulation of APP,
we obtain:
Preparation of flame retarded (FR) PP
composites
All flame-retarded PP composites were prepared in 15 min in
a Brabender-like apparatus at a temperature of about 1808C.
After mixing, the samples were hot-pressed at about 1808C
under 10 MPa for 10 min into sheets of suitable thickness for
analysis.
MEASUREMENTS
FTIR spectra
Powders were mixed with KBr powder, and the mixture was
pressed into a tablet. The FTIR spectra of samples were
recorded using a Nicolet MAGNA-IR 750 spectrophotometer.
Real time FTIR spectra were recorded using the above
spectrophotometer equipped with a ventilated oven having a
heating device. The temperature of the oven was raised at a
Copyright # 2008 John Wiley & Sons, Ltd.
MAPP PAPP % ¼ MVMFAPP PVMFAPP %
where MAPP is the content of APP used and MVMFAPP is the
content of VMFAPP obtained. Therefore the percentage of
the resin (Wresin, wt%) in VMFAPP can be expressed as
follows:
Wresin ðwt%Þ ¼ 1 MAPP =MVMFAPP
¼ ð1 PVMFAPP %=PAPP %Þ 100%
if PVMFAPP % and PAPP% are measured, Wresin (wt%) can be
calculated.
LOI
LOI was measured according to ASTM D2863. The apparatus
used was an HC-2 oxygen index meter (Jiangning Analysis
Instrument Company, China). The specimens used for the
test were of dimensions 100 6.5 3 mm3.
UL-94 testing
The vertical test was carried out on a CFZ-2-type instrument
(Jiangning Analysis Instrument Company, China) according
to the UL-94 test standard. The specimens used were of
dimensions 130 13 3 mm3.
Water leaching rate of FR PP composites
The specimens (marked Wa) were put in distilled water and
the temperature was kept at 508C for 24 hr. The treated
Polym. Adv. Technol. 2008; 19: 1914–1921
DOI: 10.1002/pat
1916 K. Wu et al.
specimens were subsequently removed and dried to constant
weight at 808C (marked Wc). The water leaching rate of the
specimens can be expressed as (Wa–Wc)/Wa 100%.
Each sample was examined under air flow (30 ml min1) on a
DTG-60H apparatus (Shimadzu Company) at a heating rate
of 108C min1. The weight of all samples was kept within 3–
5 mg in an open Al pan.
Cone calorimeter
C1s
Relative Intensity (au)
TG
O1s
The combustion tests were performed with a cone calorimeter (Stanton Redcroft, UK) tests according to ISO 5660
standard procedures, with 100 100 3 specimens. Each
specimen was wrapped in an aluminum foil and exposed
horizontally to 35 kW m2 external heat flux.
N1s
VMFAPP
APP
P2pP2S
200
400
600
800
1000
Banding energy (eV)
Figure 2. XPS spectra of APP and VMFAPP.
RESULTS AND DISCUSSION
Characterization of VMFAPP by FTIR and XPS
The FTIR spectra of APP and VMFAPP are shown in Fig. 1. It
is clear that for VMFAPP, the main absorption peaks appear
at 3200, 1664, 1560, 1504, 1430, 1339, 1256, 1138, 1075, 1020,
and 880 cm1. The typical absorption peaks of APP include
3200 (N–H), 1256 (P ¼ O), 1075 (P–O symmetric stretching
vibration), 880 (P–O asymmetric stretching vibration), and
1020 (symmetric vibration of PO2 and PO3) cm1.12 The
absorptions of 1560, 1504, and 1339 cm1 are due to the ring
vibration of melamine from the MF resin.5 The 1138 cm1
band is representative of symmetric C–O–C of –CH2–
O–CH2– between melamine groups.13 The peaks at 1430–
1458 are attributed to the O–H, C–H bending, and –CH2
deformation of PVA. The band at 1664 cm1 is assigned the
C–
– O group in PVA, and the C –– O group was likely due to the
absorption of the residual acetate group.14 The spectrum of
VMFAPP reveals not only well-defined absorption peaks of
VMF resin but also the characteristic bands of APP,
indicating that the resin exists in the VMFAPP.
Figure 2 shows XPS spectra of APP and VMFAPP. It can be
seen that the peaks located at about 134 and 191 eV are
Water solubility of VMFAPP
Figure 3 shows the influence of PVA content in the
prepolymer used on the water solubility of VMFAPP in
the microencapsulation. From Fig. 3, it can be seen that the
solubility of APP without microencapsulation at 25 and 808C
is 0.45 and 2.4 g/100 ml H2O, respectively, indicating that
APP can be easily attacked by moisture or water, especially at
high temperatures. After the microencapsulation of APP
with VMF resin, the solubility of VMFAPP decreases above
90% at 258C. As the content of the PVA in prepolymer
increases further, the solubility of VMFAPP changes little.
The trend of solubility of VMFAPP at 808C is similar to that of
1020
1256
1075
3200
VMFAPP
1430
o
80 C
2.5
Solubility g/100 ml H2O
APP
Transmittance(%)
attributed to P2P and P2S of APP. For VMFAPP, the intensities
of aforementioned peaks decrease sharply, meanwhile the
intensities of the C1S and N1S peaks centered at about 285 and
398 eV, respectively, increase greatly. The changes of the
above peaks are due to the coverage of the outside APP
particles with the VMF resin, which indicates that APP was
well coated by the resin.
1339 880
1138
pure APP
2.0
1.5
1.0
o
25 C
0.5
pure APP
1664
4000
3500
3000
2500
1504
1560
1256
2000
1500
1000
0.0
-2
500
0
2
4
6
8
10
12
14
16
18
20
Content of PVA in prepolymer (g)
-1
Wave number cm
Figure 1. FTIR spectra of APP and VMFAPP.
Copyright # 2008 John Wiley & Sons, Ltd.
Figure 3. Solubility of APP and VMFAPP versus content of
PVA in prepolymer.
Polym. Adv. Technol. 2008; 19: 1914–1921
DOI: 10.1002/pat
Microencapsulation of APP with VMF resin
VMFAPP at 258C. It is interesting to find that there is a great
difference in solubility of APP at 25 and 808C. However, the
difference in solubility of VMFAPP at 25 and 808C is small.
This is because the VMF resin outside APP is hydrophobic,
leading to a decrease in the solubility of APP.
Flame retardation of PP composites
The influence of PVA content in prepolymer used in the
microencapsulation on the LOI value of PP/VMFAPP
composite is shown in Fig. 4. VMFAPP is blended with PP
at the mass percentage of 30%. From the figure, it can be seen
that with the increase of PVA content, the LOI value of PP/
VMFAPP increases. It is proposed that a suitable phosphorus/nitrogen/carbon ratio in the IFR system is very
important for the flame retardant action of IFR in polymers.
So when the dosage of PVA in the prepolymer is above 15 g,
the LOI values of FR PP composites containing VMFAPP
show essentially no change. Moreover, it should be noticed
that the UL 94 results of most of the PP/VMFAPP composites
can reach V-0. As a result, the prepolymer containing 15 g
PVA was selected for the microencapsulation; from the
equation of content of the VMF resin, it can be calculated that
this VMFAPP sample is coated with 34.8% resin.
The LOI value of the composite containing 30% VMFAPP
(coated with 34.8% resin) is 32, whereas the value of the PP/
APP composite at the same additive level is only 20%. The
explanation for the increase may be the formation of an
intumescent char which can protect the underlying materials
from burning. When the PP composites containing VMFAPP
are heated, the resin in the coating layer of the microcapsule
releases water vapor and NH3 gas which would reduce the
concentration of air and make the material (formed mainly
by the esterification between APP and PVA) swell to form an
intumescent char. The above results illustrate that APP used
alone in PP does not have good flame retardancy (no ratings
in the UL-94 test), due to the scarcity of the carbonization and
blowing agents. Due to the presence of VMF resin outside
APP, VMFAPP is an effective flame retardant in PP in
comparison with APP.
1917
Water resistance of FR PP composites
The change of LOI values of the PP composites containing
APP or VMFAPP (microencapsulated with prepolymer
containing different PVA contents) after the hot water
treatment (508C, 24 hr) is shown in Fig. 4. For the PP/APP
binary composite at 30% additive level, the LOI values are
about 20% before the treatment and the values decrease by
2.5% after the hot water treatment. The LOI value of PP/
VMFAPP composite at a 30% loading is 31%, whereas the
value is still as high as 30% after the treatment. In spite of the
decrease in the LOI values of the PP/VMFAPP composites
after treatment, the good UL 94 ratings are maintained (most
are still V-0 rating). Therefore, it can be concluded that the
water resistance of VMFAPP is much better than APP in PP
composites.
Water leaching rates of PP/APP and PP/VMFAPP versus
content of PVA in prepolymer are shown in Fig. 5; it can be
seen that by microencapsulation, the leaching rate of FR PP
composites are reduced from 9.81 to 0.22% when the
percentage of VMFAPP is 30%. Here it is hypothesized that
the VMFAPP particle’s low solubility in comparison with
APP causes this reduction. Due to the hydrophobicity of the
VMF resin with an increase of PVA content used in the
synthesis of the prepolymer, the water leaching rates of PP/
VMFAPP show little change. So, upon exposure to water, the
comparatively better water resistance of VMFAPP in the PP
matrix would prevent the flame retardant from being
exuded, and a certain flame retardation of FR composite
can still be maintained.
The fractured surface of PP/APP and PP/VMFAPP
composites before and after water treatment was observed
by SEM, shown in Fig. 6(a), 6(b), 6(c), and 6(d). Before water
treatment, many APP grains are exposed on the surface due
to the relatively great polarity of APP. So when the
composites are exposed to water, the water molecules will
absorb on the surface of the material, and some APP grains
on the surface will first dissolve in the water, leaving some
defects on the surface. On the other hand, it can be seen that
in Fig. 6(d) after the PP/VMFAPP composite was treated
with water for 24 hr, there are still some VMFAPP grains left
32.5
V-0
V-0
32.0
V-0
LOI
31.5
V-0
V-0
31.0
V-0
V-1
V-0
V-0
30.5
V-1
Water Leaching Rate (wt%)
10
water treated
without treated
8
PP/APP
6
4
2
0
30.0
6
8
10
12
14
16
18
Content of PVA in prepolymer (g)
Figure 4. LOI values of PP/VMFAPP before and after water
treatment (508C, 24 hr) versus content of PVA in prepolymer.
Copyright # 2008 John Wiley & Sons, Ltd.
-2
0
2
4
6
8
10
12
14
16
18
20
Content of PVA in prepolymer (g)
Figure 5. Water leaching rate of PP/APP and PP/VMFAPP
(508C, 24 hr).
Polym. Adv. Technol. 2008; 19: 1914–1921
DOI: 10.1002/pat
1918 K. Wu et al.
Figure 6. SEM micrographs of fracture surfaces of the composites (1500),
(a) PP/APP; (b) PP/APP (508C water treated for 24 hr); (c) PP/VMFAPP; (d) PP/
VMFAPP (508C water treated for 24 hr). This figure is available in color online at
www.interscience.wiley.com/journal/pat
in the PP matrix. The results indicate that microencapsulation has a remarkable effect on the water resistance of APP in
the PP matrix.
Thermal analysis
The TG and DTG curves of APP and VMFAPP are shown in
Fig. 7. APP has two main decomposition processes,
beginning at about 2708C. The evolved products in the first
step are mainly ammonia and water (about 20% mass loss),
and crosslinked polyphosphoric acids (PPAs) are formed
simultaneously.15 The second stage occurs in the range of
500–7008C, which is the main decomposition process of the
APP, and weight loss is about 78%. The temperatures of
maximum mass loss rate (Tmax) for the two steps are 326 and
6258C. The residual weight of APP is 0.6% at 8008C.
In the first process, VMFAPP decomposes faster than APP
due to the esterification between APP and PVA. Above
6168C, VMFAPP is more stable than APP. The Tmax for three
steps of VMFAPP decomposition are 309, 391, and 5708C,
respectively. Moreover, VMFAPP after decomposition at
8008C left about 19.6% residue, which is much higher than
that of APP.
The TG and DTG curves of PP and the PP composites are
shown in Fig. 8. It is clearly seen that the pure PP begins to
decompose at about 2408C and has almost completely
Copyright # 2008 John Wiley & Sons, Ltd.
decomposed at 3608C. The Tmax for the decomposition is
2998C, as shown in Fig. 8 (B).
Thermal decomposition of the PP/APP composite
includes three steps. Its initial decomposition temperature
is a bit higher than that of PP. The composite PP/APP
decomposes initially at about 2508C, which is caused by the
decomposition of APP. The second step of mass loss is the
main decomposition process of the composite, and the Tmax
for this step was 3668C. The third step occurs at above 5008C
due to further decomposition of the char.
For PP/VMFAPP, its initial decomposition temperature is
similar to that of PP/APP. Moreover, due to the esterification
between the acid source and carbonization agent, PP/
VMFAPP decomposes faster in comparison with PP/APP;
the TG curve of the sample PP/APP moves to a higher
temperature in the range of 415–5958C. Above 5958C, PP/
VMFAPP is more stable than PP/APP. The increase in the
weight of the residue at high temperature may be due to
the formation of a more thermally stable carbonaceous char.
The Tmax values for the first two decomposition steps of PP/
VMFAPP are 274 and 3718C, respectively. The third step is
the decomposition of the char, and the Tmax value for this
step is 6188C. From the above results, it can be concluded that
VMFAPP is better than APP in improving the thermal
stability of the PP composite at high temperatures.
Polym. Adv. Technol. 2008; 19: 1914–1921
DOI: 10.1002/pat
Microencapsulation of APP with VMF resin
1919
Figure 7. TG (A) and DTG (B) curves of (a) APP;
(b) VMFAPP.
Figure 8. TG (A) and DTG (B) of (a) PP; (b) PP/APP; (c) PP/
VMFAPP.
Cone calorimeter study
HRR ¼ 228 kW m2. These data are consistent with the
results of flame retardation of PP composites. Moreover,
addition of VMFAPP leads to a delay in the time to ignition
and strongly prolongs the process of combustion compared
with APP in PP. From the above results, it can be concluded
that the microencapsulation can remarkably enhance the
flame retardant properties of APP in PP.
Cone calorimetry is an effective approach to compare the
combustion behavior of FR polymers. Heat release rate
(HRR) results are shown in Fig. 9. The presence of
intumescent systems in PP decreases the HRR values
significantly compared with the pure PP (the HRR peak
value of PP is 1177 kW m2).
In the case of PP/APP composite, its HRR peak is behind
that of pure PP, and its peak value is a little lower
(1064 kW m2) compared with PP. However, it is noted that
the ignition time (IT) of the PP/APP composite (24 sec) is less
than that of PP (44 sec). The reason may be due to the fact that
APP decomposes earlier than pure PP after the cone heater
irradiated the surface of the composite, and some small
volatile molecules are produced from the decomposition of
APP.
It can be seen in Fig. 9 that the HRR curve of PP/VMFAPP
is very flat and the values of HRR decrease sharply compared
with that of PP/APP. The HRR curve of the PP/VMFAPP is
typical of IFR systems. The HRR curve exhibits two peaks.
The first peak is assigned to the ignition and to the formation
of an expanded protective shield; the second peak is
explained by the destruction of the intumescent structure
and the formation of a carbonaceous residue.4 Associated
data for the PP/VMFAPP are: IT ¼ 39 sec, peak
Copyright # 2008 John Wiley & Sons, Ltd.
Figure 9. Heat release rate of PP and FR PP composites.
Polym. Adv. Technol. 2008; 19: 1914–1921
DOI: 10.1002/pat
1920 K. Wu et al.
Figure 10. Residues at the end of cone calorimeter tests of (a) PP/APP; (b) PP/
VMFAPP. This figure is available in color online at www.interscience.wiley.com/
journal/pat
To study the flame retardant mechanism of APP or VMFAPP
in polymers, we used dynamic FTIR to evaluate the thermal
degradation of the flame retardant.
For APP (Fig. 11), below 2508C, the spectra of APP present
the same peaks as the pure products taken at room
temperature; no modification of the chemical structure is
observed. Above 2508C, the bands that correspond to –NH4
(1434 cm1)16 disappear; this may be related to the elimin-
ation of NH3. As the pyrolysis temperature increases from
25 to 3008C, the 1256 cm1 peak (P –
– O) moves to a higher
wave number. The reason for the movement may be the
scission of P–O–N and the elimination of NH3. These results
demonstrate that the evolved products in the first step are
mainly ammonia and water, and crosslinked PPA are formed
simultaneously. Moreover, the 1019 cm1 spectral peak
corresponds to the symmetric vibration of PO2 and of
PO316 which allows us to determine the stability of the PPAs.
From 5508C upwards the change of the peaks at 1019 cm1
can be explained by the further decomposition of PPA, which
is in agreement with the changes in the absorption range
(3100–3300 cm1) of the O–H or N–H.12,16
For VMFAPP, its thermal degradation process is more
complicated than that of APP. It can be seen from Fig. 12 that
the strong absorption around 3200 cm1 gradually disappears below 3008C; this may be caused by the elimination
of NH3 of APP and dehydration of APP and PVA. This
viewpoint can be verified by the movement of 1080 cm1
peak (P–O–C).5,16 Moreover, we should notice the absence of
the absorptions of 1560, 1504, and 1339 cm1 which are due to
Figure 11. Dynamic FTIR spectra of APP with different
pyrolysis temperatures.
Figure 12. Dynamic FTIR spectra of VMFAPP with different
pyrolysis temperatures.
The appearance of FR PP composite residues at the end of
cone calorimeter tests is shown in Fig. 10. It is clear that there
is almost no residue left at the end of the cone calorimeter test
for the PP/APP composite. On the other hand, the surface of
the PP/VMFAPP residue is covered with an expanded char
network. The residue left by PP/VMFAPP is mainly formed
of thick black char, and the char is better than that of PP/APP
in protecting the underlying materials. The results indicate
that a good and coherent char can prevent the heat transfer
and flame spread, and thus protect the underlying materials
from further burning.
Thermal degradation of APP and VMFAPP
Copyright # 2008 John Wiley & Sons, Ltd.
Polym. Adv. Technol. 2008; 19: 1914–1921
DOI: 10.1002/pat
Microencapsulation of APP with VMF resin
5
the ring vibration of melamine groups at about 3508C; this
can be explained by the fact that melamine is disassociated
and evaporates at higher temperatures. It is interesting to
find that between the range of 300 and 6008C, the shapes of
the spectra show few changes. This may be related to
the formation of stable structures containing P–O–P and
P –– O (1080, 1020, 880 cm1) complexes. Between the same
temperatures, it is clear from Fig. 11 that APP decomposes
further. These dynamic thermal degradation data give
positive evidence for the flame retardant mechanism: the
microcapsule with a shell composed of VMF can form a more
stable charred layer in the condensed phase compared with
APP during burning of polymer materials. This char layer
slows heat and mass transfer between the gas and condensed
phases and prevents the underlying polymer from further
degradation. From these results, it can be concluded that the
shell can be used as a carbonization agent and blowing agent.
These results are in agreement with the data of TG, LOI, UL
94, and cone calorimetry.
CONCLUSIONS
In this work, APP was microencapsulated with VMF resin by
an in situ polymerization method. Microencapsulated APP
(VMFAPP) decreases its water absorption and increases its
water resistance in PP matrix. The LOI values of the PP/
VMFAPP composites increase compared with those of the
PP/APP composites at the same loading. It has been found
that APP used alone in PP does not reach the UL 94 V-0 rating
and VMFAPP used alone in PP can reach V-0 at the additive
level of 30%. Moreover, after water treatment at 508C for
24 hr, the composites containing VMFAPP could still
maintain good flame retardant properties. These results
show that microencapsulation gives better water resistance
and flame retardance compared with APP in PP.
The cone calorimeter results show that VMFAPP is an
effective flame retardant in PP compared with APP owing to
the shell which can be used as blowing and carbonization
agent. It is observed from the TG and dynamic FTIR study
that VMFAPP can form a more stable charred layer which
can prevent the underlying polymer from further combustion in the condensed phase compared with APP in PP.
Acknowledgments
The financial support from the National Natural Science
Foundation of China (No. 20776136), the program for New
Century Excellent Talents in University, and National 11th
Five-year Program (2006BAK01B03, 2006BAK06B06, and
2006BAK06B07) is acknowledged.
Copyright # 2008 John Wiley & Sons, Ltd.
1921
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