chapter 3 investigation of catalytic activity of...
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66
Investigation of Catalytic Activity of Mesoporous Silica
Chapter 3
INVESTIGATION OF CATALYTIC ACTIVITY OF MESOPOROUS
SILICA
3.1. Introduction
Natural and synthetic polymers have been used as matrices for various biomedical
applications such as drug delivery, gene delivery, tissue engineering, etc [1–5].
Commonly used synthetic polymers such as polyethylene (PE), polypropylene (PP) and
polystyrene (PS) have limited biomedical applications due to their non–biodegradability
and immunogenicity. Hence, biodegradable polymers such as polyesters,
polyphosphazenes, polyanhydridres, etc. are preferred for use in biological systems as
drug delivery vehicles, wound closure dressings, prosthetic implants and three–
dimensional porous scaffolds for tissue engineering applications [6–12]. Biodegradable
polyesters such as poly(lactic acid), poly(glycolic acid), poly(ε–caprolactone),
poly(hydroxy butyrate) and their copolymers have received considerable attention for
biomedical applications due to their biocompatibility [13–17]. These polymers undergo
degradation in vivo via hydrolytic, enzymatic or oxidative hydrolysis. It is essential that
the products of degradation are not toxic and can either be taken up the cells (resorbable)
or removed from the body (eliminable) by natural metabolic pathways. Apart from
biocompatibility, the polymer should also be easy to process and should possess the right
amount of hydrophilicity to favour cell adhesion [18].
Though many types of polyesters have been synthesized over the years, there have been
limited attempts to develop polyesters that can find applications in vivo. One of the
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Investigation of Catalytic Activity of Mesoporous Silica
major challenges in aliphatic polyester synthesis has been the separation of reaction
products from the liquid phase. Tremendous efforts have been directed to synthesize an
ideal catalytic system, which combines the advantages of both homogeneous and
heterogeneous catalysts. Although solid supports such as zeolites, alumina and metals
have been used as heterogeneous catalysts, they are usually accompanied with a
significant loss in activity and selectivity [17–23]. Conventional catalysts for polyester
synthesis include tetrabutyl titanate, H2SO4, HNO3, SnCl2.2H2O and organometallic
compounds which are highly corrosive and hazardous to the environment and our body
[24–28].
Materials with high surface area are invaluable for catalytic applications as they provide
numerous active sites for the reaction. Further, the use of a high surface area
heterogeneous catalyst enables higher conversion as well as makes it convenient to
separate the product with high purity unlike conventional homogeneous catalysts.
Mesoporous materials belong to a class of high surface area nanostructures that have
elicited immense interest for their highly efficient catalytic properties and have been used
for catalyzing a wide range of reactions from Freidel–Crafts acylation to Knoevenagal
reactions [29–36]. Over the past decade, many types of mesoporous materials have been
developed which include mesoporous carbon, mesoporous titania, mesoporous silica,
mesoporous alumina, mesoporous zinc oxide etc. [37–41]. Among these, mesoporous
silica with different pore dimensions, morphology and surface area have been developed
and extensively used as a heterogeneous catalyst for a wide range of reactions. Table 3.1
summarizes the various reactions that have been efficiently catalysed using mesoporous
silica when compared with conventional catalysts.
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Investigation of Catalytic Activity of Mesoporous Silica
Table 3.1: Mesoporous silica catalyzed reactions Mesoporous material Reaction Reference
i. Poly(4–methyl vinylpyridinium hydroxide) / SBA–15 Composite
ii. PVAm / SBA–15
Knoevenagel Reaction
[42] [43]
Aminopropyl–functionalized SBA–15 Claisen–Schmidt condensation [44]
i. SBA–15 ii. Primary amine and sulfonic acid
functionalized SBA–15 Aldol condensation [45]
[46]
SBA–15 supported silicotungstic acid Baeyer–Villiger Oxidation [47]
Sn–SBA–15 Baeyer–Villiger oxidation and Meerwin–Pondorf–
Verly reduction [48]
Ionic liquid–functionalized SBA–15
i. Cycloaddition of carbon dioxide (CO2) with epoxide
ii. Aza–Michael addition iii. Biginelli reaction of
aldehyde, ethyl acetoacetate and urea
[49]
SBA–15–supported ionic liquid–Pd(OAc)2 Heck reaction [50]
Amino–functionalized SBA–15 Henry reaction [51] Au nanoparticles supported on periodic
mesoporous organosilica (PMO) Ullmann reaction [52]
Noble metal nanoparticles stabilized in SBA–15
Suzuki–Miyaura coupling reaction [53]
Vanadium oxide catalyst supported on MCM–41, MCM–48, silica
Hydroxylation of benzene to phenol [54]
SBA–15 FischerTropsch synthesis [55]
Sulfonic Acid Functionalized SBA–15 Hantzsch four component condensation reaction [56]
SBA–15
• Michael addition • Wohl–Ziegler reaction • Acylation • Heck reaction • Tishchenko reaction • Diels–Alder reaction • Reformatsky • Luche reaction • Oxidative coupling • Reaction, synthesis of
chalcones • Synthesis of
[57]
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Investigation of Catalytic Activity of Mesoporous Silica
dihydropyrimidinones
Vanadyl (IV) Acetylacetonate Anchored SBA–15 Catalyst
Oxidative Cleavage of C=C Bond of Styrene and Its
Derivatives [58]
Ru/SBA–15
Hydrogenation of benzene to cyclohexene [59]
MCM –41, 48, SBA–15 FischerTropsch synthesis [60] V–HMS, V–MCM –41 and V–SBA –15
Oxidative dehydrogenation
(ODH) of ethane . [61]
Co–SBA–15 Aerial oxidation of ethylbenzene [62]
Primary and quaternary amine, sulfonic acid, and amino acid,
especially l–proline, functionalized SBA–15 & 16
• Knoevenagel and Henry reactions
• Claisen–Schmidt condensation
• Diethyl malonate addition reactions
[63]
The immense popularity of the mesoporous silica stems from its ease of synthesis,
tunable properties, excellent hydrothermal stability and inertness that enables it to
catalyse a broad range of reactions. It is evident that mesoporous silica with ordered
mesopores between 2–50 nm, high surface area, large pore volume and functionalities
[64], may also serve as a potential catalyst for polycondensation reactions. Recently, a
type of mesoporous silica, MCM–41, has been employed as a highly ordered catalyst
support to prepare dendrimers, a class of hyper–branched polymers [65]. Similarly, we
hypothesize that SBA–15, a class of mesoporous silica, which has larger pore size and
higher thermal stability may serve as a better catalyst for polymerization reactions [66].
Therefore, the aim of the current study was to synthesize for the first time three
polyesters namely poly(butylene succinate) (PBSu), poly(butylene sebacate) (PBSe) and
poly(butylene pimelate) (PBPi) using the mesoporous catalyst, SBA–15 with different
surface area and compare the products obtained using a homogeneous catalyst,
SnCl2.2H2O.
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Investigation of Catalytic Activity of Mesoporous Silica
The choice of the polymers was based on the fact that these are not only biodegradable
due to the ester links present, but the products of degradation can be either resorbed by
the body or eliminated without producing any toxic effects. Poly(butylene pimelate) has
been chosen for synthesis since it can degrade by hydrolysis and the degradation
products, namely 1, 4–butane diol and pimelic acid are non–toxic to the biological
system. The body eliminates 1, 4–butane diol after conversion to γ–hydroxy butyrate and
pimelic acid is a precursor of biotin (vitamin B7) [67]. L–lysine, an essential amino acid
that plays an important role in calcium absorption and suppresses viral infections [68].
The degradation products of poly(butylene succinate) are 1, 4–butane diol and succinic
acid. While 1,4–butane diol can be easily eliminated from the body, succinic acid is an
intermediate in the tricarboxylic acid (TCA) cycle, which can be converted to fumarate
by succinate dehydrogenase [69].
An interesting prospect for this polymer in drug delivery applications stems from the fact
that the brain expresses high levels of succinate dehydrogenase thereby enabling faster
and efficient degradation of this polymer. Hence, this polymer may be further explored
for brain targeted drug delivery applications. Poly(butylene sebacate) on degradation
produces 1,4–butane diol that can be easily eliminated and sebacic acid, which can be
metabolized to acetyl CoA and succinyl CoA [70].
The synthetic route and catalyst employed influences the molecular weight and purity of
the product, which is vital in determining the nature and magnitude of biological
response towards the polymer. Among the polyesters chosen, reports on the synthesis of
PBSu using direct polycondensation of dicarboxylic acid with diol in the presence of
hafnium (IV) or zirconium (IV) salts and reusable rare–earth triflates are available [36,
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Investigation of Catalytic Activity of Mesoporous Silica
37]. Reports on enzymatic synthesis of poly(butylene succinate) and poly(butylene
sebacate) are also available in literature [71, 72]. However, the process is time
consuming and the use of lipase enzyme limited the reusability and recovery of the
catalyst [73]. Poly(butylene succinate) has also been formed in the presence of other
homogeneous catalysts like titanium tetraisopropoxide and SnCl2.2H2O [74, 75]. The
synthesis of poly(butylene pimelate) has not been reported elsewhere. However, apart
from a report on the polymerization of grafted aniline using mesoporous SBA–15, no
reports are available on the catalytic efficiency of mesoporous silica on aliphatic
polyester synthesis including the above mentioned three polymers, thus making this
attempt the first of its kind [76].
3.2. Materials & Methods
3.2.1. Materials
Chloroform, methanol, tin (II) chloride, succinic acid, pimelic acid, sebacic acid and 1,4–
butane diol were purchased from Merck, India. All chemicals were of GR grade and
were used as such without any further purification.
3.2.2. Synthesis of polyesters
A typical synthesis of the aliphatic polyesters was carried out as follows. The chosen
polyester was synthesized by taking 5.1 mM of 1,4–butanediol and 5 mM of the
dicarboxylic acid (succinic acid or pimelic acid or sebacic acid) in a round–bottom flask.
The mixture was refluxed at 140°C with the catalyst (SnCl2.2H2O or different
mesoporous silica – SW, SEG, SG) for 24 h with continuous stirring in a nitrogen
atmosphere. The Dean–Stark apparatus was used to remove water from the reaction
mixture. After cooling to room temperature, the polymer obtained was dissolved in
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Investigation of Catalytic Activity of Mesoporous Silica
chloroform and filtered to separate the catalyst. The polymer was then reprecipitated in
excess methanol, filtered, dried under vacuum and characterized. The general reaction
scheme for formation of the polymer is shown below.
Scheme 3.1: Reaction scheme for the synthesis of polyester
3.2.3. Characterization of polymers
Fourier transform infrared spectroscopy (FT–IR) (Spectrum 100, Perkin Elmer, USA)
was used to analyze the polymer samples. FT–IR analysis was performed between 4000
and 450 cm–1 at a resolution of 4 cm–1 averaging 10 scans. The moisture–free polymer
sample was pelletized with KBr (IR grade, Merck) and analysed.
X–ray diffraction was used to characterize the crystallinity of polymer samples. The
samples were finely ground using a mortar and pestle and the fine powder was mounted
on a polymer slide and analyzed using an X–ray diffractometer (D8 Focus, Bruker,
Germany). The analysis was carried out from 10° to 60° in steps of 0.01° and at the scan
rate of 0.5° per step. Cu–Kα radiations were used to irradiate the sample.
Proton nuclear magnetic resonance spectroscopy was used to ascertain the structure of
the synthesized polymers. The analysis was done using CDCl3 as solvent and TMS as
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Investigation of Catalytic Activity of Mesoporous Silica
internal reference and the spectrum was recorded in a 300 MHz NMR spectrometer
(Bruker, Germany).
The hydrophobicity of the polymer films were determined using contact angle
measurements. The contact angle measurements were made between a water droplet and
the polyester film using Goniometer (Ramehart, USA). Initially, a polymer film was
prepared by applying a pressure of 100 kg/cm3 following which it was placed on a
sample holder. A water droplet was placed carefully on the prepared film and viewed
through a microscope. The contact angle was measured at constant time intervals and the
images were captured using a CCD camera.
Molecular weights of the synthesized polyesters were analyzed by gel permeation
chromatography (1200 Series, Agilent GPC, USA) in tetrahydrofuran (HPLC grade,
Merck) solvent with the sample concentration of 1 wt%. The sample (20 μL) was
injected into the column at a flow rate of 1 mL/min using an isocratic pump. The
molecular weight and molecular weight distribution of polymer samples were calculated
from a reference calibration curve obtained using polystyrene standards.
The phase transitions of the polymer samples were analyzed using differential scanning
calorimetry (DSC Q20, TA instruments, USA). Nitrogen was used as a purge gas with a
flow rate of about 20 cm3/minute. Both temperature and heat flux were calibrated
initially and about 20 mg of the samples were analyzed in the central region of the
injection parts. All the experiments were performed at a ramp rate of 10°C/minute,
starting from room temperature. The first run was eliminated to avoid interference from
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Investigation of Catalytic Activity of Mesoporous Silica
any moisture present and the third run was recorded to reveal the melting behavior of
synthesized polyesters.
3.2.4. Formation of poly(butylene succinate), poly(butylene pimelate) and poly(butylene
sebacate) microspheres
Polyester microspheres were prepared by the single emulsion technique. 0.2 g of
synthesized polymer was dissolved in 5 mL of chloroform and this was added drop wise
to 2% w/v poly(vinyl alcohol) (Sigma–Aldrich Chemicals, USA) under constant stirring
at 500 rpm. After 4 h, the microspheres formed were filtered and air–dried.
Figure 3.1: Polymer microspheres preparation through single emulsion technique
The morphology of the prepared polymer microspheres was studied using a cold field
emission scanning electron microscope (FE–SEM, JSM 6701F, JEOL, Japan). Initially
the samples were sputter coated with a thin layer of platinum. The applied voltage was
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Investigation of Catalytic Activity of Mesoporous Silica
maintained at 3 kV with a working distance of 6 mm and the images were recorded using
secondary electron detector.
3.3. Results & Discussion
3.3.1. Influence of catalyst on the polymer yield and molecular weight
Table 3.2 shows the properties of the polymers obtained using different mesoporous
materials (SW, SEG & SG) as catalyst compared to conventional catalyst such as tin
chloride (SnCl2.2H2O).
Table 3.2: Influence of conventional catalyst (SnCl2.2H2O) and mesoporous catalyst (SW) on the yield of PBSu, PBPi & PBSe.
Synthesized polyester
Physical parameters
Catalyst SnCl2.2H2O SW SG SEG
PBSu
% yield 54 90 61 42 ηint 0.05 0.38 0.25 0.08
Molecular weight (g/mol)
Mn 5466 10041 9162 398
Mw 5969 21954 10539 722
Mw/Mn 1.1 2.2 1.2 1.8
PBPi
% yield 6 25 23 10 ηint 0.08 0.55 0.32 0.15
Molecular weight (g/mol)
Mn 1098 1899 1249 776
Mw 1112 5955 1326 1602
Mw / Mn 1.1 3.1 1.1 2.1
PBSe
% yield 25 40 32 15 ηint 0.06 0.65 0.35 0.2
Molecular weight (g/mol)
Mn 1317 8809 7974 841
Mw 1340 10857 9727 1269
Mw / Mn 1.0 1.2 1.2 1.5 PBSu: Poly(butylene succinate); PBPi: Poly(butylene pimelate) &
PBSe: Poly(butylene sebacate).
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Investigation of Catalytic Activity of Mesoporous Silica
It was observed that among the four catalysts used, SW showed the maximum catalytic
efficiency for the synthesis of the three polymers. Also, the molecular weight of the
synthesized polymers obtained (Mn and Mw) and the corresponding intrinsic viscosity
(ηint) was highest for SW followed by SG. The catalytic efficiency of SW and SG are
higher than the conventional catalyst (SnCl2.2H2O). This difference may be attributed to
the advantages provided by a heterogeneous catalyst with high surface area that offers
greater number of active sites for the reaction to occur. A homogeneous catalyst such as
tin chloride does not possess these characteristics and hence the observed difference in
catalytic efficiency. Interestingly, the catalytic efficiency of the mesoporous silica
synthesized using ethylene glycol as solvent (SEG) was found to be much lower when
compared to the other two mesoporous catalysts. The order for catalytic efficiency for
the three mesoporous catalysts was found to be SW > SG > SEG. This difference in
catalytic efficiencies may not be attributed to an increase in surface area, as SEG has the
maximum surface area (Chapter 2) and however, least catalytic activity. Hence, some
other parameter seems to have an implementing role in catalytic activity of the
mesoporous samples. The transmission electron micrographs of the three mesoporous
samples reveal that both SW and SG have ordered hexagonal pores while SEG has
distorted hexagonal pores (Figure 2.6). It is therefore most likely that the pore
morphology and order have a more pronounced effect on catalysis than surface area. The
relatively high molecular weights of the polymers obtained using SW can also be
attributed to the presence of continuous tubular pores, which is absent in SEG. Similarly,
SG also has more number of ordered tubular pores and pore morphology resulting in
higher yield and molecular weight of the polymers than SEG (Figures 2.5 & 2.6).
However, the yield of the polymers and their molecular weight obtained using SG are
lower than those observed with SW. Therefore, neither surface area nor pore order might
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Investigation of Catalytic Activity of Mesoporous Silica
be the sole determinants for this difference. The 29Si NMR reveals that the SG sample
has lesser number of free –OH when compared with SW (Figure 2.7). This indicates the
importance of surface functionalities in polycondensation catalysts (Scheme 3.2).
O
O
O
Si OH (R)nHO OH (R)mC CHO OH
O O+ +
O
O
O
SiOH
(R)nO O(R)mC C
HOOH
O O
O
O
O
SiOH
(R)nOO
(R)mC C OHO O
H
O
O
O
SiOH
(R)nO
O
(R)mC C
O O
(R)n
O
O(R)mC C O
O O
n-1
O
O
O
SiOH
(R)nO O(R)mC C O
O O
n
+
-H2O
-(n-2)H2O
SW Polyester Scheme 3.2: Mechanism of polyester formation with heterogeneous mesoporous silica
catalyst
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Investigation of Catalytic Activity of Mesoporous Silica
Thus our results demonstrate that apart from surface area, pore order and surface
functionalities have a major role in imparting a high degree of catalytic efficiency to
mesoporous catalysts for polycondensation reactions. Based on the results obtained,
polymer samples obtained from SW were characterized further and compared with those
obtained using conventional homogeneous catalyst, SnCl2.2H2O.
3.3.2. Characterization of polymers
The FTIR spectra of PBSu, PBPi and PBSe samples synthesized using different catalysts
are shown in Figure 3.2, 3.3 & 3.4 respectively. The presence of absorption bands at
2800, 1740, 1480, 1100 and 780 cm–1 indicate the formation of polyester. The band at
2800 cm–1 represents –CH2– stretching, 1740 and 1480 cm–1 indicate the –C=O
stretching and –CH2– bending respectively, while the bands at 1100 and 780 cm–1
represent the –O–C–C– stretching and –CH2– rocking respectively. Most of these bands
are found in all samples, but the band at 780 cm–1 is very weak in the case of PBSu and is
absent in the other two polymer samples obtained using SnCl2.2H2O. This band is
usually associated with molecules having multiple –CH2– groups. It is likely that the
sample obtained with SnCl2.2H2O does not have a high molecular weight or is only an
oligomer.
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Investigation of Catalytic Activity of Mesoporous Silica
4000 3500 3000 2500 2000 1500 1000 500
Wavenumber (cm-1)
%T
Figure 3.2: FT–IR spectra of poly(butylene succinate) synthesized with A)
SnCl2.2H2O; B) SW; C) SEG & D) SG catalyst
4000 3500 3000 2500 2000 1500 1000 500
Wavenumber (cm-1)
%T
Figure 3.3: FT–IR spectra of poly(butylene pimelate) synthesized with A)
SnCl2.2H2O; B) SW; C) SEG & D) SG catalyst
A
B
C
D
A
B
C
D
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Investigation of Catalytic Activity of Mesoporous Silica
4000 3500 3000 2500 2000 1500 1000 500
Wavenumber (cm-1)
%T
Figure 3.4: FT–IR spectra of poly(butylene sebacate) synthesized with A)
SnCl2.2H2O; B) SW; C) SEG & D) SG catalyst
Figure 3.5 shows the powder XRD of polyesters namely poly(butylene succinate),
poly(butylene pimelate) and poly(butylene sebacate) synthesized using SW and
compared with conventional homogeneous catalyst, SnCl2.2H2O. The XRD pattern of
the PBSe polyester synthesized in the presence of SnCl2.2H2O exhibits a semi–crystalline
nature which may be attributed to its low molecular weight (Figure 3.5E), while all the
polyesters synthesized using mesoporous SW show predominantly an amorphous nature
which can be attributed to the formation of high molecular weight polyesters.
A
B
C
D
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Investigation of Catalytic Activity of Mesoporous Silica
10 20 30 40 50
F
E
2 theta (deg.)
D
C
B
A
Figure 3.5: XRD of poly(butylene succinate) (A & B), poly(butylene pimelate) (C
& D) and poly(butylene sebacate) (E & F) synthesized with SnCl2.2H2O (A, C & E) and SW (B, D & F) as catalyst
The 1H–NMR spectra of the PBSu, PBPi and PBSe samples obtained using homogeneous
and mesoporous SW catalysts are shown in Figure 3.6, 3.7 & 3.8 respectively. The
structure of PBSu indicates that it possesses three sets of magnetic equivalent protons
denoted as a, b and c in the inset of Figure 3.6. The proton NMR of PBSu shows three
signals at δ 1.62, δ 2.85 and δ 4.13 corresponding to A, B and C set of equivalent protons
respectively (Figure 3.6). The NMR shows no difference in the products obtained using
SnCl2.H2O and mesoporous SW catalysts.
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Investigation of Catalytic Activity of Mesoporous Silica
5.0 4.5 4.0 3.5 3.0 2.5 2.0 1.5 1.0ppm
SW B
O
OO
OO
n
A
AB
B
C
C
C
SnCl2.2H2O
A
Figure 3.6: 1H–NMR of PBSu synthesized with SnCl2.2H2O & SW as catalyst
In the case of PBPi, five sets of magnetically equivalent protons are present which are
denoted as A, B, C, D and E (Inset of Figure 3.7). It is seen that the samples obtained
using 0.1 g of SW show peaks at δ 1.29, δ 1.57, δ 1.65, δ 2.25 and δ 4.08 corresponding
to the protons denoted by A, B, C, D and E respectively. However, only the peak at δ
1.57 is prominent in the samples obtained using tin chloride catalyst, implying
incomplete polymerization and this is in agreement with the FTIR data (Figure 3.3).
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Investigation of Catalytic Activity of Mesoporous Silica
4.5 4.0 3.5 3.0 2.5 2.0 1.5 1.0
O
nA E
B
D D
O
O
O
O B
C C E
SW
A
DE C
B
SnCl2.2H2O
ppm Figure 3.7: 1H–NMR of PBPi synthesized with SnCl2.2H2O & SW as catalyst
The structure of PBSe indicates that it has five sets of magnetically equivalent protons
denoted as A, B, C, D and E (inset of Figure 3.8). Figure 3.8 shows that the polymer
sample obtained using SW exhibits five signals at δ 1.3, δ 1.6, δ 1.7, δ 2.3, & δ 4.1
corresponding to A, B, C, D and E respectively. The polyester synthesized with tin
chloride shows an additional low intensity signal at δ 3.7, which indicates the presence of
small amounts of –OH, most likely from butane diol. This indicates that there is
incomplete polymerization with this catalyst.
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Investigation of Catalytic Activity of Mesoporous Silica
4.5 4.0 3.5 3.0 2.5 2.0 1.5 1.0
O OH
n
A
A
B
D
DO
OBC
C
E
O
O
E
A
A F
SW
SnCl2.2H2O
D
F
EC
B
A
ppm Figure 3.8: 1H–NMR of PBSe synthesized with SnCl2.2H2O & SW as catalyst
The hydrophobicity of the polyesters was determined using a goniometer and figure 3.9
shows the contact angles of PBSu, PBPi and PBSe at various time intervals.
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Investigation of Catalytic Activity of Mesoporous Silica
Figure 3.9: Contact angle measurement of polyesters synthesized with SW as catalyst
The absolute contact angles for PBSu, PBPi and PBSe were calculated to be 60°, 68° and
72° respectively. The higher contact angle represents a greater hydrophobicity and as
expected the poly(butylene sebacate) polymer exhibited the maximum hydrophobicity
when compared with the other two polyesters. Thus, greater number of methylene
groups and a corresponding increase in the alkyl chain length confers greater
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Investigation of Catalytic Activity of Mesoporous Silica
hydrophobic character to the polymers as is evident from the contact angle data for the
three polymers which increase in the order PBSu < PBPI < PBSe. It was also observed
that over a period of nine minutes, the contact angle decreased from 60˚ to 10˚ for PBSu,
68˚ to 8˚ for PBPi and 72˚ to 5˚ for PBSe. This may be attributed to the pores present in
the surface of the polymer that permit diffusion of water droplet. The contact angle of a
polymer film has a key role in determining the degradation rate of the polymer.
Thermal analysis (DSC) data of synthesized polyesters with tin chloride and mesoporous
silica (SW) catalysts are shown in Figure 3.10. The melting point of the PBSu
synthesized using tin chloride and mesoporous silica (SW) is 97.5˚C and 96˚C
respectively. It is observed that when the SnCl2.2H2O was used as catalyst, a sharp
melting peak with higher heat flow is obtained (Figure 3.10 A). In contrast, the polymer
obtained using mesoporous silica exhibits a broad melting pattern indicating formation of
a higher molecular weight product with greater amorphous character. This is in
concurrence with the molecular weight data and spectroscopic analysis of the polymer
samples.
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Investigation of Catalytic Activity of Mesoporous Silica
70 75 80 85 90 95 100
SW
SnCl2.2H2O
AEn
do
Temperature (oC)
2
45 50 55 60 65 70
Endo
Temperature (oC)
SW
SnCl2.2H2O
B
50 55 60 65 70
Endo
Temperature (°C)
CSW
SnCl2.2H2O
Figure 3.10: DSC thermograms of polyesters [A] PBSu; [B] PBPi; and [C] PBSe
synthesized with SnCl2.2H2O & SW as catalyst
In the case of PBPi (Figure 3.10 B), it is observed that when SnCl2.2H2O was used as
catalyst, a sharp melting peak with higher heat flow is obtained at 54.1°C, while the
polymer formed using SW, a broad melting peak between 58.6°C and 59.3°C is observed
which may be attributed to the formation of a higher molecular weight polymer with
greater amorphous character due to better polymerization. A similar observation can be
made for PBSe, where the polymer formed using SW shows a broader signal around
60°C while a sharper signal is obtained around the same temperature for the polymer
formed using tin chloride (Figure 3.10 C).
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Investigation of Catalytic Activity of Mesoporous Silica
3.3.3. Fabrication of polyester microspheres
The molecular weight and hydrophobicity of a polymer are responsible for formation for
micro– and nanospheres that can find applications as drug carriers. As the polyesters
formed using SW show higher molecular weight when compared to those formed using
other catalysts, an attempt was made to check the feasibility of transforming them into
polymer microspheres using single emulsion technique. Figure 3.11 shows the scanning
electron micrographs of the polymer microspheres formed using the three different
polyesters synthesized using SW. The conditions for microsphere formation were
identical in all three cases.
A B C
Figure 3.11: Scanning electron micrographs of microspheres formed from [A] PBSu; [B]
PBPi and [C] PBSe
Among the three polymers, PBSu formed smoother microspheres while the roughness
increased for PBSe. In the case of PBPi, macroporous spheres were obtained. This
difference in the surface morphology of the spheres can be attributed to the difference in
molecular weight of the polymers. The PBSu polymers had the largest molecular weight
among the three polymers followed by PBSe while PBPi had the least molecular weight.
Therefore, the viscosity and rate of solvent evaporation from the surface of the
microspheres will vary resulting in the observed differences in surface morphology.
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Investigation of Catalytic Activity of Mesoporous Silica
These results indicate the significance of polymer molecular weight for microsphere
formation. Very low molecular weight polymers are difficult to be transformed in to
microspheres, which will in turn limit the applicability of the polymer in the biomedical
field.
3.3.4. Characterization of mesoporous silica after polymerization
The structural and textural properties of SW were analyzed post catalysis to ascertain any
alterations in the pore order and morphology. Figure 3.12 shows the FT–IR and nitrogen
adsorption–desorption isotherm of the SW post catalysis followed by 6 hours of
calcination at 550°C. The FT–IR shows no shift in the bands for mesoporous silica
before and after catalysis. Similarly, the BET surface area and BJH analysis of pore size
of the mesoporous silica are 620 m2/g and 8 nm respectively, which confirms that there is
no alteration in the structure and texture of mesoporous SBA–15 silica due to the
catalysis reaction conditions.
B
4000 3500 3000 2500 2000 1500 1000 500
2
Wave number (cm-1)
1
%T
A
Figure 3.12: [A] FT–IR spectra and [B] nitrogen adsorption–desorption isotherm of calcined heterogeneous SW, which was used already as a catalyst for polymerization
90
Investigation of Catalytic Activity of Mesoporous Silica
3.4. Conclusions
The mesoporous SBA–15 silica has been successfully demonstrated to act as a catalyst
for polycondensation reactions in this study. An interesting aspect that comes to the fore
from this study is that high surface area alone is not the sole contributor for effective
catalysis, but high pore order and surface functionalities also play a key role in improving
the catalytic efficiency towards polycondensation reactions. The mesoporous SBA–15
synthesized using water solvent integrates all these properties and hence was found to
result in relatively higher molecular weight polymers with better yield when compared
with the other mesoporous counterparts used for the study. The work also resulted in the
synthesis and characterization of poly(butylene succinate), poly(butylene pimelate) and
poly(butylene sebacate) of which the poly(butylene pimelate) is reported for the first
time. These polymers were successfully fabricated into microspheres which may be
explored in future for potential biomedical applications especially in the field of drug
delivery.
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