1. Introduction
Poly(vinyl esters) (PVEs) consist a valuable class of polymeric materials [
1], mainly for two reasons. The first one has to do with the numerous applications of these materials in the industrial sector, involving their employment as elastomers, plastics, fibers, coatings, paints, additives, adhesives, textiles, cosmetics, etc. [
2,
3,
4,
5,
6,
7] This broad range of applications is associated with the correlation between the structure and the properties of the PVEs. Depending on the nature of the side ester-group (aliphatic with various carbon atoms, aromatic, alicyclic, olefinic etc.) the PVEs can be either hydrophilic or hydrophobic, either amorphous or semi-crystalline, either liquid-like, or waxy or solid materials etc. [
8,
9,
10,
11,
12,
13,
14,
15,
16,
17,
18] The second reason has to do with the fact that PVEs can be precursors for the production of poly(vinyl alcohol) (PVA), which is a benchmark water-soluble polymer demonstrating non-toxicity, non-carcinogenic properties and possibilities for bio-conjugation for therapeutical applications. [
19,
20,
21] Therefore, it can be applied as a valuable biomaterial in pharmacological applications. [
22,
23,
24] The transformation of PVEs to PVA is conducted through hydrolysis of the ester group. The nature of the side group affects the kinetics of hydrolysis ranging from a few minutes to several hours. Under these conditions, intermediate degrees of hydrolysis can be reached leading to products with complex behaviour in aqueous solutions. [
25]
The most well-known member of the PVEs polymer family is poly(vinyl acetate) (PVAc). It is the most widely used precursor for the synthesis of PVA and numerous studies have been devoted to the synthesis of this material and its copolymers with other VEs or other monomers. [
26,
27] Much less work has been devoted to the synthesis and the study of the solution and solid-state properties of other members of the PVEs family of polymers. [
28,
29,
30,
31,
32]
The polymerization of VEs is feasible only through radical polymerization. The conventional radical polymerization, although straightforward in its applications, suffers various disadvantages. These include the lack of control over the molecular weights of the produced materials, the high polydispersity, Ð, values, the inability to produce pure end-functionalized polymers and the very limited possibilities to synthesize complex macromolecular architectures, since the technique is accompanied by several termination and transfer reactions. [
33] Especially, for VAc extended studies have been performed to reveal the presence of chain transfer reactions to monomer and polymer leading to the formation of branched structures and the appearance of regio-irregularities with increased head-to-head linkages. [
34,
35,
36,
37] For this reason, the polymerization of VEs was not a hot topic in Polymer Chemistry for many years. However, the developments in controlled radical polymerization methodologies opened new horizons for the controlled polymerization of VEs and offered the possibility to manipulate macromolecular engineering towards the synthesis of tailor-made polymers. Among these approaches, nitroxide-mediated, atom transfer radical, iodine transfer, organostibine-mediated, vanadium-mediated and cobalt-mediated polymerization techniques have been employed. [
38,
39,
40,
41,
42,
43,
44,
45] Although relative success has been reported in several cases these methods present several drawbacks rendering their universal application problematic. By far the most successful polymerization technique for VEs is the Reversible Addition Fragmentation Chain Transfer (RAFT) methodology. It was proven to be the suitable tool towards the synthesis of controlled structures in terms of both the molecular characteristics and the copolymer topology or macromolecular architecture in combination with other polymerization techniques and a variety of monomers. [
46,
47]
In this work, the synthesis of amphiphilic block copolymers of N-vinyl pyrrolidone (NVP) and various vinyl esters, PNVP-
b-PVEs, including vinyl butyrate (VBu), vinyl decanoate (VDc) and vinyl stearate (VSt) is described through RAFT approaches. These materials are expected to provide very interesting properties. On the one hand, PNVP is an amorphous polymer with a high Tg value (equal to 187
oC, depending on the humidity), soluble in both aqueous solutions and in organic solvents, without showing lower critical solution temperature (LCST) [
48,
49,
50,
51,
52] and on the other hand PVBu and PVDc are also amorphous polymers with low Tg values (-5
oC for PVBu and -45
oC for PVDc), whereas PVSt is a semicrystalline polymer with Tm=52-57
oC. [
54,
55,
56]
All monomers, NVP and VEs, are considered to belong to the category of less activated monomers (LAMs) in RAFT polymerization. The monomers are classified in two families in RAFT polymerization. They belong either to the more activated (MAMs) or to the less activated monomers (LAMs). The key parameter differentiating these two groups of monomers is their ability to stabilize radicals [
47,
57]. LAMs have a double bond, which is connected to a saturated carbon atom or conjugated to a lone pair on oxygen or nitrogen. Therefore, the polymerization of these monomers leads to the formation of poorly stabilized radicals. On the other hand, the group of MAMs includes monomers, where the double bond is conjugated to an unsaturated system, such as nitrile, aromatic ring or carbonyl groups. Consequently, these monomers form highly stabilized radicals, due to extended resonance effects. In the present work, the difference in reactivity between NVP and VEs is considered to be low thus, making it easier to combine these monomers in a single polymerization system, thus providing better control over the copolymerization procedure. However, difficulties exist in the specific system of monomers. VAc is considered to be the least active monomer among the common LAMS in RAFT polymerization because it provides highly reactive and thus unstable propagating radicals. Therefore, it is not very easy to control the polymerization reaction. The situation becomes even more problematic upon increasing the size of the n-alkyl side group of the VEs leading to extended retardation of the polymerization reaction and the possibility to have pronounced termination reactions rendering the control of the macromolecular architecture even more difficult. [
58,
59,
60]
This work is focused on the synthesis and characterization of the desired PNVP-b-PVEs block copolymers and the study of their thermal properties. The self-assembly behavior of these copolymers in selective solvents will be presented in a forthcoming publication. In the literature several efforts have been presented for the synthesis of statistical and block copolymers of different VEs, including VAc in all cases and other monomers from the same family, such as vinyl pivalate, vinyl benzoate, vinyl octanoate etc. In the past the corresponding block copolymers of NVP with VAc have been frequently reported in the literature. However, very limited work has been mentioned with the synthesis of block copolymers of NVP with other VEs.
2. Materials and Methods
2.1. Materials
N-Vinyl pyrrolidone (≥97% FLUCA) containing sodium hydroxide as inhibitor was dried overnight over calcium hydride and was distilled prior to use. The vinyl esters (TCI Chemicals) stabilized with monomethylether hydroquinone, were also dried over calcium hydride overnight and then were distilled under vacuum prior the polymerization. VBu has a bp at 115-117
οC , whereas VDc has a bp of 119-120
0C. On the other hand VSt is a solid monomer and was purified after dissolution in THF and passing through an inhibitor remover column. Azobisisobutyronitrile AIBN (98% ACROS) was purified by recrystallization twice from methanol and was then dried under vacuum. The Chain Transfer Agent, O-ethyl S-(phthalimidylmethyl) xanthate, was synthesized according to the literature protocols [
61,
62] employing O-Ethyl xanthic acid potassium salt and N-(bromomethyl)phthalimide. Dioxane and benzene were also purified over CaH
2 overnight and were distilled just prior to use.
All other reagents and solvents were of commercial grade and were used as received.
2.2. Synthesis of PNVP-b-PVEs Block Copolymers via RAFT Polymerization
The synthesis of the PNVP-
b-PVEs block copolymers was accomplished by sequential addition of monomers starting from the polymerization of NVP. O–ethyl S–(phthalimidymethyl) xanthate was employed as the CTA and AIBN as the initiator. The polymerization of NVP was conducted in glass reactors using high vacuum techniques [
63,
64] at 60
oC in benzene solutions for 12 hours.
A typical polymerization procedure for NVP with final M
n=8.9x10
3 (
Table 1, samples PNVP
-b-PVBu #3 and #4) is accomplished using a molar ratio of [NVP]
0/[CTA]
0/[AIBN]
0 = 100/1/0.2 and is described as follows: 5g of NVP were polymerized in the presence of 0.1284g CTA and 0.0148g AIBN in 5 ml of benzene. The polymerization solution was subjected to three freeze-thaw pump cycles in order to eliminate the oxygen from the polymerization apparatus. The reactor was flame-sealed and placed in a preheated oil-bath at 60
oC for 12h.
The reaction was terminated by removing the reaction flask from the oil-bath and by immediate cooling of the polymerization mixture under the flow of cold water. The apparatus was then opened exposing the mixture to air. The polymer was then precipitated in an excess of diethyl ether. This procedure was repeated at least three times in order to ensure the removal of any unreacted monomer residues. The polymers were finally dried overnight in a vacuum oven at 50oC to remove any residual solvent. The conversions for all homopolymers were near quantitative.
The PNVP homopolymers, served as the macro-CTAs to promote the polymerization of the VEs in a subsequent step. The block copolymerization reactions were performed in dioxane solutions at 80
oC for 96 hours in glass reactors under high vacuum conditions, as previously reported for the synthesis of the PNVP macro-CTAs. The quantities of the VEs monomers, the AIBN radical initiator and the dioxane solvent employed for the synthesis of the block copolymers are reported in
Table 1. The polymerization mixture was subjected to three freeze-thaw pump cycles in order to eliminate the oxygen from the polymerization apparatus The polymerization was terminated by removing the reactor from the oil-bath and cooling the mixture under a flow of cold water. The reactor was then opened and the copolymerization mixture was exposed to air. The copolymers with the PNBu blocks were precipitated in an excess of hexanes, whereas the copolymers with PVDc and PVSt blocks in methanol. The crude product was dissolved in THF and reprecipitated in the appropriate non-solvent. This procedure was repeated three times in order to ensure the removal of any unreacted monomer residues. Finally, the copolymers were dried overnight in a vacuum oven at 50
oC to remove any residual solvent. No further effort was needed to purify the samples.
2.3. Characterization Techniques
The molecular weight (Mw) as well as the molecular weight distribution, Ð= Mw/Mn, were determined by size exclusion chromatography, SEC, employing a modular instrument consisting of a Waters model 510 pump, U6K sample injector, 401 differential refractometer and a set of 5μ-Styragel columns with a continuous porosity range from 500 to 106 Å. The carrier solvent was CHCl3 and the flow rate 1 ml/min. The system was calibrated using nine Polystyrene standards with molecular weights in the range of 970–600,000.
The composition of the copolymers was determined from their 1H NMR spectra, which were recorded in chloroform-d at 30°C with a 400 MHz Bruker Avance Neo spectrometer (Billerica, MA, USA).
The Tg values of the copolymers were determined by a 2910 Modulated DSC Model from TA Instruments. The samples were heated under nitrogen atmosphere at a rate of 10 °C/min from -50 °C up to 220 °C. The second heating results were obtained in all cases.
The thermal stability of the copolymers was studied by thermogravimetric analysis (TGA) employing a Q50 TGA model from TA Instruments. The samples were placed in a platinum pan and heated from ambient temperatures to 600 °C in a 60 mL/min flow of nitrogen at heating rates of 10 °C/min.
Scheme 1.
Synthesis of the PNVP-b-PVEs block copolymers via RAFT polymerization.
Scheme 1.
Synthesis of the PNVP-b-PVEs block copolymers via RAFT polymerization.
Figure 1.
SEC traces from the synthesis of the block copolymer PNVP-b-PVBu #1 and #2.
Figure 1.
SEC traces from the synthesis of the block copolymer PNVP-b-PVBu #1 and #2.
Figure 2.
SEC traces from the synthesis of the block copolymer PNVP-b-PVDc #3 and #4.
Figure 2.
SEC traces from the synthesis of the block copolymer PNVP-b-PVDc #3 and #4.
Figure 3.
SEC traces from the synthesis of the block copolymer PNVP-b-PVSt #3 and #4.
Figure 3.
SEC traces from the synthesis of the block copolymer PNVP-b-PVSt #3 and #4.
Figure 4.
1H NMR spectrum of the block copolymer PNVP-b-PVBu #2.
Figure 4.
1H NMR spectrum of the block copolymer PNVP-b-PVBu #2.
Figure 5.
1H NMR spectrum of the block copolymer PNVP-b-PVDc #1.
Figure 5.
1H NMR spectrum of the block copolymer PNVP-b-PVDc #1.
Figure 6.
1H NMR spectrum of the block copolymer PNVP-b-PVSt #2.
Figure 6.
1H NMR spectrum of the block copolymer PNVP-b-PVSt #2.
Figure 7.
DSC thermograms of the PNVP-b-PVBu copolymers at 10o C/min.
Figure 7.
DSC thermograms of the PNVP-b-PVBu copolymers at 10o C/min.
Figure 8.
DSC thermograms of the PNVP-b-PVDc copolymers at 10o C/min.
Figure 8.
DSC thermograms of the PNVP-b-PVDc copolymers at 10o C/min.
Figure 9.
DSC thermograms of the PNVP-b-PVSt copolymers at 10o C/min.
Figure 9.
DSC thermograms of the PNVP-b-PVSt copolymers at 10o C/min.
Figure 10.
TGA plots of the PNVP-b-PVBu copolymers at 10o C/min.
Figure 10.
TGA plots of the PNVP-b-PVBu copolymers at 10o C/min.
Figure 11.
DTG plots of the PNVP-b-PVBu copolymers at 10o C/min.
Figure 11.
DTG plots of the PNVP-b-PVBu copolymers at 10o C/min.
Figure 12.
TGA plots of the PNVP-b-PVDc copolymers at 10o C/min.
Figure 12.
TGA plots of the PNVP-b-PVDc copolymers at 10o C/min.
Figure 13.
DTG plots of the PNVP-b-PVDc copolymers at 10o C/min.
Figure 13.
DTG plots of the PNVP-b-PVDc copolymers at 10o C/min.
Figure 14.
TGA plots of the PNVP-b-PVSt copolymers at 10o C/min.
Figure 14.
TGA plots of the PNVP-b-PVSt copolymers at 10o C/min.
Figure 15.
DTG plots of the PNVP-b-PVSt copolymers at 10o C/min.
Figure 15.
DTG plots of the PNVP-b-PVSt copolymers at 10o C/min.
Table 1.
Quantities for the synthesis of the bock copolymers.
Table 1.
Quantities for the synthesis of the bock copolymers.
Sample |
PNVP (g) |
AIBN (g) |
Vinyl ester monomer (mL) |
Dioxane (mL) |
Yield % |
PNVP-b-PVBu #1 |
2 |
0.0410 |
6 |
4 |
40 |
PNVP-b-PVBu #2 |
2 |
0.0410 |
1 |
4 |
33 |
PNVP-b-PVBu #3 |
2 |
0.0410 |
7 |
4 |
32 |
PNVP-b-PVBu #4 |
2 |
0.0410 |
3 |
4 |
38 |
PNVP-b-PVDc #1 |
2 |
0.0410 |
1.5 |
4 |
70 |
PNVP-b-PVDc #2 |
2 |
0.0410 |
7 |
4 |
68 |
PNVP-b-PVDc #3 |
2 |
0.0410 |
2.5 |
4 |
48 |
PNVP-b-PVDc #4 |
3 |
0.0615 |
1 |
4 |
73 |
PNVP-b-PVSt #1 |
3 |
0.0615 |
2.25 |
4 |
75 |
PNVP-b-PVSt #2 |
3 |
0.0615 |
3.75 |
4 |
52 |
PNVP-b-PVSt #3 |
3 |
0.0615 |
4.30 |
7 |
46 |
PNVP-b-PVSt #4 |
3 |
0.0615 |
6.00 |
9 |
43 |
Table 2.
Molecular characteristics of the block copolymers.
Table 2.
Molecular characteristics of the block copolymers.
|
macro CTA (PNVP) a
|
block copolymers a
|
NVP
|
Vinyl ester
|
Sample |
Mn 103 (Daltons) |
Ð |
Mn 103 (Daltons) |
Ð |
% molb
|
% molb
|
PNVP-b-PVBu #1 |
8.5 |
1.30 |
16.0 |
1.90 |
22 |
78 |
PNVP-b-PVBu #2 |
28.0 |
1.27 |
32.0 |
1.32 |
84 |
16 |
PNVP-b-PVBu #3 |
8.9 |
1.35 |
17.5 |
1.40 |
57 |
43 |
PNVP-b-PVBu #4 |
8.9 |
1.35 |
15.5 |
1.54 |
48 |
52 |
PNVP-b-PVDc #1 |
8.5 |
1.30 |
12.5 |
1.31 |
63 |
37 |
PNVP-b-PVDc #2 |
5.5 |
1.47 |
12.5 |
1.60 |
38 |
62 |
PNVP-b-PVDc #3 |
8.5 |
1.30 |
11.0 |
1.45 |
56 |
44 |
PNVP-b-PVDc #4 |
9.5 |
1.36 |
10.5 |
1.36 |
93 |
7 |
PNVP-b-PVSt #1 |
8.5 |
1.30 |
10.5 |
1.44 |
78 |
22 |
PNVP-b-PVSt #2 |
7.5 |
1.30 |
10.4 |
1.51 |
61 |
39 |
PNVP-b-PVSt #3 |
8.1 |
1.30 |
10.9 |
1.37 |
85 |
15 |
PNVP-b-PVSt #4 |
8.1 |
1.30 |
12.5 |
1.22 |
83 |
17 |
Table 3.
DSC results of the PNVP-b-PVBu block copolymers.
Table 3.
DSC results of the PNVP-b-PVBu block copolymers.
Sample |
Tg Experimental (OC) |
|
PNVP-b-PVBu #1
|
-9.1 |
80.3 |
126.6 |
PNVP-b-PVBu #2
|
- |
84.0 |
168.7 |
PNVP-b-PVBu #3
|
-8.9 |
93.6 |
153.3 |
PNVP-b-PVBu #4
|
-2.0 |
88.7 |
155.2 |
PNVP |
- |
- |
187.1 |
PVBu |
-8.5 |
- |
- |
Table 4.
DSC results of the PNVP-b-PVDc block copolymers.
Table 4.
DSC results of the PNVP-b-PVDc block copolymers.
Sample |
Tg Experimental (OC) |
|
PNVP-b-PVDc #1
|
-39.3 |
62.8 |
113.3 |
PNVP-b-PVDc #2
|
-39.7 |
63.3 |
100.8 |
PNVP-b-PVDc #3
|
-52.5 |
66.0 |
112.2 |
PNVP-b-PVDc #4
|
2.9 |
56.3 |
137.8 |
PNVP |
- |
- |
187.1 |
PVDc |
-45.0 |
- |
- |
Table 5.
DSC results of the PNVP-b-PVSt block copolymers.
Table 5.
DSC results of the PNVP-b-PVSt block copolymers.
Sample |
WVSt % |
Tm(°C) |
ΔH(j/g VSt) |
Xc % |
Tg1(°C) |
Tg2(°C) |
PNVP-b-PVSt #1 |
43.6 |
33.6 |
24.7 |
11.2 |
77.4 |
148.6 |
PNVP-b-PVSt #2 |
64.2 |
38.2 |
23.0 |
10.4 |
70.2 |
133.3 |
PNVP-b-PVSt #3 |
33.0 |
36.4 |
36.9 |
16.8 |
64.2 |
116.1 |
PNVP-b-PVSt #4 |
36.4 |
35.4 |
35.9 |
16.3 |
62.9 |
112.9 |
PNVP |
- |
- |
- |
- |
- |
187.1 |
PVSt |
- |
43.9 |
87.7 |
39.9 |
- |
- |
Table 6.
TGA results of the PNVP-b-PVBu block copolymers.
Table 6.
TGA results of the PNVP-b-PVBu block copolymers.
Sample |
Start |
End |
Max1 (OC) |
Max2 (OC) |
PNVP-b-PVBu #1
|
266.7 |
475.7 |
321.5 |
429.4 (broad) |
PNVP-b-PVBu #2
|
284.3 |
459.1 |
321.7 |
423.9 |
PNVP-b-PVBu #3
|
280.2 |
492.7 |
335.0 |
442.4 |
PNVP-b-PVBu #4
|
283.6 |
499.7 |
335.8 |
445.7 |
PNVP |
347.6 |
484.1 |
|
437.5 |
PVBu |
256.2 |
457.6 |
319.5 |
416.1 |
Table 7.
TGA results of the PNVP-b-PVDc block copolymers.
Table 7.
TGA results of the PNVP-b-PVDc block copolymers.
Sample |
Start1 |
End1 |
Max1 (OC) |
Max2 (OC) |
PNVP-b-PVDc #1
|
266.7 |
463.6 |
320.7 |
421.6 |
PNVP-b-PVDc #2
|
247.6 |
453.9 |
319.5 |
420.1 |
PNVP-b-PVDc #3
|
257.7 |
467.9 |
322.2 |
425.3 |
PNVP-b-PVDc #4
|
286.5 |
483.3 |
335.2 |
439.7 |
PNVP |
347.63 |
484.06 |
- |
437.5 |
PVDc
|
238.6 |
450.8 |
322.7 |
417.8 |
Table 8.
TGA results of the PNVP-b-PVSt block copolymers.
Table 8.
TGA results of the PNVP-b-PVSt block copolymers.
Sample |
Start |
End |
Max1 (OC) |
Max2 (OC) |
Max3 (OC) |
PNVP-b-PVSt #1 |
116.2 |
479.6 |
200.8 |
319.1 |
422.9 |
PNVP-b-PVSt #2 |
128.9 |
465.9 |
196.4 |
322.1 |
419.4 |
PNVP-b-PVSt #3 |
100.9 |
502.3 |
206.1 |
334.6 |
441.2 |
PNVP-b-PVSt #4 |
135.0 |
494.7 |
212.5 |
338.8 |
439.8 |
PNVP |
347.6 |
484.0 |
|
- |
437.5 |
PVSt
|
113.5 |
412.2 |
194.2 |
320.9 |
- |