Introduction

In recent years, there has been a significant increase in interest in organic–inorganic materials with improved properties. They can be prepared by filling a polymer matrix with inorganic particles (also organically modified) to form nanocomposites or by chemical incorporation of such particles into the polymer matrix (hybrid polymer). Especially, interesting class of this type of modifiers is polyhedral oligomeric silsesquioxanes (POSS) with the general formula (RSiO1.5)n where R is an organic functional group [1]. These organic substituents may contain reactive groups able to copolymerize with monomers, or nonreactive groups improving the miscibility with polymers. It should be emphasized that POSS compounds are not nanoparticles, but molecules, are soluble and can be dispersed in a polymer matrix on a molecular level [2]. However, during polymerization or processing, they tend to agglomerate, which leads to the formation of (nano)composites. Incorporation of POSS derivatives to the polymer matrix can significantly improve/affect its mechanical properties (e.g., strength, modulus, rigidity) as well as increase thermal stability and flame resistance or reduce the viscosity during processing. These improvements apply to a wide range of thermoplastics and thermosettings polymers [3]. Polymer/POSS composites can be used in such areas as bioimaging, shape memory materials, photonics, dielectrics, batteries, antireflective coatings, superhydrophobic surfaces, tissue scaffolding, nanolithography, biomedical adhesives, drug delivery or flame-retardant materials [4].

POSS-containing materials can be prepared using ex situ (blending POSS with polymers [5,6,7]) or in situ (by curing the monomer/POSS mixture [7, 8]) methods. In situ methods usually allow for a better dispersion of the modifier in the polymer matrix. When a material containing POSS is prepared by polymerizing a monomer containing dissolved POSS, it becomes very important to know the curing kinetics, because they determine to a large extent the properties of the material, provide information on the optimal proportions of the monomer/modifier ratios and allows the selection of technological parameters of curing.

A particularly interesting method of curing is photopolymerization. The most important advantages of this technique are: very high speed of the reaction, ambient reaction temperature, high control of the reaction (the start and end points are well defined by lighting on/off) or spatial control (the reaction takes place only in irradiated areas) [9, 10]. These advantages of photopolymerization make it an attractive method of designing and developing of new materials.

In our previous work [11], we studied materials produced in UV-initiated copolymerization of 2-hydroxyethyl methacrylate (HEMA) with octamethacryloxy-POSS (M-POSS); both the kinetics of the reaction and the properties of the obtained materials were discussed. The use of POSS functionalized with methacryloxy groups led to the formation of a hybrid polymer; the polymerization kinetics and polymer properties were influenced not only by the physical interactions between the POSS modifier and the monomer or matrix (before and after UV curing), but also the formation of a polymer network. In the present work, we excluded the effect of network formation by using POSS-containing substituents that are not reactive in radical polymerization. The systems were characterized before, during and after the photocuring, with the special emphasis on the photopolymerization kinetics. The reaction kinetics were followed by isothermal differential scanning calorimetry (DSC), because this method is especially useful for studying the UV-initiated polymerization [9].

Experimental

Materials

Monomer: 2-hydroxethyl methacrylate (HEMA, purity 97%) and photoinitiator: 2,2-dimethoxy-2-phenylacetophenone (DMPA, purity 99%) were purchased from Sigma-Aldrich. Three types of nonreactive polyhedral oligomeric silsesquioxanes: octakis[(glycidyloxypropyl)dimethylosiloxy)]octasilsesquioxane (G-POSS), octakis[(octafluorpentyloxypropyl)dimethylosiloxy)]octasilsesquioxane (F-POSS) and octakis[(hydroxypropyl)dimethylosiloxy)]octasilsesquioxane (OH-POSS) were kindly donated by Wielkopolska Centre of Advanced Technologies (synthesized according to procedures described previously [12, 13]). The substituents in the investigated compounds are linked to the POSS cage via –Si(CH3)2O– bridges; therefore, these compounds are classified as spherosilicates. All the chemicals were used as received. The structures and abbreviations of POSS compounds are shown in Fig. 1.

Fig. 1
figure 1

Structures of POSS compounds used in the work

Characterization and measurements

Viscosity

The viscosity (η) of the investigated systems was measured at 20 °C in the shear rate range 75–1500 s−1 with DV-II + PRO Brookfield Digital Viscometer (cone-and-plate geometry) connected to the Ecoline Staredition 003 thermostat (Lauda). The viscosity was found to be independent on the shear rate. Additionally, for the system containing G-POSS, viscosity was measured at 40 °C (the temperature, at which the polymerization rate coefficients were estimated). The calculated viscosities (ηcalc) of the POSS/HEMA mixtures were determined from the Kendall–Munroe equation (Eq. (1)) [14, 15]:

$${ \ln }\eta_{\text{calc}} = \mathop \sum \limits_{i = 1}^{n} x_{\text{i}} \cdot { \ln }\eta_{\text{i}}$$
(1)

where xi and ηi are the molar fraction and viscosity of the i component.

FTIR study

Intermolecular interactions between HEMA and POSS modifiers were examined by infrared spectroscopy. ATR-FTIR spectra were recorded by the Nexus Nicolet model 5700 spectrometer (Thermo Fisher Scientific, USA) equipped with a ZnSe crystal ATR accessory.

Photopolymerization kinetics

Kinetic curves were obtained using DSC Pyris 6 (Perkin–Elmer, USA) equipped with a lid specially designed for photochemical measurements. The photocurable composition used for general kinetic studies contained 0, 2, 5, 10, 15 and 20 mass% of G-POSS, F-POSS or OH-POSS. The 2-mg samples were polymerized in open aluminum pans (diameter 6.6 mm) under isothermal conditions (20 °C) in high-purity argon atmosphere (< 0.0005% of O2). The polymerization was initiated by LED lamp (LC-L1, Hamamatsu, λ = 365 nm, I0 = 2.75 mW cm−2) in the presence of DMPA (1 mass%).

All experiments were performed at least in triplicate. The reproducibility of the kinetic results was about ± 3%. In the calculations, the heat of polymerization of the methacrylate group was assumed to be 56 kJ mol−1 for one double bond [16].

Detailed kinetic studies were carried out for HEMA/G-POSS system at 40 °C, with light intensity 1 mW cm−2, DMPA concentration 0.2 mass% and G-POSS content: 0, 2, 5, 10, 15, 20, 25, 30 and 50 mass%. Determination of propagation (kp) and bimolecular termination (k bt ) rate coefficients was carried out for compositions containing 10 and 20 mass% of G-POSS. The rate coefficients were calculated from the experimental data obtained from postpolymerization processes, which were registered after stopping the irradiation at various degrees of double bond conversion. The calculations were performed over the first 10 s of the dark reaction using the bimolecular termination model [9] (Eqs. 2 and 3):

$$\frac{{\left[ M \right]_{\text{t}} }}{{\left( {R_{\text{p}} } \right)_{\text{t}} }} = \frac{{2 \cdot k_{\text{t}}^{\text{b}} }}{{k_{\text{p}} }} \cdot t + \frac{{\left[ M \right]_{0} }}{{\left( {R_{\text{p}} } \right)_{0} }}$$
(2)
$$\left( {R_{\text{p}} } \right)_{0} = \frac{{k_{\text{p}} }}{{\left( {k_{\text{t}}^{\text{b}} } \right)^{0.5} }} \cdot \left[ M \right]_{0} \cdot \left( {\phi \cdot I_{\text{a}} } \right)^{0.5}$$
(3)

where (Rp)t and (Rp)0 are the polymerization rates at time t of the dark reaction and at the moment of breaking the irradiation, respectively, [M]t and [M]0 are concentrations of double bond at time t of the dark reaction and at the moment of breaking the irradiation, respectively, ϕ denotes quantum yield of initiation and Ia is intensity of the light absorbed. The rate coefficients were calculated in the form of kp · F and k bt  · F, where F = ϕ · Ia; it was assumed that F is constant in the range of the conversions studied.

Characterization of composites

Samples for characterization of thermal and mechanical properties have been polymerized in a two-part stainless steel mold covered with a poly(ethylene terephthalate) foil and placed in a Dymax UV 5000 Flood lamp (metal halide bulb, 300–670 nm; light intensity 310 mW cm−2 measured with Dymax radiometer ACCU-CAL-50).

Thermal properties

Thermal properties of the samples were studied by DSC and thermogravimetry (TG).

Glass transition temperatures Tg were determined using the DSC1 (Mettler Toledo, Switzerland) instrument under nitrogen atmosphere at the heating rate of 20 °C min−1 in the temperature range from − 80 °C to 180 °C. Tg was evaluated from the second run of the DSC measurement and was taken as an average value from three measurements. The reproducibility of the determination was about 1 °C.

Thermogravimetric analysis (TGA) (the thermal resistance) of the obtained materials was carried out using TG 209 F3 Tarsus thermogravimetric analyzer (NETZSCH-Geratebau GmbH, Germany). 10-mg samples were heated in Al2O3 crucibles from 40 to 800 °C at a heating rate of 10 °C min−1 under nitrogen atmosphere (N2 protection gas purge 10 mL min−1; N2 sample gas purge 20 mL min−1).

Mechanical properties

The tensile properties were measured with Zwick/Roell universal testing machine model Z020 (Zwick GmbH & Co. KG, Germany) according to PN-EN ISO 527-1:1998 (crosshead speed of 5 mm min−1). The Shore D hardness on Zwick Roell apparatus was measured according to DIN 53 505. The results were obtained as the average values of six measurements for tensile properties or ten measurements for hardness.

Results and discussion

Miscibility of POSS with HEMA and poly-HEMA

Prior to polymerization, the components of the formulations (HEMA and POSS) showed very good miscibility (transparent solutions). However, during the polymerization, phase separation (turbidity of the sample) appeared in all the systems under investigation. A slight separation was observed even after addition of only 2 mass% of the POSS modifiers; it was most noticeable in the case of F-POSS, and somewhat weaker and similar for G-POSS and OH-POSS. The visible phase separation indicates that the produced poly-HEMA/POSS are two-phase materials which can be considered as a type of (micro)composites.

Intermolecular interactions in HEMA/POSS systems

Intermolecular interactions occur mainly between OH or C=O groups from HEMA and OH or ether groups from the modifiers. These functional groups can contribute to OH···OH, OH···O=C and OH···O types of inter- and intramolecular H bonds. FTIR spectra of the investigated HEMA/POSS systems in the range of OH and C=O group absorption are shown in Fig. 2.

Fig. 2
figure 2

FTIR spectra of neat HEMA and its mixtures with a, b OH-POSS, c, d G-POSS and e, f F-POSS in the a, c, e OH absorption region and b, d, f C=O absorption region. The numbers indicate the POSS content (mass%) in the composition

The absorption of HEMA in the O–H stretching region (about 3150–3670 cm−1) consists of several overlapping bands which can be ascribed to OH···OH type of H bonds (the band component at 3330–3350 cm−1), an overtone of C=O stretching (at 3427 cm−1), OH···C=O type of H bonds (with the maximum at about 3520 cm−1) and free hydroxyl groups (the band at 3620–3670 cm−1) [17]. Interactions of OH···C=O type are reflected also in the C=O stretching region (free C=O groups at ~ 1718 cm−1 and C=O involved in C=O···H–O bonding at 1701 cm−1) [17]. OH-POSS contains eight hydroxyl groups which form strong hydrogen bonds between its molecules (the band with the absorption maximum at about 3333 cm−1) [18].

Addition of OH-POSS to HEMA causes some changes in the shape of the OH absorption band. With the increase in the amount of modifier, the absorption of OH groups involved in the OH···C=O interactions disappears gradually, while the absorption of the band associated with OH···OH interactions increases. A similar but much less pronounced effect is observed in the case of G-POSS which may be related to the formation of OH···O bonds. (Observation of the oxirane group absorption was not possible due to the overlapping of corresponding bands in the range of 750–950 cm−1 with Si–CH3 absorption band.) F-POSS does not appear to affect the absorption of the OH band of HEMA.

The disappearance of OH···C=O interactions in HEMA is confirmed by changes in the C=O stretching region. In the presence of OH-POSS, the intensity of the band at ~ 1718 cm−1 increases at the expense of the intensity of the band at 1701 cm−1 indicating disruption of OH···C=O bonding and establishing of other interactions, e.g., OH···OH. A similar effect in the case of G-POSS is much less pronounced. On the other hand, the addition of F-POSS to HEMA increases the absorption intensity of the H-bonded C=O group suggesting rather weak interactions between HEMA and F-POSS and enhancing inter- or intramolecular interactions between the monomer molecules. Observation of the behavior of the Si–O–Si (1040 ÷ 1125 cm−1), C–O–C (1045 ÷ 1155 cm−1) or –CF2– (1135 ÷ 1240 cm−1) absorption bands [19] was not possible due to their overlapping.

In general, FTIR spectra seem to confirm the existence of interactions between the monomer and OH-POSS or G-POSS. However, these interactions are not sufficient to maintain full compatibility between the polymer and the modifiers.

Viscosity of HEMA/POSS compositions

Viscosity is one of parameters in which knowledge is necessary to design technological curing conditions and one of the most important factors affecting the polymerization kinetics. Termination is a diffusion-controlled process; therefore, the termination rate coefficient k bt is inversely proportional to the viscosity (k bt  ~ η−1), whereas the polymerization rate Rp is related to the termination rate coefficient as Rp ~ (k bt )−0.5 [20, 21]. Changes in the viscosity of a composition may also indicate changes in the interactions between the components. The viscosity of the compounds studied in this work differs significantly at 20 °C: from 6.79 mPa s for HEMA and 395 mPa s for G-POSS up to 1877 mPa s for F-POSS. At 20 °C, OH-POSS is solid. Thus, changes in HEMA/POSS ratio must strongly affect the viscosity of their mixture.

Experimental viscosity values at 20 °C and viscosities calculated from Eq. (1) (developed for mixtures of liquids with similar intermolecular interactions and molar volumes) are presented in Fig. 3a. The increase in the formulation viscosity is the strongest in the case of OH-POSS which to a large extent can be attributed to strong HEMA/POSS interactions confirmed by FTIR. The influence of F-POSS and G-POSS is much smaller and similar. Calculation of theoretical values of viscosity was possible only for compositions containing G-POSS and F-POSS. Experimental values show significant deviations from the theoretical values, suggesting the occurrence of viscosity synergism (slightly stronger for F-POSS), which in turn may indicate strong interactions. In general, the occurrence of synergism indicates that the viscosity of the monomer/modifier associates is greater than the viscosity of the associates in the pure compounds. Alternatively, one can consider an increase in friction forces in the monomer/POSS associates as a result of physical interactions, e.g., entanglements. However, the molar volumes of the components (HEMA and POSS) differ significantly which can enhance the observed deviations; despite this, we cannot exclude the influence of intermolecular interactions. A similar synergism of viscosity we also observed in the case of HEMA/M-POSS compositions [9]. The occurrence of this phenomenon is very important for the design of technological parameters of curing (e.g., photocurable lacquers or varnishes), because the viscosity of the formulation can be significantly higher than expected.

Fig. 3
figure 3

Measured (ηM, solid symbols) and calculated (ηcalc, open symbols) viscosities (a) and diffusion rate coefficient kdiff (b) of HEMA/POSS compositions at 20 °C as a function of POSS content. The lines are guides to the eye

Viscosity affects the propagation/termination steps if the diffusion coefficient, kdiff, is lower than the corresponding rate coefficients. The calculated kdiff values (Fig. 3b) show that at the beginning of the polymerization, both propagation and termination rates will not depend on translational diffusion. (The propagation and bimolecular termination rate coefficients for methacrylates are on the order of 103 and 107 M−1 s−1, respectively [16].)

Photopolymerization of HEMA/POSS systems

General kinetics

Kinetics of HEMA photopolymerization in the presence of POSS derivatives can be affected by the following factors: (1) change in the initial viscosity of the formulation, (2) dilution of the monomer, (3) system compatibility and (4) the impact of the inorganic POSS cage. Polymerization traces (at 20 °C) of formulations containing various amounts of the modifiers are shown in Fig. 4. Figure 4a–c presents the dependence of the polymerization rate Rp on irradiation time t, and Fig. 4d–f shows the polymerization rate Rp as a function of conversion of double bonds p.

Fig. 4
figure 4

Polymerization rate of HEMA in the presence of a, d OH-POSS, b, e G-POSS and c, f F-POSS as a function of irradiation time t and double bond conversion p. T = 20 °C, I0 = 1 mW cm−2, DMPA conc. 0.2 mass%. The numbers indicate the POSS content (mass%) in the composition

HEMA polymerizes with the formation of a linear polymer, and its polymerization kinetic curve is typical for a monomethacrylate polymerization with the steady state and gel effect regions. The development of the gel effect becomes clearly visible at about 15–20% of the double bond conversion. The most characteristic point is the maximum polymerization rate, R maxp (the end of the gel effect). During the polymerization of neat HEMA, this point is reached at around p = 40% (p at R maxp is defined as pRm). When the deceleration begins, Rp decreases sharply until polymerization ceases.

The addition of nonreactive POSS derivatives strongly affects the kinetics of HEMA polymerization, and the qualitative effect of all three compounds is similar (Figs. 4, 5): (1) addition of increasing amounts of POSS to HEMA leads to a gradual disappearance of steady state, which also results in shortening the time (tRm) after which the maximum polymerization rate, R maxp , is reached, (2) R maxp increases with the amount of POSS added, but only to its certain concentration (corresponding to the most reactive composition characterized by the highest R maxp value); above this content, R maxp begins to decrease, (3) the final degree of double bond conversion, pf, increases slightly as the concentration of modifiers increases, (4) pRm values appear to be independent of the POSS concentration to about 15 mass%.

Fig. 5
figure 5

Dependence of R maxp (a) and pf and pRm (b) values on POSS content at 20 °C. The lines are guides to the eye

As mentioned above, k bt is inversely proportional to the viscosity of the system: k bt  ~ η−1; thus, a significant increase in the initial viscosity of the POSS-containing formulations should result in faster polymerization. Therefore, the most important reason for accelerating HEMA polymerization after the addition of the tested POSS derivatives may be the increase in the initial viscosity of the formulation. Increase in viscosity leads to suppression of termination (decrease in k bt ) due to the slowing down of macroradical diffusion, which in turn enhances the gel effect. From among three types of diffusion processes controlling the termination: segmental diffusion at low conversions, translational diffusion after the beginning of the gel effect and reaction diffusion after reaching conversions in the range of pRm [9], only translational diffusion, the dominance of which determines the occurrence of the gel effect, depends on the length of the polymer chain and the viscosity of the system (both initial and increasing during the polymerization). Therefore, the higher the initial viscosity, the earlier the gel effect occurs. This is observed in our systems. Enhancement of the gel effect also leads to an increase in R maxp values.

However, the conversion at which R maxp appears (pRm corresponds to the reaction point, when the reaction diffusion begins to dominate in the termination mechanism) practically does not depend on the POSS content (up to ~ 15 mass%). When discussing this behavior, we should take into account the competition between two effects: (1) increase in the initial viscosity due to the addition of highly viscous POSS, which also increases the viscosity of the polymerizing system (compared to the modifier-free system) already at lower conversions, and (2) dilution of the system by an unreactive modifier which inhibits the increase in viscosity due to polymer formation, especially at higher conversions. In other words, the viscosity of the polymerizing system increases more slowly in the presence of POSS derivatives, and the higher the POSS concentration, the stronger the effect. The practical insensitivity of pRm values to POSS content can be associated with the influence of these two opposed effects.

The increase in the gel effect, as the concentration of POSS increases, is completed when the content of POSS reaches 15 mass%. A further increase in POSS concentration causes a reduction in pRm, which indicates that the reaction diffusion becomes the dominant termination mechanism with ever lower conversions. R maxp decreases compared to formulation containing 15 mass% of the additive because the gel effect cannot be fully developed due possibly to too high dilution of the system. Increasing the concentration of modifiers causes a small but continuous increase in the pf values. This is related to the plasticization of the polymer by additives, because the final conversion depends on the mobility of the polymerizing system.

Although the general explanation of the effect of all nonreactive POSS investigated on the HEMA polymerization kinetics is the same, there are some differences in the effects of the individual compounds. This may be related, at least in part, to the complicating phase separation effect that occurs during the polymerization. At the early stages of the reaction, the polymerizing system is a solution of the modifier and the polymer in the monomer. Upon reaching certain conversion (certain polymer concentration), the miscibility of the system becomes too small to keep the modifier completely dissolved and it begins to separate, changing the viscosity of the phase in which the polymerization takes place. So, further polymerization occurs in the monomer/polymer/POSS phase depleted with the modifier. Such a decrease in modifier concentration in the polymerizing phase and the resulting change in viscosity can affect the polymerization kinetics. The phase separation can also weaken the plasticizing effect of the additive, which in turn can affect the final conversion. Therefore, it is difficult to determine unambiguously what is the reason for the lower R maxp values of the system containing OH-POSS. It can be speculated, for example, that due to the best compatibility of the poly-HEMA/OH-POSS system, the amount of POSS separating during the reaction is the smallest and the dilution effect is the strongest. It is also possible, however, that the much higher initial viscosities of the HEMA/OH-POSS formulations result in an earlier completion of the gel effect, resulting in lower R maxp values.

Detailed kinetics

To obtain more information on the effect of nonreactive POSS derivatives on HEMA polymerization, we have performed detailed kinetic studies for the selected system, including the determination of the polymerization rate coefficients. Because the effect of all three POSS compounds is similar, we chose G-POSS as a model modifier and followed reaction kinetics over a wider range of its concentration (up to 50 mass%). The rate coefficients were determined for compositions containing 10 and 20 mass% of the modifier.

The investigations presented in this section were carried out at 40 °C, at lower light intensity and lower photoinitiator concentration. The change in the polymerization conditions was dictated by the need to slow down the reaction in order to increase the accuracy of determining the rate coefficients. (It should be remembered that HEMA photopolymerization rate decreases with increasing temperature [22].)

The viscosity of the formulation as a function of G-POSS content, measured at 40 °C, is shown in Fig. 6. At this temperature, HEMA viscosity is 3.4 mPa s, whereas viscosity of G-POSS is 128.2 mPa s. Obviously, these viscosities are lower than at 20 °C, but measurements in the range of 0–100% of G-POSS concentration well illustrate synergism of viscosity. The greatest difference between the experimental and calculated viscosity occurs at 80 mass% (21.2 mol%) of the modifier which indicates that intermolecular interactions between HEMA and G-POSS are the strongest when HEMA to G-POSS mol. ratio is 4:1.

Fig. 6
figure 6

Measured (ηM, solid symbols) and calculated (ηcalc, open symbols) viscosities of HEMA/G-POSS compositions at 40 °C as a function of G-POSS content. The lines are guides to the eye

Changes in polymerization conditions led to the expected decrease in the polymerization rate (about two times) (Fig. 7). The general picture of the dependence of polymerization parameters on the G-POSS content is analogous to 20 °C. However, the maximum on the curve R maxp  = f(POSS content) has shifted from around 10÷15 mass% to 20 mass%, which is mainly related to the increased polymerization temperature and the resulting decrease in viscosity. Thus, to achieve an analogous effect of slowdown the termination (necessary to obtain a composition with the highest R maxp ), the content of the more viscous compound (G-POSS) must be increased. However, the viscosity of the most reactive composition at 20 °C is about 8 ÷ 9 mPa s (at 10 ÷ 15 mass% of G-POSS), whereas at 40 °C, it is only about 5 mPa s (20 mass% of POSS). This proves that the influence of 8G-POSS on the HEMA polymerization is not only due to the reduction in the k bt coefficient.

Fig. 7
figure 7

Dependence of R maxp , pf and pRm on G-POSS content at 40 °C. The lines are guides to the eye

Determination of polymerization rate coefficients as functions of conversion degree p was performed for systems containing 0, 10 and 20 mass% of G-POSS. (The corresponding kinetic curves are shown in Fig. 8.) The latter composition is characterized by the highest R maxp value among compositions from the entire range of G-POSS content tested; thus, the differences between the rate coefficients of formulation with and without the modifier should be greatest. Measurements were carried out in the conversion range up to 40 mass% (≤ pRm) due to too large deviations of the polymerization conditions after the completion of the gel effect from those described by the assumed kinetic model.

Fig. 8
figure 8

Polymerization rate of HEMA/G-POSS systems as a function of irradiation time t (a) and degree of double bond conversion p (b). T = 40 °C, I0 = 1 mW cm−2, DMPA conc. 0.2 mass%. The numbers indicate G-POSS content (mass%) in the composition

Parameters related to rate coefficients of propagation (kp · F) and termination (k bt  · F) and their ratio as functions of double bond conversion p are shown in Fig. 9. Although these parameters do not represent real values of rate coefficients, their determination provides information on changes in actual kp and k bt coefficients in the presence of modifiers.

Fig. 9
figure 9

The ratio of the photopolymerization rate coefficients k bt /kp (a) and the individual parameters kp·F and k bt · F (b) as functions of double bond conversion p at 40 °C. The numbers indicate G-POSS content (mass%) in the composition. The lines are guides to the eye

The dependence of the k bt /kp ratio on the conversion is shown in Fig. 9a. Despite some scatter of data from the early stages of the reaction, a very slight decrease in this ratio with increasing conversion in the steady state region can be observed for the neat monomer and composition containing 10 mass% of the modifier. This stage is not observed for composition modified with 20% of G-POSS due to the lack of the steady state (compare Fig. 8). After beginning of the gel effect, a rapid drop of the k bt /kp ratio occurs; this drop is slowed down at about 35% of double bond conversion, with the tendency to form a plateau, characteristic of the reaction stage, when termination becomes controlled by the reaction diffusion (independent on the chain length). Such a dependence is typical for the behavior of k bt with increasing conversion; reflection of k bt changes on the k bt /kp = f(p) dependence results from the fact that the termination rate coefficients are about 3 ÷ 4 orders of magnitude higher than the propagation rate coefficients. The addition of G-POSS results in a marked decrease in the k bt /kp ratio, mainly associated with the decrease in k bt , although some increase in the kp value cannot be ruled out.

The individual parameters kp·F oraz k bt ·F are shown in Fig. 9b. The behavior of k bt ·F with the increasing conversion corresponds exactly to the behavior of the k bt /kp ratio described above. Clearly visible is also the influence of G-POSS consisting of the reduction in the k bt ·F values; this is mainly due to the increased initial viscosity of the composition. Interestingly, in the presence of G-POSS, the decrease in the k bt ·F values with the increase in conversion is slower (lower slope of the curve, better seen in Fig. 9a). This can suggest that although the macroscopic increase in viscosity caused by the addition of G-POSS hinders the translational diffusion of macroradicals, it is likely that the presence of POSS cages mitigates these difficulties by exerting a slip effect.

According to theory, kp·F values in the investigated conversion range should be constant. The observed slight increase with conversion results from the deficiency of the calculation model used, especially in conditions of increased viscosity. However, the general picture of the kp·F = f(p) dependence for the three compositions makes it clear that the introduction of G-POSS to HEMA causes a slight increase in kp. This can result from interactions between the monomer and the modifier, which cause the HEMA molecules to cluster around the G-POSS molecule, thereby increasing the local concentration of the double bonds. Thus, the observed accelerating effect of G-POSS on HEMA polymerization is related to both the decrease in the k bt coefficient (dominant effect, mainly due to the increase in viscosity) and to the increase in the kp coefficient, which results from the interaction between G-POSS and the monomer.

Thermal properties

Glass transition

Glass temperatures Tg of the poly-HEMA/POSS composites are shown in Fig. 10. Neat poly-HEMA is a rigid polymer; its Tg is 83 °C. The introduction of nonreactive POSS affects this value, which proves that the phase separation was incomplete and a part of the modifiers remained dissolved in the polymer. In our preliminary study [23], we indicated that addition of small amounts (up to about 5 mass%) of POSS derivatives reduces Tg due to disruption of hydrogen bonding between poly-HEMA chains. This effect, and the effect of POSS cages increasing the free volume [23, 24], causes plasticization of the material. Tg begins to rise when POSS content in the composite exceeds 5 mass%. Such behavior suggests that separated POSS domains behave like nanofiller aggregates, introducing topological constraints and steric hindrance, which leads to an increase in Tg. Interestingly, the described effect is the lowest for OH-POSS which is probably due to the strong hydrogen bonds between OH groups in OH-POSS and in poly-HEMA that reduce the mobility of polymer chains.

Fig. 10
figure 10

The glass transition temperature Tg of poly-HEMA/G-POSS (a), poly-HEMA/F-POSS (b) and poly-HEMA/OH-POSS (c) materials as a function of POSS content

Thermal stability

The effect of the investigated POSS derivatives on the thermal stability of the poly-HEMA matrix was evaluated for composites loaded with 20 mass% of the POSS modifiers. The TG and DTG curves of neat POSS compounds, neat poly-HEMA matrix and poly-HEMA/POSS composites are shown in Fig. 11. Temperatures at 5% mass loss (T5), at 50% mass loss (T50) and residual mass (R) are reported in Table 1.

Fig. 11
figure 11

TG curves of poly-HEMA, G-POSS, OH-POSS, F-POSS and their composites containing 20% of the modifiers (a); corresponding DTG curves (bd)

Table 1 The results of thermal decomposition of POSS compounds, polymer matrix and composites containing 20 mass% of the modifiers

Of the neat modifiers, the lowest thermal stability shows OH-POSS (three-step degradation), which is mainly associated with dehydration of OH groups. The thermal stability of G-POSS and F-POSS (one-step degradation) is similar and better than the stability of OH-POSS. However, in all cases, the residual mass R is higher than that resulting from the mass fraction of POSS cages, which can be associated with the glassy silica layer formed during the pyrolysis of the POSS cages decreasing the diffusion rate of the decomposition gases [25, 26].

Introduction of modifiers into the polymer matrix does not affect markedly the beginning of the matrix decomposition (occurring in several steps associated with dehydration, depolymerization and degradation of the polymer backbone), and 5% of mass loss occurs at the temperatures very close to that observed in the case of pure poly-HEMA. However, the modifiers (except of OH-POSS) slow down the loss of mass during increasing temperature as is evident from the increased T50 values. TG and DTG curves of the composites are superposition of the corresponding curves for the individual components. Thus, the nonreactive POSS have very slight influence on thermal decomposition of the poly-HEMA matrix. The protective effect exerted by POSS is manifested by the increased amounts of residual mass R.

Mechanical properties

The results of mechanical measurements are presented in Fig. 12. In several cases, for higher POSS loadings, the obtained materials were too brittle to determine their mechanical parameters, hence the lack of some measuring points. As can be seen, the effect of all three POSS types is very similar and leads to deterioration of mechanical properties. At low modifier concentrations, this is probably due to plasticization of the material, which can also have a positive aspect in some applications. Up to about 10% by mass of the modifier content, the stiffness of the composites (associated with the Young’s modulus) decreases only slightly and this concentration appears to be the upper limit for filling the poly-HEMA with the tested nonreactive POSS derivatives. The negative effect of higher POSS loads on mechanical properties can be mainly attributed to the phase separation.

Fig. 12
figure 12

Dependence of Young’s modulus Et (a), tensile strength σM (b), elongation at break εB (c) and Shore hardness H (d) of poly-HEMA/POSS composites on POSS content. The lines are guides to the eye

Conclusions

The effect of various amounts of three nonreactive POSS derivatives on the photo-induced polymerization of HEMA and properties of the resulting materials was investigated by DSC and TG. The HEMA/POSS systems were characterized before, during and after the photocuring, with the special emphasis on the photopolymerization kinetics.

The investigated POSS derivatives, although fully miscible with HEMA, are only partially miscible with the polymer, forming separate domains in the cured material. Thus, poly-HEMA/POSS are two-phase materials that can be considered as a type of (micro)composites. The HEMA/POSS mixtures exhibit a viscosity synergism that may confirm the interaction between the monomer and the modifier. Although FTIR studies confirm the existence of intermolecular interactions between HEMA and OH-POSS or G-POSS, poly-HEMA/POSS interactions are insufficient to ensure full compatibility of the components in the cured material.

The dependencies Tg= f(POSS content) show a minimum between 2 and 5 mass% of the modifier content. At low concentrations, POSS derivatives disrupt hydrogen bonding between poly-HEMA chains and the presence of POSS cages increases the free volume; these effects cause the plasticization of the material. Above about 5 mass%, the separated POSS domains behave as nanofiller aggregates, introducing topological constraints and steric hindrance, which leads to an increase in Tg.

The nonreactive POSS have very little effect on thermal decomposition of the poly-HEMA matrix, which can result in a degree from the phase separation. Phase separation is also the main reason of the deterioration of the mechanical properties of composites compared to a pure polymer matrix.

Nonreactive POSS derivatives significantly affect the kinetics of HEMA polymerization. They enhance the gel effect and increase the polymerization rate and the conversion of double bond. The enhancement of the gel effect is mainly associated with a substantial increase in the initial viscosity of POSS-containing formulations which leads to suppression of termination reaction (decrease in k bt ). This beneficial effect intensifies with the POSS content up to 15 mass% and then begins to decrease due to possibly too large dilution of the system. Determination of the polymerization rate coefficients as function of double bond conversion for HEMA/G-POSS mixtures proved that the observed accelerating effect of G-POSS on HEMA polymerization is related to both the decrease in the k bt coefficient (predominant effect, mainly due to the increase in viscosity) and to the increase in the kp coefficient, which results from the interaction between G-POSS and the monomer. Detailed kinetic studies showed also the effect of the POSS cage, which seems to mitigate the inhibitory effect of viscosity on the diffusion of macroradicals by exerting a slip effect.