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REINFORCEMENT OF CRYSTALLINE POLYMERS

THERMODYNAMIC AND KINETIC ASPECTS OF REINFORCEMENT

4.3 REINFORCEMENT OF CRYSTALLINE POLYMERS

gc

i i2 i1 gi m m2 m1 gm

i i2 i1 m m

ϕ α α ϕ α α

ϕ α α ϕ α

− −

2 − αm1) [4.45]

This equation correlates Tgc with the thermal properties of matrix and transition layer.

4.3 REINFORCEMENT OF CRYSTALLINE POLYMERS

Crystalline polymers have some advantages, compared with amorphous polymers, because of their two-phase structure. This structure can be repre-sented as a low-modulus continuous phase in which high-modulus crystallites are uniformly distributed.49Macroscopic properties of crystalline polymers are determined by the relative content of the crystalline phase (degree of crystallinity, X).49 Similar to the degree of crystallinity, the conformational state of segments in tie chains, connecting amorphous and crystalline regions, plays a very important role. It is evident that any change in properties of crystal-line polymers is connected with either the degree of crystallinity or the conformational state of tie segments. Introduction of fillers into crystalline poly-mers influences both the structure and physical and mechanical properties of crystalline polymers. These processes were discussed in detail by Solomko.50At the same time, the general physico-chemical principles of reinforcement of crys-talline polymers are the same as for amorphous polymers, and based on the same approaches.

The interaction of polymer chains with a filler surface, which leads to re-duction in chain mobility, must alter the kinetics of crystallization. Fillers may also influence the processes of nucleation in crystallization. The effectiveness of the nucleation is determined by the nature of both polymer and filler. Investiga-tions of the influence of small addiInvestiga-tions of salts of organic acids, used as artificial nucleating agents, on crystallization shows51-53that they lead to changes in the supermolecular structure of polymer because changes of concentration of nucle-ating agents change conditions of crystallization and the process takes place at a higher rate. The mechanism of action of additives is as follows: on the surface of the solid particles of the nucleating agent there are formed ordered regions of polymer as a result of adsorption, acting as centers of crystallization. These or-dered regions are maintained on the surface, even at above melting tempera-tures, when homogeneous centers of crystallization within its bulk are completely broken up. With sufficiently high concentration of additives, the number of heterogeneous centers on their surface considerably exceeds the number of homogeneous centers which are formed in the bulk in the course of crystallization. An increase in the number of centers of crystallization leads to an increase in the overall rate of crystallization and a reduction in size of the spherulites. Artificial nucleating agents, even at concentration of 0.2 wt%, alter the rheological properties of polymer melts, which is linked with their struc-ture-forming action even in the melt.

By choosing substances of different nature as artificial nucleating agents and varying their concentration and particle size, it is possible to create polymer melts having high viscosity and resistance to temperature. Consequently, in the case of crystallizing polymers, the particles of filler are likewise centers of crys-tallization and structure-formation, just as in amorphous polymers, thus hav-ing a significant influence on the type of structure formed.

4.3.1 KINETICS OF CRYSTALLIZATION IN THE FILLER PRESENCE

The dependence of the equilibrium conversion degree,α, during crystalli-zation from melt is described by the Avrami-Erofeev equation:

α(t) = 1 exp(-K t )− p n [4.46]

where Kpis the rate, and n is a geometric constant characterizing the nature of the nuclei and the type of structures formed. Values of Kpand n are determined from the crystallization isotherms of filled and unfilled polymer in coordinates log[-log(1 -α)] vs log t, whereas the half-periods of crystallization, t, may be found from semi-logarithmic dependence ofαon log t. As a rule, the final stages of crystallization are characterized by the deviation from Eq 4.46. This deviation begins earlier for filled systems. For filled systems, the constant n is not an inte-ger, being between 2.24 and 2.72. Deviations from the Avrami-Erofeev equation had been already observed even for unfilled polymers, and are due to various causes, namely: the possibility of occurrence of simultaneous or consecutive crystallization according to different mechanisms. It may be simultaneous growth of crystalline structures on the nuclei of various type or secondary crys-tallization, during which the structures, formed by primary cryscrys-tallization, be-come more perfect and the total crystallinity degree increases. Since the value n is usually determined from the initial linear sections of crystallization iso-therms, when the secondary crystallization is absent, it is most probable that a fractional value of n is brought about mainly by simultaneous growth of crystal-line structures on nuclei of different type. They may be polymeric aggregates of fluctuating character, filler surface or micro-ordered regions, formed close to the polymer-filler interface. Deviations from straight-line dependence of the iso-therms of crystallization of filled polymers are more evident than for unfilled polymers,54-58 and they begin at lower degrees of crystallization. This may be brought about by the fact that the contact of the growing crystalline structures with each other, up to which stage the process is described by the Avrami-Erofeev equation, takes place at a lower degree of conversion because of the presence of filler. Filler is responsible for formation of a larger number of nu-clei of crystallization, which brings about the formation of a larger number of crystallites, which rapidly fill the entire volume of the crystallizing polymer.

Naturally, further increase in crystallinity is due to the perfecting of the pri-mary structures. This process is no longer described by the Eq 4.46.

The above remarks are also confirmed by the fact that these deviations be-come more evident with a lowering of the temperature of crystallization. The lowering is accompanied, in turn, by an increase in the number of nuclei of crys-tallization.

The crystallization of polymer in the presence of fillers is influenced by two main factors:

• the interaction of polymer with filler, changing configuration of adsorbed segments of chains, contributing to the onset of crystallization

• the actual presence of filler in the polymer melt, which raises the viscosity and hinders crystallization.

These factors are predetermined by the nature of the filler surface and filler concentration. With low filler content, the rate of crystallization rises be-cause filler particles act as nuclei of crystallization. With the rise of filler concen-tration, this process is hindered, and the rise in the viscosity of the system becomes the predominant factor. Thus, the kinetics of crystallization of filled polymers may only be described by Eq 4.46 in initial stages, with a fractional value of n. The rate of crystallization passes through a maximum at a low degree of filling, and then gradually becomes lower than the rate of crystallization of unfilled polymer as the amount of filler increases. In contrast to crystallization from melt, there is no considerable difference in the values ofα, at which devia-tion from the Avrami-Erofeev equadevia-tions begins (0.55-0.8), in crystallizadevia-tion from the rubber-like state in the presence of filler. This is explained by the fact that in crystallization from a filled melt, the formation of boundary regions of polymer with reduced mobility is equivalent to crystallization of unfilled poly-mer from the rubber-like state. In this case, the changes in n take place as a re-sult of growth of crystalline structures on nuclei of a different type. It must be noted that the rate of crystallization, whether of unfilled or filled polymer, is higher in crystallization from the melt. Thus, the filler has a specific effect on the process of crystallization. Comparison of the constants n in crystallization from melt or from the rubber-like state indicates that the addition of even a small amount of filler to polymer leads to an action equivalent to transformation of the system from a melt of a rubber-like state, and this affects the mechanism of crys-tallization and its kinetic parameters. In accordance with the theory of phase conversion,49the overall rate of crystallization, Gcryst, at temperature, T, is ex-pressed by the following equation:

where Go is for exponential member, exp(-∆G/kT) and exp(-∆E/kT) are the probabilities of the formation of a stable nuclei of crystallization and molecular transfer through the liquid-crystal inter-face, respectively, ∆G is the change in free energy during the formation of a nu-clei of a critical size, and∆E is activation energy of transfer.

From this equation, it is seen that the overall rate of crystallization from the melt may be regulated by introducing even a small amount of filler, if any pa-rameters of Eqs 4.46 and 4.47 will be changed by this incorporation. The nu-cleating role of filler manifests itself ei-ther in increasing concentration of nuclei or in decreasing energetic barrier of nu-cleation due to the decrease in the inter-facial energy at the polymer-filler interface. If the mechanism of crystallization is not changed with changing tem-perature, then the dependence of logGcryston log1/T will be a straight line from which the sum (∆G +∆E) may be calculated.

Figure 4.7 shows the dependence of the rate constant of crystallization of polyurethane on the temperature of crystallization from melt and rubber-like state. This dependence takes the form of straight lines, but the slope at low or high degrees of supercooling differs in sign. This is explained by the fact that the mechanism of crystallization from melt in the neighborhood of the melting point is determined mainly by the term∆G/kT, and accordingly, the temperature coef-ficient of the overall rate of crystallization is negative. On crystallization from the rubber-like state, the processes of diffusion through the interface becomes predominant, i.e., a positive value of temperature coefficient is determined by the term∆E/kT. Figure 4.8 shows plots of the dependence of (∆G +∆E) on the filler content (fumed silica) on crystallization from melt and from rubber-like

Figure 4.7. Dependence of logk on tem-perature of crystallization from the melt (a) or from the rubber-like state (b) Fumed silica content: 1-0%, 2-0.5%, 3-1.0%, 4-5%, 5-10% (by mass).

state. Bearing in mind that in the region of low

∆T, the crystallization is controlled by nucle-ation, it may be considered that the result given in Figure 4.8 indicates a reduction in the value of ∆G, necessary for the formation of a nucleus of a critical size. According to the ex-isting theories of crystallization,49,59∆G is de-termined by the equation:

∆G = 4b∆ ∆ T

k H TT

o e mo

m crit

σσ [4.48]

whereσ andσe are, respectively, the free en-ergy of the side and end faces of the crystallite, Tmo is equilibrium melting point,∆T = Tmo - Tcrit,

∆H is the enthalpy of melting, bois the height of the surface nucleus. It may be reckoned that σe, Tmo,∆H and bo do not depend on the pres-ence of a solid phase in the system. Conse-quently, the reduction in ∆G with the addition of a filler to melt must be attributed to reduction inσ(for identical values of∆T). The experimental results meet theoretical predictions. As Figure 4.8 shows, on crystallization from the rubber-like state in the neighborhood of Tg(in contrast with the case described above) the values of (∆G+ ∆E) initially increase and then remain practically un-changed. In our opinion, this is explained by an increase in the activation energy of diffusion of chain segments in the melt,∆E, as a consequence of raising the viscosity of the system. It is known that the value of∆E may be expressed, with sufficient accuracy, by the expression:60

∆E = 4120

k(51.6+ T T )− g [4.49]

Thus the increase in (∆G +∆E) with the addition of filler may be explained by raising the glass transition temperature of polymer. This conclusion is in line with the ideas about the influence of filler on the glass transitions of amorphous

Figure 4.8. Dependence of (∆G +

∆E) on fumed silica content in crystallization from the melt (1) or from the rubber-like state (2).

polymers. The constant value observed for (∆G +∆E) when changing the content of filler correlates well with the absence of change in the activation energy of vis-cous flow of melts of filled polymers with a rise in filler content. It must be noted that the values of (∆G +∆E) on crystallization from melt and from rubber-like state differ considerably for unfilled polymer, whereas in filled systems they are approximately identical (Figure 4.8).

Investigation on the influence of the nature of the surface of unmodified (fumed silica with free OH-groups on the surface) and modified (with dimethyl dichlorosilane with no OH groups on the surface) fillers shows that the degree of crystallization is higher in the case of unmodified fumed silica because of hetero-geneous nucleation. The energy of interaction of polymer with a polar surface of filler is higher than with a non-polar, which facilitates the transfer of macromolecules into surface layers and formation of micro-ordered regions ca-pable of acting as heterogeneous nuclei of crystallization. Introducing small amounts of filler into polymer with flexible chains may decrease the rate of the formation of the crystalline phase because of the increase in activation energy of transfer through the liquid-crystal interface. This effect is determined by the change in melt microstructure near the interface. The effect depends on the amount of the filler, i.e., on the fraction of the surface layers in the system. The influence of fillers on the crystallization of oligomers was also studied.61,62

4.3.2 CRYSTALLIZATION IN THIN LAYERS ON THE SURFACE

One of the most characteristic features of structural changes in the surface layers of crystallizing polymers is the transcrystalline morphology of the thin layers on the surface - distinct from the spherulitic morphology in the bulk.63 For transcrystalline morphology, the appearance of column-like structures, ori-ented along the normal to the interface and extending into the bulk up to the dis-tances (10-20)×10-6 m, is typical. The formation of transcrystalline layer is determined by higher concentration and higher activity of heterogeneous nuclei at the surface as compared with bulk.49When the melt is supercooled to the crys-tallization temperature, a great number of the centers of cryscrys-tallization are formed, initiating the growth of half-spherulites, as the front of crystallization propagates from the surface to the depth of melt. Transcrystalline growth ends on the front of column-like crystals moving from the surface with the front of spherulite growth in the bulk. The thickness of the transcrystalline layer is

de-termined by the ratio of the number of heterogeneous centers of crystallization at the surface and in the bulk.

The transcrystalline morphology is a result of the epitaxial growth and de-pends on the surface structure. It was established,64-66for transcrystalline struc-tures in polyurethanes, that the action of the surface extends to tens of microns.

The effect of transcrystallization is very important for reinforcement, as shown for transcrystallization of polypropylene in the presence of many synthetic fibres.67The formation of a transcrystalline interphase in fiber-reinforced poly-propylene depends on the type of fiber, the isothermal crystallization tempera-ture, and polymer molecular mass. The restriction of the front of spherulite growth by other interfaces (e.g., other filler particles) is of a great importance for reinforcement of crystallizing polymers. The diminishing of effective thickness of the interlayer between two particles, <L>, up to the values lower than the spherulite size (~5.10-6m), leads to the regular decrease of the rate of the bulk crystallization, Gcryst, at the same supercooling∆T.68For spherulitic crystalliza-tion, the rate of bulk crystallizacrystalliza-tion, Gcryst, is determined from the equation:

Gcryst= const SRvRNR [4.50]

where SR is the surface of spherulite, vR is the rate of the radial growth of spherulite, and NRis the number of spherulites in a volume unit. In the presence of fillers, the decrease in the rate of bulk crystallization is connected either with NRor with SR. The most probable is the change of SRwith a decrease in the thick-ness of the polymer interlayer. A transition should be observed from three-di-mensional to two-dithree-di-mensional crystallization, according to the spherulitic mechanism. This effect manifests itself in a decrease of contribution of the value SRfrom SR=4πR2to SR=2πRD, where R is radius of a disk of a growing crystal and D is its thickness. At condition D~<L>, the linear decrease in Gcryst, propor-tional to <L> should be observed. It was proven for crystallization of polycaproamide in the presence of 83 % bm of glass spheres. However, with de-crease in the interlayer thickness, not only does the rate of bulk crystallization diminish but also the spherulitic crystallization, GR.69-71These effects have been observed for many polymers of different chemical nature on supports varying in the phase state and surface energy. It was established that the phase state of the support has no influence on the spherulitic growth rate, whereas diminishing

the interlayer thickness below a critical value (~10-6m ) leads to the decrease of GR.61At the thickness of the interlayer <L> < 1×10-6m, the full suppression of crystallization was observed for some polymers.69

The long-range influence of the surface on crystallization, which deter-mines the thickness of the surface layers of crystalline polymers, is comparable with the spherulite sizes (5-10)×10-6m. At a rather high amount of filler, when the distance between filler particles is lower than the spherulite size, the poly-mer is subjected to surface effects. In this case, the structure and properties of polymer in the surface layer must depend on the distance from the surface. In this respect, one more level of microheterogeneity of the surface layers arises, due to the influence of the surface on crystalline structure.

Let us analyze the influence of the surface on the inhibition of crystalliza-tion in the surface layers.69-72The study was conducted on the influence of the thickness of a polymer interlayer between two glass surfaces on crystallization for gutta percha, isotactic polypropylene, and cellulose tribenzoate. Figure 4.9 shows the data for PP. The character of the curve, indicating the influence of the thickness of layer on the rate of nucleation, is explained by the fact that the fig-ure gives the sum of rates of nuclei formation at the interface and in the bulk. At a low thickness range, the nucleation on the surface is predominant; increasing the thickness of the interlayer leads to a more rapid increase in volume of spherulites than in the number of nuclei, and thus the curve turns downwards.

Figure 4.9. Influence of the thickness of interlayer of polypropylene between two glass surfaces on the volume of the spherulites v (1), the rate of nucleation vo(2), the rate of linear growth v3per unit of bulk (3) or per unit of surface, vs(4).

The minimum on curve 2 corresponds to the thickness at which the contribution of nucleation in the bulk to the overall rate of nucleation on the surface and in the bulk begins to increase. At sufficiently great thicknesses of the film, the nu-cleation in bulk begins to play a more important role than the nunu-cleation on the surface, and the number of nuclei in the film increases proportional to the thick-ness of the film in the same way as the volume of the crystalline phase. This means that the rate of spherulite growth reckoned per surface unit, GR, becomes

The minimum on curve 2 corresponds to the thickness at which the contribution of nucleation in the bulk to the overall rate of nucleation on the surface and in the bulk begins to increase. At sufficiently great thicknesses of the film, the nu-cleation in bulk begins to play a more important role than the nunu-cleation on the surface, and the number of nuclei in the film increases proportional to the thick-ness of the film in the same way as the volume of the crystalline phase. This means that the rate of spherulite growth reckoned per surface unit, GR, becomes