Chunhua Wangab,
Feng Hua,
Kejian Yangb,
Tianhui Hub,
Wenzhi Wangb,
Rusheng Dengb,
Qibin Jiangb and
Hailiang Zhang*a
aKey Laboratory of Polymeric Materials & Application Technology, Key Laboratory of Advanced Functional Polymer Materials of Colleges of Hunan Province, College of Chemistry, Xiangtan University, Xiangtan 411105, China. E-mail: zhl1965@xtu.edu.cn
bZhuzhou Times New Material Technology Co. Ltd., Zhuzhou 412007, China
First published on 12th October 2015
A novel star-branched nylon 6 with hexafunctional cyclotriphosphazene core was synthesized using hexa(4-carboxylphenoxy)cyclotriphosphazene (HCPCP) with six carboxyl groups as multifunctional agent in the hydrolytic ring-opening polymerization of ε-caprolactam, and then used for the investigation of mechanical properties, crystallization and rheology behaviors. Star-branching structure and molecular weight have great effects on its properties. Compared with linear nylon 6, star-branched nylon 6 has lower relative viscosity and higher melt flow rate while its mechanical properties can be almost retained by the use of star-branching and an appropriate molecular weight. Research on crystallization behavior indicates that the degree of crystallinity (Xc) of star-branched nylon 6 decreases slightly, but its crystal structure still belongs to α form. The peak crystallization temperature (Tc) and crystallization rate (1/t1/2) of star-branched nylon 6 are significantly higher than that of linear nylon 6 because of heterogeneous nucleation induced by HCPCP core, which is beneficial for the use of rapid molding process. As the molecular weight increases, the Tc and 1/t1/2 of star-branched nylon 6 first increase and then decrease. Capillary rheometer measurement exhibits that the shear viscosity of star-branched nylon 6 decreases with decreasing molecular weight, and the shear viscosity of star-branched nylon 6 with an appropriate molecular weight shows a low value and little or no sensitivity to shear rate and temperature. Such rheology behavior allows for processing at low temperature and low pressure and reduces system cost.
It is well-known that star-branching decreases molecular dimension of polymer and results in a decrease in viscosity and a rise in flowability.11–13 Theoretically, incorporation of star-branched architecture into nylon molecule can result in some unusual properties compared to linear nylon with similar molecular weight, especially lower viscosity indicating its improved processability, which has been evidenced by Flory's pioneering work on star-branched nylon 6.7
Recently, star-branched nylon has attracted increasing interests due to its special properties that set it apart from linear nylon. For example, Fu et al. reported the synthesis of star-branched nylon 6 and nylon 12 using trimesic acid and cyclohexanonetetrapropionic acid as tri- and tetra-functional agents and investigation of their viscosities, mechanical properties and crystal morphologies.14–16 Yuan et al. focused on the molecular weights and molecular weight distributions of star-branched nylon 6s obtained by the polymerization of 6-aminocaproic acid in the presence of trimesic acid, EDTA and cyclohexanonetetrapropionic acid as multifunctional agents, and the results showed that the molecular weights calculated were in good agreement with those measured by experiment.17,18 Zhang et al. prepared high-flow nylon 6 with star-branched structure and dendritic polyamidoamine (PAMAM) core by in situ polymerization, and its melt flow rate was 70–90% higher than that of linear nylon.19–21 Wan et al. synthesized star-branched nylon 11 using the second generation polypropyleneimine dendrimer (PPI) as multi-functional agent, and investigated its isothermal and nonisothermal crystallization kinetics.22,23
Although many studies have been devoted to the synthesis, mechanical property, crystallization behavior, relative viscosity and melt flow rate of star-branched nylon, little attention has been paid to the systematic investigation of rheological behavior for star-branched nylon. Research on this aspect is very important because rheological behavior is one of the most important properties for polymer processing and application. Moreover, the multifunctional agents that have been reported and used to synthesize star-branched nylons are limited. Some multifunctional agent reported such as PAMAM is subjected to thermally decompose or undergo a number of side reactions even at a relatively low temperature (∼120 °C).24 For this reason, the corruption and disassociation of PAMAM were doomed to occur when ε-caprolactam and PAMAM were polycondensated at a high temperature (220–260 °C) for a rather long time (>3 h). Undoubtedly, the thermal stability of multifunctional agent is extremely critical for the targeting star-branched nylon to maintain structural integrity during high temperature melting polycondensation process. It is inspiring to find that multifunctional cyclotriphosphazene such as HCPCP can well satisfy this demand because of its excellent thermal stability caused by rigid benzene ring and nitrogen and phosphorus six-member ring structure. Furthermore, HCPCP has simple preparation method, easily controlled process, high yield and low cost. However, to our knowledge, few reports focus on star-branched nylon with multifunctional cyclotriphosphazene core.
In this study, we first chose hexafunctional cyclotriphosphazene HCPCP as multifunctional agent to synthesize a series of star-branched nylon 6 with different molecular weights by the hydrolytic ring-opening polymerization of ε-caprolactam, and then systematically investigated its mechanical properties, thermal properties, crystallization behaviors, flowabilities, and in particular rheological behaviors. Our results will demonstrate how star-branching and molecular weight influence its properties by comparing with linear nylon 6.
Sample | Caprolactam (g) | HCPCP (g) | Water (g) |
---|---|---|---|
SPA-1 | 2000 | 94.1 | 60 |
SPA-2 | 2000 | 70.6 | 60 |
SPA-3 | 2000 | 56.5 | 60 |
SPA-4 | 2000 | 37.6 | 60 |
SPA-5 | 2000 | 28.2 | 60 |
LPA | 2000 | 0 | 60 |
All the samples for mechanical properties tests were prepared by injection molding. Tensile strength and elongation at break were measured according to GB/T 1040.2-2006. Bending strength and bending modulus were measured according to GB/T 9341-2008. The charpy impact notched strength was measured according to GB/T 1043.1-2008. The moisture contents of the samples were regulated under standard conditions.
Thermal gravimetric analysis (TGA) was carried out on a Mettler Toledo TGA/DSC1 1100SF instrument at a heating rate of 10 °C min−1 under N2. The crystallization and melting behaviors of the samples were detected using DSC 204 F1 differential scanning calorimeter manufactured by Netzsch Company. The temperature and heat flow were calibrated using standard materials (indium and zinc). The scans were performed under N2 at the heating and cooling rate of 10 °C min−1. The samples with typical mass of 3–10 mg were encapsulated in sealed aluminum pans. The crystal structures of the samples were measured by wide-angle X-ray diffraction (WXRD). The WAXD patterns of melt-crystallized sample films were recorded on a Philips X' Pert Pro diffractometer with a 3 kW ceramic tube as the X-ray source (Cu Kα) and an X' celerator detector in the 2θ range from 3 to 40° at a scanning step of 0.02°.
The relative viscosities of the samples were determined by an Ubbelohde viscometer using 0.01 g mL−1 solution in 98% sulfuric acid in 25 °C water bath. The melt flow rates (MFR) in g per 10 min of the samples were measured by a melt flow rate tester (ZRZ1452) made from MTS Company at 235 °C and 0.325 kg load, according to GB/T3682-2000. Rheological behaviors of the samples in melt were investigated by capillary rheometer (RH7-D) made from Malvern Company with shear rates ranging from 50 to 4000 s−1. The capillary diameter (D) was 1.0 mm, its length (L) was 16.0 mm, and the L/D was therefore 16.0. The experiments were carried out at 230, 240, 250 and 260 °C.
Molecular weight characterization data of star-branched and linear nylon 6 obtained by end group titration, SLS and GPC are listed in Table 2. As shown in Table 2, the molecular weight obtained by GPC is obviously lower than that obtained by end group titration and SLS due to the smaller hydrodynamic volumes of star-branched nylon 6 in solution. However, all the results indicate that the molecular weight of star-branched nylon 6 mainly depends on the concentration of HCPCP, and the molecular weight increases with decreasing concentration of HCPCP, which are consistent with the results of previous work.7,17,18 As the concentration of HCPCP decreases to some extent, molecular weight of star-branched nylon 6 can approach and even exceed that of linear nylon 6.
Sample | [–COOH]a × 105 mol g−1 | [–NH2]a × 105 mol g−1 | Mn,EDTa × 10−4 | Mw,SLSb × 10−4 | Mn,GPCc × 10−4 | PDIc |
---|---|---|---|---|---|---|
a The [–COOH] and [–NH2] values were determined by end group titration, and Mn,EDT = bm/{[–COOH] + (b − 1)[–NH2]}, where m is the sample weight for titration and b is the functionality of multifunctional agent.b The Mw,SLS was obtained by SLS measurement and Zimm extrapolation method.c The Mn,GPC and PDI were measured by GPC and calibrated by narrowly distributed polystyrene standards. | ||||||
SPA-1 | 33.75 | 3.42 | 1.18 | 2.47 | 0.97 | 1.98 |
SPA-2 | 26.83 | 2.91 | 1.45 | 3.05 | 1.18 | 2.03 |
SPA-3 | 18.76 | 2.84 | 1.82 | 3.72 | 1.36 | 1.87 |
SPA-4 | 12.92 | 2.48 | 2.37 | 4.51 | 1.58 | 2.10 |
SPA-5 | 7.33 | 2.52 | 3.01 | 5.64 | 1.82 | 2.28 |
LPA | 5.29 | 5.47 | 1.86 | 3.98 | 1.67 | 2.16 |
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Fig. 5 Mechanical properties of star-branched and linear nylon 6. Error bars represent the standard deviations. |
Sample | Tda (°C) | Tmb (°C) | Tcc (°C) | ΔHmb (J g−1) | Xcd (%) | 1/t1/2e (min−1) |
---|---|---|---|---|---|---|
a The initial thermal decomposition temperature Td was measured by TGA at a rate of 10 °C min−1 under N2.b The melting point Tm and the fusion enthalpy ΔHm were obtained by DSC during the second heating process.c The crystallization temperature Tc was obtained by DSC during the cooling process.d Xc = ΔHm/ΔH0m, ΔH0m = 230.1 J g−1.e 1/t1/2 denotes the crystallization rate and is the reciprocal value of the half-crystallization time when the relative degree of crystallinity (Xt) reaches 50%. | ||||||
SPA-1 | 387.4 | 217.6 | 173.8 | 48.6 | 21.1 | 0.77 |
SPA-2 | 388.9 | 218.4 | 175.6 | 49.5 | 21.5 | 0.86 |
SPA-3 | 390.5 | 219.7 | 178.3 | 51.5 | 22.4 | 1.01 |
SPA-4 | 391.7 | 219.9 | 182.5 | 53.2 | 23.1 | 1.38 |
SPA-5 | 392.1 | 220.0 | 180.1 | 52.7 | 22.9 | 1.23 |
LPA | 392.6 | 222.1 | 173.5 | 53.8 | 23.4 | 0.64 |
The melting and crystallization behaviors of star-branched and linear nylon 6 were researched by DSC. The DSC thermal diagrams of star-branched and linear nylon 6 during the first cooling and subsequent heating process at a rate of 10 °C min−1 are shown in Fig. 7 and the results are listed in Table 3. Note that the melting point (Tm) of star-branched nylon 6 decreases with decreasing molecular weight. The decrease in Tm is ascribed to the rising branched degree and the decreasing hydrogen bond interaction. The degree of crystallinity (Xc) was determined from DSC analysis with the aid of the fusion enthalpy of 230.1 J g−1 for the perfectly crystalline nylon 6. As shown in Table 3, the Xc of star-branched nylon 6 is somewhat lower than that of linear nylon 6, since HCPCP core and its adjacent chains are suspected to be unable to crystallize. Scheme 2 shows the schematic illustration of crystallizability and crystallization rate of chains resided at different regions depending on the distance to HCPCP core of star-branched nylon 6. The chains of star-branched nylon 6 can crystallize if the free energy change ΔG is less than zero.27 As the chains are approaching HCPCP core, the crystallization becomes ever harder because of star-branching which restricts the chains folding and increases the free energy to some extent, and meanwhile the crystallization rate becomes ever slower as a result of the chain motion increasingly inhibited by HCPCP core. The Xc of star-branched nylon 6 increases with increasing molecular weight. It is because star-branched nylon 6 with higher molecular weight has less HCPCP core and uncrystallizable chain and therefore is able to form more perfect crystal. With the further increase of the molecular weight, the Xc increases slowly and even reduces slightly due to the more entanglements between the longer arms such as SPA-5.
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Fig. 7 DSC thermal diagrams of star-branched and linear nylon 6 during the first cooling (a) and the subsequent heating (b) at a rate of 10 °C min−1. |
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Scheme 2 Schematic illustration of crystallizability and crystallization rate of chains of star-branched nylon 6. |
As shown in Fig. 7, the peak crystallization temperature (Tc) of star-branched nylon 6 is higher than that of linear nylon 6. This result indicates that central HCPCP core can help star-branched nylon 6 to change the manner of nucleation from homogeneous nucleation to heterogeneous nucleation. In other words, HCPCP core plays a more important role than temperature in nucleation and crystallization of star-branched nylon 6. Accordingly, star-branched nylon 6 is easy to nucleate and then crystallize at a higher temperature than linear nylon 6 under the same cooling rate. A similar heterogeneous nucleation phenomenon was also reported in star-branched poly(ε-caprolactone).28
Another important parameter for crystallization behavior is the half-crystallization time (t1/2), which is the time when relative crystallinity (Xt) reaches 50%. Its reciprocal value, 1/t1/2, is often used to represent crystallization rate. Fig. 8 shows the Xt in the course of nonisothermal crystallization for star-branched and linear nylon 6 as a function of crystallization time at a cooling rate of 10 °C min−1. All curves present the similar S-shape, indicating that cooling rate has retardation effect on the crystallization. What's more, the curve of star-branched nylon 6 shifts obviously to the shorter crystallization time region in comparison with linear nylon 6, indicating the faster crystallization rate. The dependence of crystallization rate on the molecular weigh of star-branched nylon 6 is shown in the inset of Fig. 8. With the increasing molecular weight, the 1/t1/2 of star-branched nylon 6 first increases and then decreases. This may result from the opposite effect of HCPCP core concentration on nucleation rate and crystal growth rate. For SPA-1 to SPA-4 with relatively low molecular weights and high concentrations of HCPCP cores, their crystallization rates depend mainly on crystal growth rates of crystallizable chains. From SPA-1 to SPA-4, the molecular weight increases, the length of crystallizable chain becomes longer, the restriction of HCPCP core on the motion of crystallizable chain decreases, crystal growth rate increases, and thus crystallization rate increases. For SPA-5 with relatively high molecular weight and low concentrations of HCPCP cores, nucleation rate has greater effect on crystallization rate, and nucleation rate decreases obviously due to low concentration of HCPCP core, so its crystallization rate decreases. If the molecular weight continues to increase, we can infer by theoretically that the crystallization rate of star-branched nylon 6 will further decrease and approach that of linear nylon 6. Molecular weight effect on crystallization behavior of star-branched nylon 6 can be also observed from the Tc values listed in Table 3. The effect of molecular weight on Tc is similar to that of 1/t1/2. For star-branched nylon 6, the fast crystallization rate will contribute to the use of rapid molding process.
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Fig. 9 Relative viscosity and melt flow rate of star-branched and linear nylon 6. Error bars represent the standard deviations. |
To systematically investigate rheological behaviors of star-branched and linear nylon 6, capillary rheometry was applied. Fig. 10 shows the rheological curves of star-branched and linear nylon 6 at 230 °C. As shown in Fig. 10, shear stress increases with the increasing shear rate, but the relationship between shear stress and shear rate is nonlinear. Therefore, the melts of star-branched and linear nylon 6 exhibit non-Newtonian rheological behaviors.
Non-Newtonian index (n) is usually used to represent the degree of deviation from Newtonian fluid. The linear least square method is applied to fit lgτ vs. lg
γ curve, and the slope of the fitting straight line is the n value. Table 4 lists the n values of star-branched and linear nylon 6 at different temperatures. All the n values are less than 1.0, which further indicates the melts of star-branched and linear nylon 6 are pseudoplastic fluids. The value of n essentially reflects the sensitivity of shear viscosity to shear stress and shear rate. At the same temperature, the n value of star-branched nylon 6 reduces with increasing molecular weight, which means the degree of deviation from Newtonian fluid increases accordingly, due to the more entanglements between the longer arms. Compared with linear nylon 6, the n value of star-branched nylon 6 with relatively low molecular weight is higher and approaches 1.0, so the shear viscosity of star-branched nylon 6 with relatively low molecular weight is not sensitive to shear stress and shear rate. Moreover, the n value of star-branched and linear nylon 6 increases with the rise of temperature. This result demonstrates that the sensitivity of shear viscosity to shear stress and shear rate weakens with the rising of temperature.
T (°C) | Non-Newtonian index (n) | |||||
---|---|---|---|---|---|---|
SPA-1 | SPA-2 | SPA-3 | SPA-4 | SPA-5 | LPA | |
230 | 0.92 | 0.90 | 0.83 | 0.70 | 0.61 | 0.63 |
240 | 0.95 | 0.93 | 0.87 | 0.76 | 0.67 | 0.68 |
250 | 0.97 | 0.95 | 0.90 | 0.81 | 0.76 | 0.75 |
260 | 0.98 | 0.97 | 0.92 | 0.85 | 0.80 | 0.78 |
Fig. 11 shows the dependence of shear viscosity of star-branched and linear nylon 6 on shear rate at 230 °C. The shear viscosity of star-branched and linear nylon 6 reduces with increasing shear rate, exhibiting a shear thinning behavior of pseudoplastic fluid. This is because molecular chains orient along the flow direction and disentangle at high shear rate, and the relative motions between molecules become easier. Compared with linear nylon 6, the shear viscosity of star-branched nylon 6 with relatively low molecular weight shows a low value and little or no sensitivity to shear rate, which agree well with the result of n. The dependence of shear viscosity on the molecular weigh of star-branched nylon 6 is shown in the inset of Fig. 11. The shear viscosity of star-branched nylon 6 increases with increasing molecular weight, due to the longer arms lengths and the more entanglements between the longer arms. When the molecular weight increases to some extent, the shear viscosity of star-branched nylon 6 can reach and even exceed that of linear nylon 6. This result is consistent with the aforementioned result of relative viscosity.
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Fig. 11 Shear rate dependence of shear viscosity of star-branched and linear nylon 6 at 230 °C. The inset shows the dependence of shear viscosity on the molecular weigh of star-branched nylon 6. |
Fig. 12 shows the temperature dependence of shear viscosity of star-branched and linear nylon 6 with shear rate at 1338 s−1. The shear viscosity reduces with increasing temperature. As the temperature increases, the movement of chain segment increases, the free volume of the melt increases, intermolecular interaction weakens, and thus shear viscosity reduces. Flow activation energy (ΔEη) reflects the sensitivity of shear viscosity to temperature. At the constant shear rate, the relationship between shear viscosity and temperature follows Arrhenius equation, so the ΔEη value can be calculated by the slope of lgη vs. T−1 straight line. The ΔEη values of star-branched and linear nylon 6 at different shear rates are listed in Table 5. As shown in Table 5, with the increase of shear rate, the ΔEη value decreases, that is to say the sensitivity of shear viscosity to temperature weakens. The increase of shear rate is benefit to disentanglement and the number of entanglement points decreases accordingly, so the ΔEη value decreases. At the same shear rate, the ΔEη value of star-branched nylon 6 increases with increasing molecular weight, due to the more entanglement between long arms. This phenomenon can be also observed in Fig. 12. Compared with linear nylon 6, star-branched nylon 6 with relatively low molecular weight shows a lower ΔEη value, so its shear viscosity is not sensitive to temperature as well. Such rheological behavior allows star-branched nylon 6 with appropriate molecular weight to process at low temperature and low pressure and reduces system cost. When the molecular weight increases to some extent, the ΔEη value of star-branched nylon 6 is no longer strongly dependent on the molecular weight and approaches that of linear nylon 6.
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Fig. 12 Temperature dependence of shear viscosity of star-branched and linear nylon 6 with shear rate at 1338 s−1. |
γ (s−1) | ΔEη (kJ mol−1) | |||||
---|---|---|---|---|---|---|
SPA-1 | SPA-2 | SPA-3 | SPA-4 | SPA-5 | LPA | |
259 | 58.03 | 64.29 | 68.32 | 73.52 | 75.65 | 73.74 |
1338 | 53.22 | 58.45 | 64.07 | 68.28 | 71.80 | 70.25 |
2314 | 50.56 | 54.76 | 61.28 | 65.16 | 67.26 | 67.76 |
4000 | 48.14 | 52.03 | 58.65 | 62.39 | 64.42 | 65.18 |
Footnote |
† Electronic supplementary information (ESI) available: HCPCP characterizations and TGA curves of star-branched nylon 6. See DOI: 10.1039/c5ra15598c |
This journal is © The Royal Society of Chemistry 2015 |