Meng Li*a,
Fen Liua,
Yu Lia and
Xihuai Qiang*b
aDepartment of Applied Chemistry, School of Science, Xi'an Jiaotong University, Xi'an 710049, People's Republic of China. E-mail: limeng0721@stu.xjtu.edu.cn
bCollege of Bioresources Chemical and Materials Engineering, Shaanxi University of Science & Technology, Xi'an 710021, People's Republic of China. E-mail: qiangxihuai@163.com
First published on 27th February 2017
Stable cationic waterborne polyurethanes (CWPUs) with a high solid content (HSC) were synthesized via the combination of cationic ionic and nonionic segments (polyoxyethylene alkyl amine, PAE). The process was based on an iterative strategy to design the cationic groups in soft segments and the chain terminal of polyurethanes (terminal ions) together with the determination of the optimal bimodal particle size distribution (PSD). The effects of the polymerization degree of poly(ethylene glycol) groups (PEG-g) in PAE and its interaction with the hydrophilic groups N-methyl diethanolamine (MDEA) in polyurethane were studied. It was found that the terminal ions resulted in a much finer dispersion, better dispersion stability, smaller particle size and lower viscosity. Moreover, the highest solid content (52.18%) of CWPU was obtained by the incorporation of PAE and a low terminal ions content of 2.5%, which had a bimodal particle size distribution. The increasing length of PEG-g was also found to enhance the thermal stability and render a better mechanical stability for the polyurethane films as the increasing PEG-g length may weaken the hydrogen bonding and reduce the extent of phase separation. The experimental results were further compared with molecular dynamic simulation results, which verified that the specific molecular structure of this WPU ensured its excellent properties. The static structure and dynamic properties obtained strongly supported the experimental observations reported on the morphology and thermal and mechanical properties of these polyurethanes.
The critical point to obtain WPUs with a high solid content is to effectively control the latex viscosity. The viscosity of a latex increases extremely rapidly with the augmentation of the solid content, especially above the upper limit of the solid content,15,16 since the particles are so crowded that the interactions between neighbouring particles are strong.17 Particle size distribution (PSD) is an important parameter in determining the relationship between the solid content and viscosity,18,19 and one of the key points to obtaining a high solid content with low viscosity (HSC/LV) is to control the particle size and its distribution. Generally, it is possible to increase the upper limit of solid content of WPUs with a multimodal PSD, since the small particles are able to fit into the interstices between large particles, thus weakening the particles' interactions. Furthermore, if the difference between the particle diameters and the volume percentage is located in a reasonable range, small particles could efficiently pack into the voids among the large particles, thus increasing the maximum packing factor of the particles.20,21
Another method to decrease the viscosity of WPUs is to reduce the dosage of ionic monomers in polyurethane, which can suppress the swelling of latex particles22 caused by the electric double layer, along with the electroviscous effect of latex particles. So reduction of the dosage of ionic monomers in polyurethane can increase the solid content. Lee and Kim23 designed a WPU with ionic groups merely in soft segments and chain terminals, which made the hydrophilic groups easily enter the surface of particles, and thus a solid content up to 45% was achieved with the dosage of DMPA down to 2%. However, the decrease in ionic groups possibly will lead to poor latex stability. Hou and his co-workers11 synthesized a WPU with a high solid content via the combination of ionic and nonionic monomers. Although one of the WPU's solid content reached a maximum value of 52%, this work only focused on PEG systems, where the products are anionic polyurethanes. Other relative research work reported by Y. Chen and Y. L. Chen verified that a minimum content of –COOH (0.178 mmol g−1 or 2.4% DMPA) is required to form stable dispersions.24 All the existing research indicates that employing ionic monomers alone has a limited ability for developing high solid content WPUs.
As to the synthesis of WPUs, the combination of ionic and nonionic monomers was employed to obtain finer particles than possible just using ionic monomers alone,25 which implies that the combination has a positive effect on the dispersion and stability properties of WPUs. In these processes, the ionic centres were incorporated as chain extenders and were located in the hard segments. Consequently, the mobility of the ionic segments was very much limited by the rigidity of the hard segments, and the ionic groups were not well exposed to the particle surfaces, which ensured more ionic groups to produce a stable dispersion. Besides, the connection relationships of anionic and nonionic monomers or the position of those hydrophilic groups in polyurethane should also have an influence on the dispersion and stability properties of WPUs.26 Namely, the combination of ionic and nonionic monomers, normally containing oxyethyl segments, has a synergistic effect on WPUs, leading to fine particle sizes and a stable dispersion with low hydrophilic groups.
Nowadays, the structural design and property characterization of WPUs are mainly based on laboratory trial and error experiments, which is necessary but time-consuming and not efficient. In the case of cationic WPUs, since the polymerization process is much more violent than that of anionic one, and the emulsifying capacity of cationic hydrophilic monomers is lower than that of anionic monomers, detailed experimental as well as theoretical studies on the structure–property relationship of CWPUs have not been widely reported. Computer simulation in turn can provide an attractive complement or substitute tool to support the efforts involved in the synthesis and characterization of new products.27–29 Moreover, molecular simulations have played an increasingly important role in materials modelling and subsequent technology development, as they can reveal the microscopic pictures of underlying mechanisms that are otherwise experimentally inaccessible or difficult to obtain.30,31 In addition, molecular simulations can also provide an insight into the microcosmic structural changes ultimately responsible for the macrocosmic behaviour. Raghu et al.7 investigated the effects of hard segments in the polyurethane chain on the cohesive energy density, the surface properties and the solubility parameter values by using MD simulations and an experimental method, and they reported that the simulation results showed good agreement with the experimental data. Rahmati and his co-workers27 investigated the effect of the degree of polyurethane polymerization on the structural, physical and separation properties via the use of grand canonical Monte Carlo and molecular dynamic methods.
Considering the lack of studies in the existing literature, in this study reported here, we combined atomistic simulations and laboratory experiments to explore the synergistic effect on the combination of cation ionic (MDEA) and nonionic monomers (PAE) in polyurethane, and designed the ionic groups in the terminal of the main chain polyurethane as well as in the hard and soft segments. The effect of MDEA and PEG-g in PAE on the dispersion size, viscosity and stability of latex were then analyzed. The thermal and mechanical properties of the derived films were also studied. The main objective of the work was to obtain a further understanding of the key factors important to synthesize CWPUs with a high solid content, as well to reveal the relations between the micro-simulation and macro-experiments. Meanwhile, this strategy could provide a novel synthetic scheme to CWPUs with a high solid content.
A 250 mL round-bottomed, four-necked flask equipped with a nitrogen inlet, a condenser with a drying tube, a mechanical stirrer and a thermometer were used for the reaction. The synthesis of CWPU (Scheme 1) was catalyzed by DBTDL (0.03% based on the total solid content). The reactions were implemented at 80 °C until the theoretical NCO values were obtained, as determined by the dibutylamine titration method (ASTM D2572-97(2010)). Acetone was added at the same time to reduce the viscosity. Then, acetic acid as a neutralizing agent was not added into the reaction until the mixture was slowly cooled to 40 °C. The neutralization reaction proceeded at the same temperature for 30 min. Finally, distilled water was added to the mixture (based on 50% solid) with agitation at high shearing rates (2000 rpm) to emulsify the solution. The CWPU was obtained after the removal of acetone from the emulsion at 50 °C by rotary vacuum evaporation under reduced pressure. The formulations used to prepare the CWPU are given in Table 1.
Samplea | Hard segment | Soft segment | PEGb monomers | Stability/6 months | MCc | SCd | |||
---|---|---|---|---|---|---|---|---|---|
TDI | PNGA | MDEA | IPDI | PAE | |||||
a Sample code was named according to the content of PEG-g and MDEA; for example, P10-25 means containing 10 PEG-g in PAE and 2.5% MDEA.b The content of PEG-g in PAE approximate PEG monomers.c MC = MDEA content based on total weight of polymer.d SC = solid content of CWPU.e NS = no sedimentation; LS = little sedimentation; MS = much sedimentation. | |||||||||
P05-15 | 1.85 | 1.00 | 0.24 | 0.50 | 1.00 | PEG-g-200 | MSe | 1.5 | — |
P10-15 | 1.90 | 1.00 | 0.26 | 0.50 | 1.00 | PEG-g-400 | NS | 1.5 | 43.37 |
P20-15 | 1.95 | 1.00 | 0.32 | 0.50 | 1.00 | PEG-g-1000 | NS | 1.5 | 43.26 |
P30-15 | 2.00 | 1.00 | 0.38 | 0.50 | 1.00 | PEG-g-1500 | NS | 1.5 | 42.06 |
P05-25 | 2.00 | 1.00 | 0.40 | 0.50 | 1.00 | PEG-g-200 | NS | 2.5 | 47.77 |
P10-25 | 2.05 | 1.00 | 0.45 | 0.50 | 1.00 | PEG-g-400 | NS | 2.5 | 52.18 |
P20-25 | 2.15 | 1.00 | 0.55 | 0.50 | 1.00 | PEG-g-1000 | NS | 2.5 | 49.15 |
P30-25 | 2.25 | 1.00 | 0.65 | 0.50 | 1.00 | PEG-g-1500 | NS | 2.5 | 45.53 |
P05-35 | 2.20 | 1.00 | 0.58 | 0.50 | 1.00 | PEG-g-200 | NS | 3.5 | 49.57 |
P10-35 | 2.25 | 1.00 | 0.65 | 0.50 | 1.00 | PEG-g-400 | NS | 3.5 | 50.08 |
P20-35 | 2.40 | 1.00 | 0.79 | 0.50 | 1.00 | PEG-g-1000 | NS | 3.5 | 46.66 |
P30-35 | 2.55 | 1.00 | 0.93 | 0.50 | 1.00 | PEG-g-1500 | LS | 3.5 | 41.68 |
P00-15 | 2.36 | 2.00 | 0.30 | — | — | — | MS | 1.5 | — |
P00-25 | 2.65 | 2.00 | 0.50 | — | — | — | LS | 2.5 | 42.34 |
P00-35 | 3.00 | 2.00 | 0.82 | — | — | — | NS | 3.5 | 45.08 |
The Fourier transform infrared (FTIR) spectrum was recorded with a Perkin-Elmer Spectrum 100 FTIR spectrometer in the range 4000–500 cm−1 using a thin film prepared by casting a dilute DMF solution of the latex onto KBr flake and then evaporating DMF by heating under the infrared lamp.
The average particle sizes of the polyurethane dispersions were determined by a Zetasizer Nano-s (Malvern Instruments). Approximately 0.1 mL of the dispersion was diluted with 3 mL deionized water before the measurements. All the samples were measured at a temperature of 25 °C.
Transmission electron microscopy (TEM) images were obtained from a HITACHI-H7650 Microscope with an accelerating voltage of 80 kV, with the samples stained by 0.2 wt% phosphotungstic acid hydrate before observation.
Thermogravimetric analysis (TGA) was performed using a TGA Q5000 thermogravimetric analyzer (TA Instruments). The samples were placed in an alumina crucible and heated at 10 °C min−1 from 30 °C to 500 °C under a N2 atmosphere, where the flow rate of N2 was 30 mL min−1.
The DSC experiments were carried out in a DSC-200 instrument (NET-ZSCH, Germany). An aluminium pan containing 10–15 mg of sample was heated from −70 °C to 100 °C under a nitrogen atmosphere (flow rate: 40 mL min−1). The heating rate was 10 °C min−1. The first heating run was carried out to remove the thermal history of the samples. From the second heating run, the DSC curve of the sample was obtained.
The viscosities of the CWPU dispersion were measured in a Brookfield digital viscometer (Model DVII). Measurements were carried out at 25 °C using spindle No. 1 at 30 rpm.
The tensile properties of the cast films were measured at room temperature using an Instron 5566 testing machine, according to the ASTM D-412 specifications. A crosshead speed of 100 mm min−1 was used.
Stability of the CWPU: every day, 50 mL latex was placed in a glass bottle at room temperature to observe the condition of the latex, and it was recorded the number of days when lamination or precipitation had occurred.
The percentage of swelling for a particular film was determined by measuring its weight increase as a function of time using the equation:
(1) |
Considering the computational accuracy and expense, the model size was controlled at approximately a maximum of 12000 atoms in the models. Periodic boundary conditions were applied to the cubic simulation cells. For each system, all the chosen configurations were subject to a 10 circle thermal annealing from 300 K to 600 K and then back to 300 K with 50 K intervals. At each temperature, a 100 ps NPT ensemble was performed at constant pressure (1 bar) with a time step of 1 fs. A Nose thermostat and Berendsen38 barostat were used in all the simulations. At this situation, the last configuration was further subject to a 50000 step energy minimization, followed by annealing. Then the system was cooled down at intervals of 20 K, followed by a 1 ns NPT simulation to obtain the final equilibrium density. Afterward, the 10 ns NPT and 5 ns NVT simulations were performed to collect the data. The atomic trajectory, which was recorded every picosecond, was suitable for the structural and equilibrium thermodynamic properties analysis. For the simulations, we used a 12 core machine CPUs Intel Xeon@CPU X5650@2.67 GHz.
The effect of the PEG-g content in PAE on the synthesized CWPU is shown in Fig. 2. There is an obvious improvement on the dispersion and stability properties for the CWPU-incorporated PAE. When using MDEA alone as a hydrophilic monomer, a stable latex can only be obtained with an MDEA content above 2.5%. Those results are in accordance with previous results. For the samples incorporated with PEG-g-400 (or PEG-g-1000), all the samples had smaller particles size than the one incorporated with PEG-g-1500. However, all the samples incorporated with PEG-g-200 exhibit the largest sizes, indicating PEG-g-200 has little effect on improving the dispersion and stability of CWPU. So the effect of PEG-g is in the order of: PEG-g-400 ≈ PEG-g-1000 > PEG-g-1500 ≫ PEG-g-200.
Series | Dispersion size (nm) | Viscosity (mPa s) | Tensile strength/Mpa | Breaking elongation/% |
---|---|---|---|---|
P05-15 | 683.3 | 228 | — | — |
P10-15 | 336.2 | 200 | 18.85 | 685 |
P20-15 | 248.5 | 112 | 17.57 | 733 |
P30-15 | 361.4 | 520 | 16.33 | 764 |
P05-25 | 416.3 | 609 | 23.73 | 637 |
P10-25 | 214.7 | 626 | 20.17 | 677 |
P20-25 | 108.6 | 517 | 18.26 | 717 |
P30-25 | 378.2 | 870 | 17.57 | 755 |
P05-35 | 312.9 | 976 | 24.71 | 629 |
P10-35 | 233.3 | 510 | 22.91 | 661 |
P20-35 | 153.4 | 480 | 19.56 | 703 |
P30-35 | 488.5 | 3770 | 18.82 | 733 |
P00-15 | 589.6 | 272 | — | — |
P00-25 | 337.8 | 708 | 26.01 | 618 |
P00-35 | 215.6 | 950 | 27.85 | 607 |
Fig. 3 Schematic of the latex particles incorporated with PEG-g: (a) incorporated with PEG-g-400 and (b) incorporated with PEG-g-1500. |
Meanwhile, the particle size in the terminal ions was much smaller than that in the hard ions. This indicates that the concentration of ionic groups at the surface with the terminal chain is much higher than that with the hard chain. This can be explained by considering the chain rigidity of the hard segments, the chain flexibility of the soft segments, the high mobility and the low free energy of the chain ends. If the conformation change needs less energy, more ionic groups will be exposed to the surfaces during the dispersion. This leads to smaller particles with greater dispersion stability.
As to the samples containing PEG-g-400, the particle sizes decreased sharply with increasing the hydrophilic (–CH2–CH2–O–)n groups entering the o/w interface and the decreasing σ, whereas the particle sizes of the samples incorporated with PEG-g-1500 increased abruptly (as illustrated in Table 2 and Fig. 4), and the latex then became viscous with the same water addition. The results further prove the assumption that the long hydrophilic chains of PEG-g-1500 may form a thicker hydrated layer, which is not beneficial for decreasing the particle size, regardless of its role in decreasing σ.
Fig. 4 Synergistic effect of PEG-g and MDEA on particle size and viscosity of the CWPU (only 2.5% MDEA shown here for ease of visualization). |
Moreover, it was found that the change of particle size showed a different trend in the case of PEG-g combined with MDEA compared to using PEG-g alone as a hydrophilic monomer (nonionic WPU), where in the latter case the higher molecular mass of PEG-g resulted in smaller particle sizes of the latexes. Those results indicated that there was a synergistic effect between PEG-g and MDEA, which allows the hydrophilic groups in the CWPU to more easily enter into the o/w interface, resulting in better dispersion and stability.
As shown in Fig. 5 and Table 2, it is interesting to find that P05-25 and P10-25 exhibit a bimodal particle size distribution while P00-25 and P30-25 showed a unimodal particle size distribution. From P05-25 to P20-25, it can be seen in the particle size distribution graphs that two peaks of the samples become closer and finally emerge into one peak in P30-25.
Fig. 5 The particle size distribution of CWPU, (a) P00-25; (b) P05-25; (c) P10-25; (d) P20-25 and (e) P30-25. |
This phenomenon can be explained by the increment of PEG-g in the CWPU, resulting in the difference in the hydrophilicity of CWPU diminishing gradually and the average particle sizes tending to be close. As a matter of fact, the viscosity increased sharply from P20-25 to P30-25, and all samples in the present study showed the same trend. According to the research on traditional emulsions by Greenwood, small particles were able to fit into the packs among large particles when the diameter ratio of large particles to small particles was more than 5.67 (ref. 20) (Fig. 6). As shown in Fig. 5, P20-25 with the diameter ratio of 5.1 presented a relatively high viscosity, which can be explained by the fact that many of the small particles are not actually small enough to fit into the interstices among the large particles, thus decreasing the packing efficiency. However, the viscosity of P05-25 with the diameter ratio of 12.6 was higher than P10-25 with the diameter ratio of 7.2, indicating that the packing density decreased when the diameter ratio was too large. Therefore, a particle diameter ratio of 7.2 and a reasonable bimodal PSD are appropriate to raise the up limit of the solid content for the CWPU.
Fig. 6 A two-dimensional schematic showing the effect of the size of the smaller particles trying to pack into the pore among larger particles. |
Samples | Tgs/°C | Tgh/°C | T5%/°C | T10%/°C | T50%/°C |
---|---|---|---|---|---|
P00-25 | −40.3 | 32.2 | 139.34 | 182.60 | 297.85 |
P05-25 | −52.2 | 30.2 | 149.98 | 208.14 | 325.27 |
P10-25 | −54.8 | 28.1 | 157.58 | 212.53 | 330.01 |
P30-25 | −55.3 | 24.7 | 177.15 | 220.56 | 361.81 |
The thermal stability of WPU was evaluated by TG analysis. The typical TG and DTG curves of CWPU are shown in Fig. 9. TG analysis gave information, not only about the thermal stability of the polyurethanes but also on their structure, as the differentiated degradation steps of the hard and soft segments can be detected. What is especially important is the initial degradation temperature, which is dependent on the thermal stability of the weakest point(s) within the polyurethane macromolecule, i.e. urethane bonds and ester bonds. It is known that the hard segments are more prone to thermal decomposition than the soft segments in polyurethane. The basic process that takes place during degradation is depolymerization, i.e. the decomposition of PU to its parent substances: diisocyanate and polyols. The DTG curve of WPU presents a different degradation mechanism and indicates three stages of degradation. The first degradation at temperature ranges of 50–200 °C can be attributed to the volatilization of small molecular material remaining in the film. The second degradation at the temperature range of 250–350 °C mainly relates to the destruction of urethane groups. Finally, the maximum weight loss occurs within the range of 350–440 °C and most probably relates to the disruption reaction of ester bonds in polyester urethanes.
The thermal degradation temperatures of 5% weight loss (T5%), 10% weight loss (T10%) and 50% weight loss (T50%) are summarized in Table 3. As shown in Table 3, the higher the content of soft segments in a polymer is, the more stable the polymer is at elevated temperatures and the lower the initial rate of its degradation is. This phenomenon can be attributed to the length of PAE increasing, as it was shown that as the content of flexible segments in the polymer increases, the degree of phase separation decreases at the same time, and then there are lower hydrogen bonding interactions. The temperature of thermal resistance slightly increases in such cases. In addition, the presence of a side alkane groups in the CWPU reduces the potential for the formation of urethane–urethane hydrogen bonds, which makes it difficult for hard segments to agglomerate, i.e. their phase separation becomes hindered.45
MSD(t) = 〈|ri(t) − ri(0)|2〉 | (2) |
(3) |
Samplesa | Tgs/°C | Tgh/°C | Free volume/Å3 | Volume/Å3 | FFV/% | Rg/Å | Rete/Å | NHB/NO |
---|---|---|---|---|---|---|---|---|
a Samples A, B, C and D stand for P00-25, P05-25, P10-25 and P30-25, respectively. | ||||||||
A | −33.2 | 41.1 | 13884.63 | 87975.15 | 15.78 | 31.38 | 16.23 | 0.092 |
B | −46.2 | 38.8 | 13841.84 | 91022.55 | 15.21 | 41.33 | 18.75 | 0.087 |
C | −47.3 | 36.5 | 14083.42 | 98037.49 | 14.37 | 55.44 | 19.90 | 0.078 |
D | −50.5 | 32.9 | 17919.79 | 129540.96 | 13.83 | 58.40 | 23.20 | 0.061 |
Fig. 13 shows the O⋯N RDFs in the samples at 298 K. It can be seen that the first peak appearing in each RDF curve in the range from 1.8 to 2.1 Å are generally lower in intensity with PEG-g increasing, indicating that the hydrogen bonds decrease with the increasing PEG-g as expected. However, the second and third peaks increased with increasing PEG-g, which was probably attributed to the different chain conformation of PEG-g in PAE. Note that all sharp peaks at distances greater than 4 Å are absent and the RDF tend to 1, which is generally regarded as proof of the amorphous nature of a polymer system.53 The NHB/NO ratio corresponds to the ratio of the total number of hydrogen bonds to the total number of oxygen atoms. As suggested by a previous study,54,55 a criterion of “H⋯O length ≤2.5 Å, C–O⋯H or N–H⋯O bond angle ≥120°” was adopted to count the total number of hydrogen bonds in each sample (Fig. 14). The calculated NHB/NO ratios of the different samples are shown in Table 4. It can be seen that the results are in accordance with the aforementioned results, i.e. the hydrogen bonds decrease with increasing PEG-g.
Fig. 15 Probability distribution of the dihedral torsions for the O–C–C–O torsion (left) and C–O–C–C torsion (right) in the backbone. |
As shown in Fig. 15, all the samples had a helical conformation because the OC–CO angles exhibited a large population of the gauche conformation at ±70°, while the CC–OC angles have both gauche and trans states, which is in agreement with previous simulation studies and experimental results.56,57 Thus, the flexibility of the chains is related to the conformation structure of PEG-g in PAE. Chains with an ordered, all-trans conformation had low flexibility, whereas all the samples with a disordered, helical conformation had high flexibility.
As shown in Fig. 17, we plotted the average end-to-end distance and the average radius of gyration as a function of degree of polymerization (DP) for PEG-g on a log–log plot to verify the spatial structure of the polymer chain. We fitted these data to an equation of the form:
y = A(DP)x | (4) |
Fig. 17 Average chain end-to-end distance (Rete) and chain radius of gyration (Rg) as a function of DP. |
Both the structural measures could be well fitted by eqn (4). The scaling exponents for the radius of gyration and the chain end-to-end distance were 0.521 and 0.533, respectively. These exponents are close to 0.5, which is the scaling exponent for the characteristic polymer size in the case of sufficiently long chains, where the chains behave as random walks (RWs), as shown by Kamio et al.58 As is known, polymer chains with a scale factor higher than 0.6 can be classified as rigid chains, and the higher the scale factor, the more rigid the polymer chains.55 All of those results indicated that the increasing DP could result in a more flexible polymer chain.
The highest solid content (52.18%) CWPU was obtained by incorporation of PAE and a low terminal ions content (2.5%), which had a bimodal particle size distribution. We then chose representative samples and were able to show that the key factors to obtain a high solids content with low viscosities is the control of the particle size and its distribution. The thermal and tensile-strength properties of films derived from CWPUs were also analyzed. The results also showed that the temperature of thermal degradation slightly increases with the increasing length of PEG-g, which can be attributed to the length of PAE increasing and the degree of phase separation decreasing at the same time also leading to lower hydrogen bonding interactions. Meanwhile, with the increment of the PEG-g length, the hydrogen bonding was weakened and the extent of phase separation decreased, resulting in the tensile strength decreasing and the elongation at break increasing.
We further discussed the structure–morphological–property relations of CWPU by using simulations based on a realistic model. The static structure and dynamic properties were analyzed. It was found that the flexibility of the chain increased (e.g. MSD, chain end-to-end distance and radius of gyration) with increasing PEG-g, which led to the number of hydrogen bonds as well as Tg decreasing. The scaling exponents for the radius of gyration and the chain end-to-end distance also illustrated that increasing the DP could result in a more flexible polymer chain. Besides, all the samples had a helical conformation, which meant that the polymer chain had large flexibility. All of these simulation results intuitively reveal the microcosmic conformation of the molecular chain, and in further detail elucidated the effect of introducing PAE on the polymer properties.
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