Shusheng Lia,
Xiangzheng Kong*b and
Shengyu Feng*a
aKey Laboratory of Special Functional Aggregated Materials & Key Laboratory of Colloid and Interface Chemistry (Shandong University), Ministry of Education, School of Chemistry and Chemical Engineering, Shandong University, Jinan 250100, P. R. China. E-mail: fsy@sdu.edu.cn
bCollege of Chemistry and Chemical Engineering, University of Jinan, Jinan, 250022, P. R. China. E-mail: xzkong@ujn.edu.cn
First published on 14th October 2015
A novel type of highly uniform polymer microspheres, poly(urea–siloxane) (PUSs) was prepared through the precipitation polymerization of 1,3-bis(3-aminopropyl)-1,1,3,3-tetramethyldisiloxane (APTMDS) with isophorone diisocyanate (IPDI) in H2O–acetone mixed solvent. No additives such as surfactant and initiator were used. The effects of monomer ratio, H2O/acetone ratio, and monomer concentration on the yields and morphologies of the PUSs were investigated. Results indicated that PUS sizes can be regulated from 2.14 μm to 7.11 μm by varying the monomer ratio, monomer concentration and H2O/acetone ratio. Hydrogen bonds between polyurea units, polyurea and APTMDS moieties endowed the materials with good elasticity. The structures and morphologies of the materials were characterized by FT-IR, NMR, and SEM, and the thermal properties were characterized by TGA and DSC analyses.
Undoubtedly, polymeric spheres with micro- or macro-sizes possess larger surface areas and are more flexible than bulk materials.12 Silicone colloidal spheres have been used as catalysts,13 biosensors,14,15 chromatography,16 drugs carriers,17 and supports of vaccines,18 enzymes,19 antigens.20 Furthermore, they display an irreplaceable role in a number of material areas as they are finely dispersed in polymer matrices to improve their mechanical properties.21
Studies have been conducted on the fabrication of various types of polysiloxane spheres, namely polysiloxane spheres modified or coated by other species,22–24 organic and inorganic particles modified or coated by polysiloxane,25–27 and interpenetrating polysiloxane/polymer spheres.28 However, these spheres were obtained by multistep process, in which silicone parts are often prepared by hydrolytic polycondensation of trialkoxysilanes or trichlorosilanes.29,30 Therefore, these particles are also named polysiloxanes. The polycondensation does not lead to polysiloxane elastomers but polysilsesquioxanes,31–33 which most often have a rigid structure.
Fortuniak and Vilanova et al. obtained elastic polysiloxane particles through hydrosilylation or free radical emulsion polymerization.34,35 The particle sizes and monodispersion are uncontrollable for unavoidable adhesion between particles. The expensive and potentially inactivated noble catalyst is essential but hard to be removed in hydrosilylation.27,35 Lai et al. prepared particles with a polyurea core and a polysiloxane shell by the sol–gel process, in which triethoxysilane-functionalized polymers were made to react with 3-aminopropyltriethoxysilane and isocyanate (NCO)-ended prepolymers.36 In this case, 3-aminopropyltriethoxysilane is used as coupling agent to form three-dimensional Si–O–Si reticulation that restricts chain segment movement, but another organic–inorganic hybrid system is formed.
The rigid or elastic particles described above were prepared by heterogeneous polymerizations. In those processes, surfactants or stabilizers along with vigorous stirring were needed.34,37 In many cases, trace residual surfactants or stabilizers induce adverse consequences in many applications, particularly in biological and medical fields.38,39 Precipitation polymerization without any surfactants or stabilizers is a probable alternative method for preparation of polymeric microspheres, which originated in free radical precipitation polymerization of different vinyl monomers in recent decades.40,41 However, it is difficult to use for PUSs preparation because of the different functional groups in isocyanates and vinyl monomers.
For the preparation of pure PU spheres, Kong et al. proposed a novel protocol via condensation step precipitation polymerization of isophorone diisocyanate (IPDI) with H2O in acetone.42 Dalmais et al. further obtained uniform-size core–shell spheres from IPDI and poly(dimethylsiloxane–amide) prepolymer using a microfluid-assisted method.43 As far as we know, the preparation of PUSs microspheres with a convenient synthetic route has not been explored at all. Herein, we report the fabrication of novel PUSs by one step precipitation polymerization of IPDI with 1,3-bis(3-aminopropyl)-1,1,3,3-tetramethyldisiloxane (APTMDS) in H2O–acetone mixed solvent, in which, microsphere sizes from 2.14 μm to 7.11 μm can be precisely controlled. Unlike the previously reported studies on polymeric particles, this process is carried out without any surfactants and energy-consuming stirring.
Precipitation polymerization started as homogeneous solution of monomers and solvents. This was confirmed by an initially clear and transparent solution, which also indicated that generated pre-polymers were dissolved in the system. The reaction mixture turned turbid, indicating that the propagating chains have grown beyond their solubility limit in the medium (critical molecular weight) and precipitated to form primary particles. The phase-separation of growing polymer chains was caused by enthalpic precipitation in cases of unfavourable polymer–solvent interactions, or entropic precipitation in cases where cross-linking prevents the polymer and solvent from freely mixing.44 The first case was the main reason for non-crosslinked structure of PUSs. This was justified by further cross-linking degree tests, where the PUSs was easily dissolved in protic solvent, methanol and ethanol at reflux. The dramatic effect of hydrogen bonding on the morphologies and properties of siloxane–urea segmented copolymers and network morphologies of PU units have been demonstrated by previous fundamental studies.7,45–47 The resulting nucleus aggregated into larger microspheres, which continued to grow by capturing other particles and newly formed polymer chains, or by absorption and monomer polymerization. The turbidity increase of the reaction system indicated the growth of PUSs particles and a milk-like system was obtained.
| Runs | APTMDS/IPDI (weight) | NH2/NCO (moles) | tturbidb (min) | Dn (μm) | Dw/Dn | Sphere yields (%) | Oligomers (%) |
|---|---|---|---|---|---|---|---|
| a S0P10: S means APTMDS; P means IPDI; 0/10 means the mass ratio of APTMDS and IPDI.b tturbid: the minimum time for the precipitation polymerization system to begin to cloud. | |||||||
| aS0P10 | 0/10 | 0 | 48 | 6.11 | 1.01 | 60.36 | 30.28 |
| S1P9 | 1/9 | 0.10 | 45 | 6.12 | 1.01 | 57.70 | 33.87 |
| S2P8 | 2/8 | 0.22 | 33 | 6.04 | 1.02 | 53.73 | 36.03 |
| S3P7 | 3/7 | 0.38 | 9 | 3.39 | 1.03 | 52.53 | 38.15 |
| S4P6 | 4/6 | 0.59 | 7 | 2.79 | 1.06 | 51.14 | 42.99 |
| S5P5 | 5/5 | 0.89 | 6 | 2.49 | 1.09 | 52.18 | 41.70 |
| S6P4 | 6/4 | 1.34 | 0 | — | — | 28.94 | 63.43 |
Fig. 2 and Table 1 clearly show that PUSs of different sizes can be obtained by controlling monomer ratios. With increased APTMDS content, the sizes of PUSs gradually decreased from 6.11 μm to 2.49 μm. This may be caused by the decrease in surface energy. Microspheres with smaller sizes possess larger surface areas, which is thermodynamically unstable. The siloxane in the process can introduce desirable surface properties, with low surface energy as the most important. Whether in non-aqueous or aqueous systems, silicones used as surface active agents can significantly reduce their surface tension to as low as 21 mN m−1,48 which benefited to the formation of PUSs with small size. Furthermore, particle sizes are related to the selected solvent in polymerization, as well as the hydrogen bonds index in the solvent. A polymer allows the forming the particles whose size could be larger than expected due to the presence of secondary forces.49 Here, the content of polyurea groups and hydrogen bonds decreased along with IPDI content, which resulted in microspheres with smaller size. As shown in Table 1, the size distribution (Dw/Dn) of PUSs increased from 1.01 to 1.09 accordingly with increasing APTMDS from 0 wt% to 50 wt%. The rapid formation of PUSs nucleus should assume the main responsibility. The surplus particles formed in a short time intensified their collision, leading to a larger size distribution. The accelerated nuclei formation was visually displayed by turbid time. The precipitation of polymer chains and formation of primal particles accelerated with increased APTMDS, due to the hydrophobicity of Si–O–Si segments; thus, the turbid time (tturbid) of the reaction system decreased. The yields of PUSs also clearly decreased slowly and their oligomers increased along with increased APTMDS from 0 wt% to 50 wt%. The more APTMDS reacted with IPDI, the less NCO groups were left. Harder contractions occurred between –NCO groups and newly formed NH2 groups derived from –NCO group with H2O. This inevitably reduced the polymer molecular weight and left more oligomers in the solvent. If NH2/NCO was above 1 (S6P4) in molar ratio, then just a small (28.94%) output was obtained. Undoubtedly, when no or little IPDI was involved, no chain growth occurred, and no PUSs was obtained. To summarize, the size of PUSs can be controlled by adjusting of APTMDS content (no more than 50 wt%) in monomers at the expense of size distribution.
The impact of H2O content on the formation and uniformity of PUSs was carried out with varied H2O/acetone ratios in weight (1/9, 2/8, 3/7, and 4/6), keeping APTMDS/IPDI at 3/7 and the monomer constant at 2.0 wt%. The obtained results are given in Table 2, and selected SEM images are shown in Fig. 3.
| H2O–acetone (weight) | tturbid (min) | Dn (μm) | Dw/Dn | Yields (%) | Oligomers (%) |
|---|---|---|---|---|---|
| 1/9 | 75 | 2–6 | — | 31.09 | 60.38 |
| 2/8 | 40 | 2–6 | — | 34.87 | 52.13 |
| 3/7 | 9 | 3.39 | 1.03 | 52.53 | 43.15 |
| 4/6 | 1 | 2.14 | 1.04 | 66.50 | 24.96 |
Table 2 and Fig. 3 clearly show that relatively uniform PUSs was formed when H2O/acetone ratio was 3/7. With increased ratio to 4/6, the uniformity of PUSs decreased slightly from 1.03 to 1.04. This finding was due to the formation of more microspheres prompted by the reduced solubility of the oligomers in the polymerization medium. As aforementioned, the initially clear polymer solution in H2O–acetone turned turbid as polymerization progressed. The turbidity time was sharply shortened from 75 min to 9 min with increased H2O/acetone ratio from 1/9 to 3/7, and the turbidity rapidly increased as the ratio reached 40%. This advanced appearance of turbidity could be attributed either to an accelerated polymerization of pre-polymers with H2O or to the reduced oligomer solubility. The earlier appearance of turbidity was mainly due to the latter rather than the former, because H2O amount was much higher than –NCO groups of pre-polymers even at the lowest H2O content. The subsequent reactions of –NCO groups with the newly formed amine were faster than the amine-yielding reaction of H2O with –NCO groups, and therefore led to PUSs. PUSs was observed not to form if the reaction of –NCO group with H2O instantaneously occurred. In this case, given that –NCO groups further reacting with amine groups were available shortly after the start of polymerization, amine-terminated IPDI monomers or oligomers remained in the system.
When H2O/acetone ratios were 1/9, and 2/8, PUSs about 2 μm to 6 μm were obtained, whereas smaller ones were obtained at 3/7 and 4/6 H2O/acetone ratios (2.24 and 2.10 μm, respectively). This may be caused by the aggregation of primal particles, similar to the size of PUSs obtained at 3/7 and 4/6 H2O/acetone ratios. The aggregation that spontaneously occurred was perhaps due to their adhesive surface, which was related to solvent used in polymerization, and the aggregation led to serious coagulations and poor size distribution. H2O in the mixed solvent plays two main roles. Firstly, as a part of mixed solvent, H2O affects the morphologies of PUSs by changing the solubility parameters. Secondly, as a reactant, it reacts with –NCO to from NH2 groups, which further react with –NCO to form growing polymer chains. Thus, if no H2O was added in, the precipitation cannot conduct and no PUSs was obtained.
| Monomer (wt%) | Dn (μm) | Dn/Dw | Yields (%) | Oligomers (%) |
|---|---|---|---|---|
| 2.0 | 3.39 | 1.03 | 52.53 | 43.15 |
| 3.0 | 4.24 | 1.04 | 56.84 | 40.13 |
| 4.0 | 4.51 | 1.06 | 60.19 | 34.57 |
| 5.0 | 6.58 | 1.06 | 66.51 | 26.96 |
| 6.0 | 7.11 | 1.07 | 70.22 | 24.59 |
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| Fig. 4 SEM images of the microspheres obtained from precipitation step polymerization with varied monomer concentrations. | ||
Fig. 4 shows that with increased monomer concentrations, the size of PUSs increased from 3.39 μm to 7.11 μm, and the size distribution decreased from 1.03 to 1.07 accordingly. This indicates that the sizes of PUSs could be controlled by varying monomer concentrations but at the expense of PUSs dispersity. The exasperated size distribution was caused by accelerated collision of the particles, which was induced by the rapid formation of a mass of nuclei particles at high monomer concentrations.
C
O disappeared entirely in the PUSs (Fig. 5B and C), indicating that all –NCO groups of IPDI reacted. The strong stretching vibration peaks for N–H at 3360 cm−1, C
O at 1654 cm−1, C–N at 1240 cm−1 and plane banding vibration of N–H at 1550 cm−1, confirm the formation of polyurea groups (–NH–CO–NH–).51–53 The C
O and N–H observed at 1654 and 3360 cm−1, respectively, suggest that the solid product was connected by disordered hydrogen bonding between the active hydrogen atoms of the two urea donor groups (N–H) in one urea molecule and an acceptor oxygen of the carbonyl group (C
O) in another urea molecule, but not the free urea (1690 cm−1) or ordered hydrogen bonding (1630 cm−1).54,55 Compared with S0P10 (Fig. 5B), the obvious vibration absorption of Si–O–Si at 1053 cm−1, and Si(CH3)2 at 847 and 790 cm−1, confirm the successful introduction of the polysiloxane into PUSs.11,56 The absorptions at 2957 cm−1 and 2923 cm−1 are associated to stretching vibration of CH2 and CH3 respectively.
O, or urea's C
O. The hydrogen bonding interaction produces physical crosslinks, thereby reinforcing the PU matrix; and increases strength and stiffness.52 Thus, the PUSs should process drastic enhanced mechanical and tensile properties. This is true in the case of siloxane polymers because the constitutive (OSi[Me]2) units do not permit the establishment of strong interactions with the other polymer or units, and a small content of the polysiloxane allows a reduction in the interfacial tension. Therefore, a great APTMDS leads to easier dissolution of PUSs in protic solvents.
The similar curves of TGA and DSC for all samples in Fig. 8 indicated their similar molecular structures. Taking TGA curve of S3P7 as an example, it has an appreciable weight loss of 5% at about 310.6 °C (T5%, initial temperature of degradation), 50% at 352.1 °C (T1/2, temperature of 50% weight loss), and, 90% at 402.3 °C (T90%, temperature of 90% weight loss). On the DSC curve, an obvious degradation endothermic peak was obtained at 357.5 °C (Td). The weight loss and endothermic peak was caused by the decomposition of urea units. Several literature have shown that the decomposition of poly(urea–silicone) or poly(urethane–silicone) copolymers was in a two-way step, related to hard segments and soft segments.60 Here, only one decomposition step was observed due to the highly incorporated structure of PUSs. That is to say, no obvious hard and soft segments were present in the PUSs, but alternate structures of short siloxane and urea units were observed.
With the content of siloxane in PUSs samples (S0P10, S1P9, S3P7, and S5P5) increased from 0% to 50%, the T1/2 and Td decreased from 356.5 °C to 341.6 °C and from 362.5 °C to 347.5 °C respectively. The initial degradations of the copolymers occurred at the urea group (–NH–CO–NH–). However, examining the structures of PUSs, two types of urea were distinguished: urea-A and urea-B (Fig. 9). Therefore, the initial degradation of PUSs may occur at urea-A and/or at urea-B. At the range of 300 °C to 340 °C of TGA curves, the samples displayed different degradation rates (the weight loss percentage per minute, % min−1). As the content of urea-A in PUSs increased, the degradation rates increased accordingly: 2.7% min−1 of S0P10, 4.5% min−1 of S1P9, 7.2% min−1 of S3P7, and 10.7% min−1 of S5P5. The degradation of polyurethane and polyurea segments is a depolymerization process.60 Thus, in this case, urea-A degraded to form PDMS2 and IPDI fragments, while the degradation of urea-B possibly formed IPDI fragment only. The PDMS2 had higher volatility than IPDI, and had most effect in the region. In common studied poly(urea–silicone) or poly(urethane–silicone) copolymers, a high temperature was need to break Si–O–Si and great heat resistance was exhibited when long polysiloxane involved in. However in PUSs, siloxane parts are so short to provide heat resistance and signification change of PUSs were obtained in DSC and TGA. In spite of this, all samples of PUSs can be assumed to have excellent heat resistance at 300 °C in an inert atmosphere.
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