Open Access Article
Kuldeep Rajpurohit,
Sabrina A. Shaikh
,
Ashok K. Pandey
* and
Hemlata K. Bagla*
Department of Nuclear and Radiochemistry, Kishinchand Chellaram College, HSNC University, Mumbai-400020, India. E-mail: ashok.pandey@kccollege.edu.in; hemlata.bagla@kccollege.edu.in
First published on 16th March 2026
A green, initiator-free method for polymerizing 2-acrylamido-2-methyl-1-propane sulfonic acid (AMPS) was developed using low-frequency ultrasound (20 ± 3 kHz) in aqueous solution. Unlike conventional sonochemistry, where radical formation occurs via water sonolysis, the radical generation originates directly from the AMPS monomer, as verified by ESR, DPPH radical scavenging assays and NMR experiments. ESR experiments indicated the radical formation on AMPS at elevated temperatures, which was lowered by cavitation-induced shear forces caused by low-frequency ultrasound. Water functions as a medium for proton-assisted activation, as no polymerization occurs in aprotic solvents, such as DMF and 1-decanol, as well as a hydrogen-bonded deep eutectic solvent (choline chloride
:
ethylene glycol in a 1
:
2 mol proportion). Comparative experiments showed that acrylamide, methacrylic acid, and (3-acrylamidopropyl)trimethylammonium chloride failed to polymerize ultrasonically, underscoring the unique reactivity of AMPS. AMPS also polymerized under microwave heating, albeit at a higher temperature, further confirming that cavitation-induced mechanical activation assists but does not solely govern radical formation. Mechanistic validation was obtained through model reactions involving acrylamide polymerization in the presence of methane sulfonic acid (1
:
1 mol ratio), and AMPS did not polymerize in its neutralized Na+ form. These results establish that the sulfonic acid group serves dual functions, as a proton donor and as a charge-balancing counterion, thereby enabling an acid-assisted, hydrogen-bond-directed radical polymerization pathway under sono-mechanical activation. The poly(AMPS) hydrogels were characterized by FESEM, thermal analysis and swelling experiments. The tunable swelling behavior, governed by the crosslinker density, was observed with water uptake decreasing from 1678 wt% at 2 mol% MBA to 250 wt% at 15 mol%. Lightly crosslinked gels exhibited self-healing behavior driven by reversible hydrogen bonding. GPC and viscosity analyses revealed simultaneous cavitation-induced depolymerization and radical polymerization, similar to ionizing radiation-based polymerization, though rapid crosslinking stabilized the hydrogel network. The incorporation of functional polymeric hydrogels into cementitious systems has emerged as an effective strategy for modifying hydration behavior, mechanical performance, and microstructural development. The cross-linked poly(AMPS) hydrogel was used in its calcium form (Ca-poly(AMPS)) as an additive in ordinary Portland cement, and its effect was evaluated as functions of setting time, compressive strength, tensile strength, and heat of hydration.
Mechanochemical activation-based free radical polymerization offers several advantages, such as solvent-free polymerization, the possibility of new synthetic chemistry, no dependency on the solubility of monomer and precipitation, and controlled polymerization.17 The mechanochemical activation of polymerization or depolymerization is based on the utilization of mechanical forces generated by ball-milling to generate reactive free radicals. Ball milling and grinding provide higher shear forces that lead to solid-state polymerization of many vinyl monomers without the need for initiators.17 Another type of mechanochemical polymerization is activation by ultrasonication at high frequencies, which is well-suited for solvent media.18,19 The use of ultrasonic activation for chemical reactions is known as sonochemistry.20 Suslick classified mechanochemistry into four categories depending upon the manner of applying mechanical force, i.e. tribochemistry (the chemistry of surfaces in contact), trituration (chemistry induced by grinding and milling), macromolecular mechanochemistry (from breakage of polymer chains to molecular motors and biological motion), and sonochemistry (the chemistry generated from the mechanical consequences of sound).21 Ultrasonic waves in liquid media generate heat, shock waves, and microstreaming via cavitation, enhancing molecular motion.22 The sonochemical reactions could be attributed to mechanical forces generated due to shock waves and molecular motions, and free radicals formed due to cavitation, which can be varied by the frequency and intensity (power) of applied ultrasonication.23
Sonochemical radical generation increases with frequency up to a maximum in the mid-to-high range (∼300–800 kHz), after which it declines.23 At low frequencies, cavitation bubbles collapse violently due to their larger radius, producing strong shear forces but relatively lower radical yields. In contrast, ∼500 kHz offers optimal radical formation, whereas at ∼1 MHz, the bubble size is too small for effective collapse, leading to negligible radical production.24 The cavitation is a major factor for mechanochemical activation by ultrasound.25 Free radical polymerization at low frequencies (20–40 kHz) requires high power input and controlled conditions, including an inert atmosphere, increased viscosity (e.g., with glycerol), emulsion polymerization using sodium dodecyl sulfate, etc.26–29 At ∼500 kHz, polymerization proceeds more efficiently due to enhanced radical availability.30 Alternatively, chemical initiators such as AIBN, BPO, or sodium persulfate readily decompose under low-frequency cavitation (∼20 kHz) and have been extensively applied in bulk gel synthesis and in situ gel formation within porous polymer membranes.31–33
The additive-free sono-mechanical polymerization is the sustainable green route for the bulk production of high-purity hydrogels for commercial-scale applications such as health-care or polymer-reinforced green cement. Therefore, this study intended to develop a sustainable, additive-free water-based method for synthesizing poly(2-acrylamido-2-methyl-1-propane sulfonic acid) (poly-AMPS)-based hydrogels through sono-mechanical-activation at a low frequency (20 ± 3 kHz) of ultrasound, focusing on understanding the mechanism of polymerization, characterization of properties of hydrogel and tuning properties for the desired applications. The cross-linked poly(AMPS) hydrogel in its calcium form (Ca-poly(AMPS)) has been studied as a functional additive in ordinary Portland cement for understanding its effects on hydration kinetics, setting time, compressive strength, and tensile strength in the cementitious materials.
000× and at an accelerating voltage of 20 kV. Gel permeation chromatography (GPC) analysis of un-crosslinked poly(AMPS) in water was carried out using an 1260 Infinity II GPC system. An ultrasonic probe sonicator (model DP 700, procured from Gravity Laboratory) with 20 ± 3 kHz frequency, 700 watts power, and a 1.5 cm titanium probe was used to prepare hydrogels. Electron spin resonance (ESR) spectroscopy was performed on a JEOL JES-FA200 spectrometer (X-band: 8.75–9.65 GHz; sensitivity: 7 × 109 spins/0.1 mT; resolution: 2.35 µT) equipped with aqueous, electrochemical, UV-irradiation, sample-mixing, and angular-rotation accessories. Thermogravimetric analysis (TGA) was conducted using a Hitachi NEXTA STA-300 (RT to 1500 °C; operating up to 1300 °C; heating rate: 0.1–100 °C min−1). Differential scanning calorimetry (DSC) was carried out on a Hitachi DSC7020 (−150 °C to 725 °C; 0.1–100 °C min−1) under N2 flow (50–500 mL min−1) with liquid-nitrogen cooling. Nuclear magnetic resonance (NMR) spectra were recorded in D2O on a JEOL ECZR 600 MHz spectrometer fitted with a 5 mm multinuclear broadband probe and a TH5 variable-temperature probe (−100 °C to +150 °C) with automatic tuning and matching.
The formation of free radicals was studied by the radical scavenging assay using DPPH as described elsewhere.34 To prepare the DPPH solution for the radical scavenging assay (RSA), 0.08 mg of DPPH was dissolved in 100 mL of methanol to achieve a 0.2 µM concentration. In the RSA assay, several sample combinations were prepared to study the radicals scavenging by DPPH during polymerization. The test sample included two conditions: one containing 5 g of AMPS, 0.39 g of MBA, and 10 mL of distilled water combined with 10 mL of DPPH solution and another prepared without the DPPH solution, using only 5 g of AMPS, 0.39 g of MBA, and 10 mL of distilled water. To establish baseline controls, a negative control was prepared by mixing 10 mL of DPPH solution with 10 mL of distilled water, while a positive control consisted of 5 g of AMPS combined with 10 mL of DPPH solution. Each mixture was allowed to react for 5 minutes, providing sufficient time for interaction between free radicals and DPPH, thus enabling accurate RSA measurements under different conditions. The absorbance at 517 nm was monitored using a UV-visible spectrophotometer. The RSA percentage was calculated using the following formula:35
To investigate the effect of sonication on the viscosity of poly(AMPS) solutions, a series of experiments were conducted with varying poly(AMPS) concentrations and sonication times. Each experiment measured the changes in viscosity using an Ostwald viscometer at specific time intervals, providing insight into how sonication influences the rheological behaviour of AMPS solutions. The molecular weight determination of un-crosslinked poly(AMPS) was carried out by GPC using water as a solvent and PEG/PEO as the standards for calibration.
Poly(AMPS) hydrogels crosslinked with 5, 10, and 15 mol% of MBA were immersed in 0.1 M CaCl2 solution to convert these into Ca2+ forms. The Ca2+-equilibrated gels were dried before mixing with OPC. The Ca2+-equilibrated hydrogel was added in varying amounts, 0 (control), 0.3, 0.5, 1.0, and 2.0 wt%, to a mix of 398 ± 2 g of OPC with 102 g of distilled water. The water content corresponded to 0.85 times water required for normal consistency (30 wt% of OPC weight). Mixing was completed within 3–5 min at 27 ± 2 °C and 65 ± 5% relative humidity. The initial and final setting times were determined using a Vicat apparatus in accordance with BIS.37
Mortar for the control mix was prepared using 200 g of cement, 600 g of standard sand, and 84 g of distilled water. In hydrogel-modified mortars, OPC was replaced with 0.3, 0.5, 1.0, and 2.0 wt% hydrogel, corresponding to 199.4 g cement + 0.6 g gel, 199.0 g cement + 1.0 g gel, 198.0 g cement + 2.0 g gel, and 196.0 g cement + 4.0 g gel, respectively, while keeping the sand (600 g) and water content (84 g) constant. The mortar was placed in 70.6 mm cube moulds in three layers, each layer being tamped and subsequently compacted on a vibrating table at 12
000 ± 400 vibrations per min for 2 min. After 24 h of moist curing at 27 ± 2 °C and ≥90% RH, the specimens were demoulded and cured in water for 7, 28, and 60 days. The compressive strength was obtained as the average of three specimens as per the BIS method.38
For tensile strength determination, the control mortar consisted of 40 g of cement, 120 g of standard sand, and 16.8 g of distilled water. Hydrogel-modified mixes were prepared by replacing OPC partially with 0.12, 0.20, 0.40, and 0.80 g of hydrogel, while maintaining constant sand and water contents. The mortar was cast in briquette moulds in three layers with proper tamping and vibration, stored under moist conditions for 24 h, demoulded, and water-cured for 7, 28, and 60 days. Tensile strength was determined in triplicate in accordance with the BIS protocol.39
For the calorimetric study, the control paste consisted of 60 g of cement and 24 g of distilled water. In hydrogel-modified systems, OPC was replaced partially with 0.18, 0.30, 0.60, and 1.20 g of hydrogel, while maintaining a constant water content of 24 g. The paste was hand-mixed for 4 min, transferred to sealed plastic containers, and stored in a vertical position until testing at 7, 28, and 60 days. The heat capacity of the calorimeter was determined using a standard ZnO reaction in a solution containing 2 N HNO3 and HF. The heat of solution of anhydrous cement and hydrated cement was measured by recording the temperature rise after dissolution in the acid mixture. The heat of hydration was calculated from the difference between the heat of solution of anhydrous and hydrated cement in accordance with BIS.35
To clarify how the monomer structure governs sono-mechanical polymerization, a series of acrylate-based monomers with distinct functional groups were examined under identical 20 kHz sonication conditions using 10 mol% MBA as the crosslinker. The chemical structures of monomers are shown in Fig. 1. Monomers representing weakly acidic (methacrylic acid), neutral (acrylamide), and strongly basic ((3-acrylamidopropyl)trimethylammonium chloride, APMAC) functionalities, as well as AMPS in both its protonated (H+) and sodium (Na+) forms, were evaluated. Under prolonged sonication, none of the compared monomers underwent polymerization to form crosslinked hydrogels of poly(APMAC), poly(methacrylic acid), or poly(acrylamide), suggesting that neither neutral nor weakly acidic or strongly basic functionalities support sono-mechanical polymerization. Although methacrylic acid contains an acidic group, its acidity is far lower than that of sulfonic acid present in AMPS. Importantly, AMPS differs from APMAC only in the functional groups. AMPS carries a sulfonic acid moiety, whereas APMAC bears a quaternary ammonium cation. As shown in Fig. 1, AMPS contains both an amide segment (similar to acrylamide) and an alkane sulfonic acid unit, strongly suggesting that the sulfonic acid group plays an important role in enabling sono-mechanical polymerization. To verify this, acrylamide was polymerized in the presence of methane sulfonic acid (1
:
1 molar ratio). Under the same sonication conditions used for AMPS, a crosslinked poly(acrylamide) gel formed readily. Acrylamide also formed a gel in 0.01 M H2SO4. These experiments, summarized in Table S1 (SI), consistently demonstrated that sulfonic acid groups promoted polymerization under sono-mechanical activation.
The effect of solvent and monomer concentration on the sono-mechanical formation of poly(AMPS) gels (10 mol% MBA) showed that gelation occurred exclusively in water, while no gel formed in DMF, 1-decanol and the deep eutectic solvent (DES) formed from choline chloride and ethylene glycol in a 1
:
2 mol proportion, having low viscosity. This solvent dependence is consistent with the unique cavitation properties of water, its high vapor pressure, low viscosity, and high surface tension, which promote efficient bubble formation and collapse, enabling effective mechanical activation of AMPS. Water also dissolves AMPS uniformly due to its strong polarity and hydrogen-bonding ability, preventing phase separation that can occur in DMF or 1-decanol, where polarity mismatch limits AMPS solubility. As reported in the literature, phase-transfer catalysts can sometimes overcome such incompatibility,27,28 but without them polymerization is inefficient in these nonaqueous media. Additionally, the hydrogen-bonding environment of water stabilizes short-lived reactive intermediates, and its high thermal conductivity helps dissipate heat generated during cavitation, minimizing undesirable side reactions. In contrast, differences in physicochemical properties of DMF and 1-decanol, including vapor pressure and surface tension, alter the cavitation bubble dynamics and reduce the efficiency of energy transfer. Despite its moderate viscosity (∼40 cP), the crosslinked poly(AMPS) gel could not be formed due to reduced AMPS ionization, which prevented H+ ion catalyzation for the formation of free radicals on AMPS.
The requirement for proton availability was further validated by converting AMPS into its Na+ form, see Fig. 1. When the monomer solution was neutralized with NaOH (pH ≈ 7) and subjected to identical sonication conditions, AMPS–Na+ failed to form a hydrogel despite the presence of MBA. This clearly shows that protonated AMPS is necessary for chain activation and propagation and that neutralization effectively suppresses polymerization.
While these solvent properties influence cavitation, it can be seen from Fig. 2 that cavitation primarily serves to provide the activation energy needed for proton-assisted initiation of AMPS. Once this activation occurs, the subsequent polymerization becomes strongly dependent on the monomer concentration rather than on bulk solvent characteristics. This trend is evident in Fig. 2, i.e. increasing AMPS concentration accelerates gelation and increases conversion. For example, 2.4 mol L−1 results in complete gelation in 5 min, while 0.6 mol L−1 results in only 85% conversion in 20 min. Although increasing the water volume from 10 mL to 20 mL changes the total liquid volume, it dilutes the monomer and lowers the local concentration of reactive species, an effect that directly slows network formation. Consequently, gelation time is only weakly sensitive to moderate changes in total solvent volume, because the rate-determining steps, after sono-mechanical activation, are governed by monomer availability and spatial proximity rather than by differences in cavitation intensity across these volumes. It was also observed that gelation time was affected by sonication power, and no gelation was observed below a threshold, which was 50 W cm−2 in the present case. It was observed that the poly(AMPS) hydrogel was not obtained in the presence of the free-radical scavenger DPPH, confirming that polymerization occurred through a free-radical polymerization mechanism.
![]() | ||
| Fig. 2 Formation of the MBA crosslinked poly(AMPS) gel in different solvents, with varying conc. of AMPS. | ||
The ESR spectra recorded at the X-band frequency are expected to exhibit the characteristic resonance of organic free radicals in the g ≈ 2.0 region (≈336 mT), confirming the formation of paramagnetic species. The spectra were acquired at 80, 120, 150, and 200 °C and are shown in Fig. S1 (SI). No detectable ESR signal was observed at 80 °C, indicating insufficient thermal activation for free radical formation. However, the progressive increase in signal intensity and improved spectral quality were observed at ≥120 °C, suggesting thermally induced radical formation in AMPS.
At 200 °C, the spectrum showed a distinct resonance when plotted as intensity versus g-value in Fig. 4, appearing as a broad signal centred at g ≈ 2.0. This is a characteristic of carbon-centred organic radicals. Although hyperfine interactions with protons of the polymer backbone are expected, no resolved splitting is observed, probably due to motional averaging and thermal line broadening at elevated temperatures.
These results confirm the formation of thermally generated radicals along the AMPS backbone, with the unpaired electron exhibiting delocalized spin density. However, the temperature required for formation of free radicals on AMPS is higher, i.e. more than 120 °C.
The radical scavenging activity (RSA) carried out using DPPH during the sonication of DI water with the same power and duration used in polymerization did not reveal the formation of free radicals in water to a significant extent. However, sonolysis of water with 20 kHz ultrasound may have generated OH˙ and H˙ radicals, but the yield might have been below the detection limit of RSA. It was observed that DPPH completely inhibited the formation of the crosslinked poly(AMPS) hydrogel by sonication (148 W cm−2 power) of an aqueous solution containing AMPS (2.4 mol L−1) and 10 mol% cross-linker for 10 min, whereas the hydrogel formed readily within 5 min in the absence of DPPH. This suggested that the polymerisation of AMPS in the present case (20 kHz sonication) occurred due to cavitation. This was based on the fact that the radical scavenger DPPH was consumed in significant amounts (85–90%) during 5 min of sonication of an aqueous solution containing AMPS (2.4 mol L−1) and AMPS (2.4 mol L−1) with 10 mol% MBA, without any gel formation. Therefore, the primary source of radicals may have originated from AMPS or AMPS–water interactions under a sonication field rather than bulk water sonolysis. Direct mechanical stretching of a small vinyl bond in solution is unlikely. However, mechanical stress caused by cavitation may induce distortion and elongation of the protonated vinyl bond, facilitating homolytic cleavage.
C bond and lowers the barrier for homolytic cleavage. Simultaneously, the applied mechanical stress stretches and distorts the protonated vinyl bond, promoting bond scission and generating monomer-centred radicals. FTIR analysis supports this mechanism by indicating the disappearance of the vinyl C
C stretching band that confirms polymerization, while the shifts in the amide and carbonyl regions indicate protonation and hydrogen-bond reorganization during activation. Once radicals are formed, chain propagation proceeds through successive radical addition to neighbouring monomer units, leading to the growth of the polymer backbone. Termination occurs either by radical recombination or by proton-mediated capping reactions. In this process, the sulfonic acid group performs dual functions, as a proton donor for activation and as a counterion for charge stabilization, thereby enabling an acid-assisted, hydrogen-bond-directed radical polymerization pathway. The sono-mechanical-based polymerization mechanism of AMPS could be explained by integrating proton activation, disruption of hydrogen-bonded clusters, and ultrasound-induced mechano-radical formation, as illustrated in Fig. 5.
![]() | ||
| Fig. 6 The variation of viscosity of AMPS solutions as a function of sonication time with a constant power of 148 W cm−2 at 20 kHz. | ||
To study the formation of poly(AMPS) under sonication, the number average molecular weight (Mn), weight average molecular weight (Mw) and polydispersity index (PD) were determined by GPC for the samples sonicated for 10 min, where the viscosity was reduced as shown in Fig. 6, and for 20 min, leading to significant rise in the viscosity. The results obtained by GPC analyses are given in Table 1. It is seen from these results that there were multiple peaks of Mn. However, there were two major peaks of Mn in both samples. In the 10 min sonicated sample, the two major peaks of Mn were at 17
885 g mol−1 (72%) and 3677 g mol−1 (25%). Both the peaks had a PD close to 1. One major Mn peak grew to 1
324
599 g mol−1 (71%) and the PD was equal to 2.27, which are characteristics of free radical-based polymerization. Other peaks had low molecular weights. For example, the second major peak of Mn was 15
034 g mol−1 (25%) in the 20 min sonicated sample. This suggested that the small growing chains were added to the main growing chain, forming higher molecular weight chains and an increase in PD. The other peaks of Mn are attributed to fragments of polymer chains caused by cavitation.
| Sample details | Peak (area) | Mn (g mol−1) | Mw (g mol−1) | PD |
|---|---|---|---|---|
| AMPS conc.: 0.8 mol L−1; 10 min sonication at 148 W cm−2 and 20 kHz | 1 (1.02%) | 619 | 632 | 1.02 |
| 2 (25.7%) | 3677 | 3914 | 1.06 | |
| 3 (71.8%) | 17 885 |
18 705 |
1.05 | |
| 4 (1.44%) | 28 886 |
30 564 |
1.06 | |
| AMPS conc.: 0.8 mol L−1; 20 min sonication at 148 W cm−2 and 20 kHz | 1 (3.2%) | 85 | 91 | 1.07 |
| 2 (0.4%) | 496 | 514 | 1.04 | |
| 3 (24.0%) | 15 034 |
15 655 |
1.04 | |
| 4 (1.2%) | 36 579 |
37 211 |
1.02 | |
| 5 (71.3%) | 1 324 599 |
3 008 040 |
2.27 |
In free radical polymerization by sono-mechanical activation, the simultaneous processes of polymerization (chain growth) and depolymerization (chain breaking) of poly(AMPS) led to multiple molecular weight peaks in GPC after 20 min of sonication. During polymerization, radical initiation and propagation resulted in chains of varying lengths, while termination through combination or disproportionation produced a broad molecular weight distribution. Depolymerization also occurred by cavitation, as seen by the rise and fall of viscosity shown in curves given in Fig. 6, where polymer chains broke into shorter fragments that could not undergo further polymerization. This process introduced additional low-molecular-weight species, further diversifying the molecular weight profile. In reversible radical systems, such as RAFT polymerization or thermal equilibrium conditions, polymerization and depolymerization can coexist dynamically, which was also observed in the sono-mechanical activation for different reasons. This equilibrium resulted in distinct high- and low-molecular-weight species, reflecting the balance between chain growth and fragmentation. Therefore, the appearance of multiple peaks in GPC could be attributed to the interplay of polymerization, depolymerization, and termination events. The formation of the hydrogel in a shorter time suggested that depolymerization did not play a significant role, and rapid crosslinking stabilized the three-dimensional network of the hydrogel. Contrary to this, chain growth free radical polymerization of poly(AMPS) involved propagation of long chains, which was inherently slower because it depended on the initiation and addition of individual monomers over a period of time. Therefore, shear forces could fragment the growing polymer chain.
It is also important to note that the water uptake capacity is also influenced by osmotic forces, which depend on the chemical conditions of the equilibrating solution. Therefore, the water uptake capacity of 10 mol% crosslinked poly(AMPS) was also studied in solutions having pH = 1, pH = 13 and 0.5 M NaCl and compared with that in deionized water. It is evident from Fig. 7b that the water uptake capacity followed the order: DI > pH = 1 ≈ pH = 13 > 0.5 NaCl. Thus, the equilibrium water uptake capacity of poly(AMPS) hydrogels crosslinked with a 10 mol% cross-linker varied significantly with the chemical composition of the equilibrating aqueous solution. The sulfonic acid group (–SO3H) is a strong acidic group and therefore remains ionized at both acidic and basic pH. This led to similar water uptake capacity at lower and higher pHs. In salt solutions, however, the ions shield the charges on the –SO3− groups, reducing the electrostatic repulsion and osmotic pressure, resulting in significantly lower water uptake. The higher uptake capacity in DI water could be attributed to the higher osmotic pressure in the poly(AMPS) hydrogel and no charge shielding.
The chemical structure of crosslinked poly(AMPS) was confirmed by studying its FTIR spectrum and comparing it with the FTIR spectra of the monomer AMPS and the crosslinker MBA. The FTIR spectra are given in Fig. S4 (SI). It is seen from the FTIR spectrum of the poly(AMPS) hydrogel shown in Fig. S4c (SI) that characteristic peaks corresponding to the amide group (N–H stretch: the broad peak around 3330 cm−1, C
O stretch: the strong peak near 1645 cm−1, and N–H bend: the peak near 1550 cm−1) and sulfonic acid group (S
O stretch: two strong peaks near 1039–1181 cm−1 and smaller peaks due to shift caused by hydrogen bonding with water) were present. The C
C stretching peak at 1612 cm−1, characteristic of the vinyl double bond in AMPS and MBA, disappeared in the poly(AMPS) hydrogel. Instead, a new peak appeared in the FTIR spectrum of the hydrogel at 1391 cm−1 due to C–N stretching vibrations from the MBA crosslinker. Thus, the FTIR spectrum comparison indicated that the expected chemical structure of the hydrogel was formed, and there was no degradation of the monomer and crosslinker during sonication.
The DSC thermograms of poly(AMPS) hydrogels crosslinked with 5 mol% and 15 mol% MBA given in Fig. 9 show characteristic thermal transitions associated with water melting and glass transition of the polymer network. It is seen for the 5 mol% MBA-crosslinked poly(AMPS) hydrogel that a single broad endothermic peak is observed in the sub-zero (−27 °C) to near-zero (8 °C) temperature region and a peak at −3.5 °C. This endothermic thermal transition could be attributed to the melting of freezable water confined within the hydrogel network as well as Tg. The broad nature of this peak indicates a distribution of water environments, primarily dominated by loosely bound or free water, weakly interacting with the sulfonate (–SO3−) groups of poly(AMPS). In contrast, the 15 mol% MBA crosslinked hydrogel exhibited two partially overlapped endothermic peaks in the water-melting region. This behavior suggests the presence of two distinct water domains within the highly crosslinked network. This first endothermic transition could be attributed to free or weakly bound water, melting closer to 0 °C. The second endothermic transition is due to more strongly bound or confined water, associated with ionic interactions and nanoscale confinement imposed by the dense crosslinking. The increased crosslink density restricts chain mobility and creates heterogeneous microdomains, leading to separation of water environments and peak splitting. It is also possible that the Tg of poly(AMPS) hydrogel with 15 mol% MBA shifts to a higher temperature and becomes broader due to restricted segmental motion, which may merge with the bound-water endotherm, resulting in the observed joined peaks. It is interesting to note that the DSC curve of the 15 mol% crosslinked hydrogel shows a more negative baseline shift compared to the 5 mol% sample. This feature is indicative of enhanced network rigidity, consistent with increased crosslink density and reduced polymer chain mobility. The stronger polymer–water interactions and higher fraction of non-freezable or strongly bound water further contribute to this baseline shift. The DSC results suggested that increasing MBA content from 5 to 15 mol% significantly alters the thermal behavior, water–polymer interactions, and microstructural heterogeneity of poly(AMPS) hydrogels.
![]() | ||
| Fig. 9 DSC curves of poly(AMPS) crosslinked with 5 mol% (dashed line) and 15 mol% (solid line) of MBA. | ||
The thermal properties of 5% MBA-crosslinked poly(AMPS) under a nitrogen atmosphere were studied by thermogravimetric analysis (TGA) and differential thermal analysis (DTA). The degradation pathway of crosslinked poly(AMPS) under N2 is expected to be an endothermic transition corresponding to dehydration and exothermic thermal transitions attributed to desulfonation of –SO3H groups, amide linkage decomposition, main-chain scission and carbonaceous char formation. The TGA and DTA curves given in Fig. S5a and b (SI) exhibit a multistep degradation pattern as expected. An initial weight loss of ∼14.6% below 150 °C corresponds to the removal of free and hydrogen-bonded water, consistent with the broad endothermic DTA peak in the corresponding region. The second degradation stage (150–300 °C) could be attributed to the degradation of –SO3H groups coincident with the release of strongly bound water. The major exothermic peaks at ∼279 °C and ∼326 °C in the DTA curve coincided with mass loss and could be assigned to sulfonic acid decomposition, followed by amide group cleavage and main-chain scission of the AMPS backbone. A minor thermal transition near 396 °C corresponded to secondary degradation and carbonization processes. The residual mass at high temperature indicated char formation.
It is important to note from Fig. 10a2 that the methylene blue dyes diffused in the unloaded cut piece under humid conditions but not in the hydrogel gel piece dried under ambient conditions, as can be seen from Fig. 10b2. This could be due to high chain mobility in the hydrogel with higher water content, which would allow the proximity of fixed binding sites. Methylene blue binds to fixed sulfonate sites via reversible ionic bonds, allowing exchange with nearby sulfonate groups. This would lead to the diffusion of bound methylene blue from one binding site to another binding site by jumping43 and lead to the uniform distribution of methylene blue in both cut pieces. However, this would not be possible when the water content is lower, leading to insufficient chain mobility required for the fixed-site jumping.
The process of self-healing in the lightly crosslinked poly(AMPS) involves true network reformation rather than surface sticking alone. This is based on the fact that when two cut hydrogel pieces, one loaded with MB, were brought into contact, the diffusion of the dye across the interface occurred after fusion overnight. Such interfacial molecular exchange requires the presence of water-swollen, dynamic polymer chains capable of interpenetration and reorganization, which is not consistent with mere surface adhesion. The microscopic observations show a gradual disappearance of the interface and reconstitution of a continuous network, supporting a self-healing mechanism driven by chain mobility and reversible hydrogen bonding interactions within the lightly crosslinked AMPS hydrogel matrix. The dye-diffusion experiment and the visualization demonstrate that the healing process arises from chain interdiffusion and network relaxation, rather than simple physical adhesion.
| Crosslinking (mol%) | Dose (wt%) | Compressive strength (MPa) | Tensile strength (MPa) | Heat of hydration (kJ kg−1) | Setting time (min) | |||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| 7 days | 28 days | 60 days | 7 days | 28 days | 60 days | 7 days | 28 days | 60 days | Initial | Final | ||
| Control | 0 | 35 ± 2 | 48 ± 3 | 57 ± 5 | 2.9 ± 0.2 | 3.5 ± 0.3 | 4.2 ± 0.4 | 298 ± 9 | 335 ± 11 | 347 ± 15 | 150 ± 15 | 210 ± 10 |
| 5 | 0.3 | 33 ± 3 | 43 ± 3 | 52 ± 5 | 2.9 ± 0.2 | 3.6 ± 0.3 | 4.3 ± 0.4 | 295 ± 9 | 334 ± 11 | 343 ± 15 | 148 ± 15 | 220 ± 10 |
| 0.5 | 32 ± 3 | 40 ± 3 | 52 ± 5 | 2.9 ± 0.2 | 3.4 ± 0.3 | 4.1 ± 0.4 | 293 ± 9 | 332 ± 11 | 343 ± 15 | 145 ± 15 | 226 ± 10 | |
| 1.0 | 33 ± 3 | 41 ± 3 | 49 ± 5 | 2.7 ± 0.2 | 3.7 ± 0.3 | 4.3 ± 0.4 | 291 ± 9 | 330 ± 11 | 346 ± 15 | 141 ± 15 | 227 ± 10 | |
| 2.0 | 29 ± 3 | 42 ± 3 | 50 ± 5 | 3.0 ± 0.2 | 3.6 ± 0.3 | 4.3 ± 0.4 | 287 ± 9 | 329 ± 11 | 342 ± 15 | 140 ± 15 | 231 ± 10 | |
| 10 | 0.3 | 34 ± 3 | 43 ± 3 | 51 ± 5 | 2.9 ± 0.2 | 3.8 ± 0.3 | 4.4 ± 0.4 | 296 ± 9 | 334 ± 11 | 345 ± 15 | 151 ± 15 | 212 ± 10 |
| 0.5 | 31 ± 3 | 40 ± 3 | 50 ± 5 | 3.0 ± 0.2 | 3.6 ± 0.3 | 4.5 ± 0.4 | 293 ± 9 | 331 ± 11 | 341 ± 15 | 149 ± 15 | 218 ± 10 | |
| 1.0 | 32 ± 3 | 40 ± 3 | 51 ± 5 | 3.0 ± 0.2 | 3.7 ± 0.3 | 4.6 ± 0.4 | 291 ± 9 | 330 ± 11 | 345 ± 15 | 143 ± 15 | 225 ± 10 | |
| 2.0 | 30 ± 3 | 41 ± 3 | 50 ± 5 | 3.1 ± 0.2 | 3.8 ± 0.3 | 4.6 ± 0.4 | 287 ± 9 | 329 ± 11 | 342 ± 15 | 146 ± 15 | 234 ± 10 | |
| 15 | 0.3 | 33 ± 3 | 42 ± 3 | 50 ± 5 | 3.0 ± 0.2 | 3.7 ± 0.3 | 4.4 ± 0.4 | 291 ± 9 | 330 ± 11 | 338 ± 15 | 149 ± 15 | 223 ± 10 |
| 0.5 | 31 ± 3 | 40 ± 3 | 51 ± 5 | 3.0 ± 0.2 | 3.7 ± 0.3 | 4.3 ± 0.4 | 291 ± 9 | 332 ± 11 | 334 ± 15 | 148 ± 15 | 225 ± 10 | |
| 1.0 | 31 ± 3 | 42 ± 3 | 51 ± 5 | 2.9 ± 0.2 | 3.7 ± 0.3 | 4.5 ± 0.4 | 290 ± 9 | 328 ± 11 | 348 ± 15 | 151 ± 15 | 227 ± 10 | |
| 2.0 | 29 ± 3 | 41 ± 3 | 49 ± 5 | 3.1 ± 0.2 | 3.7 ± 0.3 | 4.7 ± 0.4 | 285 ± 9 | 327 ± 11 | 341 ± 15 | 145 ± 15 | 239 ± 10 | |
The Ca-poly(AMPS) hydrogel contains calcium sulfate species, which are chemically analogous to gypsum commonly added to OPC to regulate the hardening process. In view of this similarity, both initial and final setting times were systematically evaluated. The results indicate that incorporation of the hydrogel exerts only a marginal influence on the initial setting time, which remains close to that of the control mixture (approximately 140–151 min). In contrast, the final setting time exhibits a moderate increase with increasing hydrogel dosage, reaching up to 239 min in certain formulations. The variation of setting times with dosage for the 15 mol% crosslinked Ca-poly(AMPS) system shown in Fig. 11 suggests that, at the maximum dosage of 2 wt%, the initial setting time decreases by about 7%, whereas the final setting time increases by approximately 10% relative to the control. The slight acceleration of the initial set may be attributed to the availability of additional calcium ions that promote early ettringite formation,46 while the moderate retardation of the final set likely arises from regulated release of water from the hydrogel network. Importantly, both the acceleration of the initial setting and the retardation of the final setting remain within acceptable practical limits for cementitious applications.
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| Fig. 11 Variation of initial and final setting times of Ordinary Portland Cement as a function of dosage of 15 mol% MBA crosslinked Ca-poly(AMPS) hydrogel. | ||
The cumulative heat of hydration data given in Table 2 suggests the hydration-regulating function of the hydrogel. At 7 days, total heat release is slightly lower for hydrogel-containing systems (approximately 285–296 kJ kg−1) compared with the control (298 kJ kg−1), indicating moderated early hydration kinetics. The reduction in early heat evolution is beneficial for minimizing thermal gradients and associated cracking risks in mass concrete applications. However, at later ages, the differences in cumulative heat become marginal, confirming that total hydration is not suppressed but temporally redistributed.
The incorporation of the crosslinked poly(AMPS) hydrogel into OPC is expected to influence the mechanical performance depending upon the crosslinking density and dosage. It is seen from Table 2 that a consistent but moderate reduction in early-age compressive strength is observed in all hydrogel-containing systems compared with the control mix. At 7 days, compressive strength decreased from 35 MPa for the control to values in the range of 29–34 MPa depending on hydrogel content. This early reduction can be attributed primarily to a localized decrease in free water availability for immediate cement hydration. Additionally, the swollen hydrogel domains may introduce early capillary porosity. Despite this initial reduction, strength development at later ages shows substantial recovery. At 28 and 60 days, compressive strength values approach those of the control system, reaching 49–52 MPa at 60 days compared to 57 MPa for neat OPC. This convergence indicates that the hydrogel does not permanently inhibit hydration. However, it redistributes the hydration process over time. As the internal relative humidity decreases during ongoing hydration, the hydrogel gradually releases stored water, enabling continued reaction of unhydrated clinker phases. This internal curing mechanism promotes secondary formation of the C–S–H gel, contributing to progressive matrix densification and partial compensation for early porosity. In contrast to compressive strength, tensile strength is maintained or slightly improved in hydrogel-modified systems, particularly at later curing ages. Values up to 4.6–4.7 MPa at 60 days are observed compared with 4.2 MPa for the control, see Table 2. The improved tensile response suggests that the hydrogel contributes to stress redistribution and microcrack control within the cementitious matrix. The polymeric domains may act as localized energy-dissipating centres, reducing crack propagation and enhancing resistance to tensile stresses. This behavior is particularly important for durability performance, where crack control is requisite.
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