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MaterialsMaterials
  • Article
  • Open Access

18 April 2026

15 Pages

Comparative Study on the Performance and Hydration Mechanism of Coal Gangue Cementitious Materials with Different Alkali Activators

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1
School of Civil Engineering, North China University of Technology, Beijing 100144, China
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China Academy of Building Research, Beijing 100013, China
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China Building Technique Group Co., Ltd., Beijing 100020, China
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School of Mine Safety, University of Emergency Management, Langfang 065201, China
This article belongs to the Section Construction and Building Materials

Abstract

Coal gangue (CG) ranks among China’s most significant industrial solid by-products. In response to China’s carbon neutrality commitments and the growing emphasis on resource recycling, finding effective ways to valorize CG has emerged as a pressing concern. Based on the mineral composition and chemical composition characteristics of CG, this study systematically investigated the enhancement effects of three alkali activators (Na2SiO3, NaOH, and Ca(OH)2) on the cementitious properties of CG. Through different dosage and compressive strength tests, the efficiency ranking of the three activators was determined as follows: Na2SiO3 > Ca(OH)2 > NaOH. A 10% Na2SiO3 dosage combined with 28-day curing was identified as the optimal condition for achieving sufficient reaction and structural densification. Under these conditions, the compressive strength of CG cementitious material reached 6.4 MPa, representing an increase of 190.9% compared to the blank group (2.2 MPa), significantly superior to Ca(OH)2 (69.55%) and NaOH (62.27%). X-ray diffraction (XRD) and scanning electron microscopy-energy dispersive spectroscopy (SEM-EDS) analyses revealed that alkali activators function primarily by disrupting the crystalline framework of CG, promoting the cross-linking polymerization of silicon–aluminum monomers to generate dense cementitious products, thereby improving material performance. The Na2SiO3 is attributed to its “dual activation effect”, providing OH− to create an alkaline environment while supplying reactive silicate ions (SiO32−) to accelerate N-A-S-H gel and C-A-S-H gel formation. These findings offer guidance for optimizing CG-based cementitious formulations for formula optimization and large-scale utilization of CG cementitious materials.

1. Introduction

Coal continues to dominate China’s energy mix; it accounted for 66.6% of the energy production structure in 2023. By the end of 2023, China’s coal reserves reached 218.57 billion tons, and raw coal production reached 4.76 billion tons in 2024, setting a historical record [1]. Intensive coal extraction has led to steadily rising CG output, showing an overall upward trend from 2011 to 2022, mainly distributed in major coal-producing areas such as Shanxi, Inner Mongolia, and Shaanxi provinces. Currently, China has formed more than 2700 gangue mountains, with a total stockpile exceeding 7 billion tons, occupying more than 200,000 mu of land, establishing CG as a major contributor to China’s industrial waste burden [2,3]. During the stockpiling process, the heavy metals and acidic substances contained in CG can easily infiltrate underground through rainwater erosion, polluting water resources and soil. Meanwhile, the loose mountain structure poses collapse risks, threatening the surrounding ecological environment and human safety [4].
To promote the resource utilization of CG, China has successively issued policies such as the “Administrative Measures for Comprehensive Utilization of CG” and “Opinions on Strengthening Clean and Efficient Utilization of Coal”, explicitly proposing to advance CG utilization in ecological restoration, backfilling mining, and engineering construction. CG is rich in minerals such as kaolinite and quartz, as well as chemical components like Al2O3 and SiO2, possessing the potential for transformation into resource products such as cementitious materials and adsorbent materials [5,6]. However, its low natural reactivity limits high-value utilization efficiency, making activation technology to enhance its performance a key research direction [7,8,9,10].
Alkali-activated materials (AAMs) are novel cementitious materials prepared using industrial solid wastes as raw materials and alkaline solutions as activators, with advantages of low carbon footprint, environmental friendliness, and excellent mechanical properties [11,12]. The alkali activation process is generally understood to proceed through dissolution of Si-O and Al-O bonds in the precursor under high-pH conditions, followed by condensation polymerization of dissolved silicate and aluminate species into gel networks—predominantly N-A-S-H or C-A-S-H gels depending on the Ca content of the system [13]. Common alkali activators include NaOH, Ca(OH)2, and Na2SiO3, each imparting distinct activation pathways. NaOH provides strong alkalinity that promotes rapid dissolution of Si-Al phases in the precursor; however, the absence of an external silicon source limits the density of the resulting gel network [14]. Ca(OH)2 supplies Ca2+ ions that favor C-A-S-H gel formation and long-term strength development, but its relatively low solubility restricts early-age reactivity [15,16,17,18]. Na2SiO3 simultaneously provides OH− for alkaline activation and SiO32− as an additional reactive silicon source, which accelerates gel polycondensation and promotes denser microstructures; the silicate modulus has been identified as a critical parameter governing gel product composition and mechanical performance [7].
Regarding CG-based AAMs specifically, Wang et al. [8] demonstrated that activator type is a decisive factor controlling the mechanical behavior of CG-based alkali-activated systems. Feng et al. [10] explored the alkali activation of spontaneous combustion CG, emphasizing the importance of raw material characteristics on cementitious performance. Zhang et al. [9] reported that thermal pre-treatment of CG significantly enhances its reactivity toward alkali activation by converting crystalline kaolinite to amorphous metakaolinite. However, the majority of existing studies have focused on CG–slag or CG–fly ash blended systems [14], in which the contributions of supplementary cementitious materials and activator chemistry are inherently coupled and difficult to separate. Systematic comparative studies of CG systems—without supplementary materials—under identical activator dosage conditions remain scarce. Furthermore, while the relative merits of individual activators have been discussed in blended systems, the mechanistic basis for performance differences among NaOH, Ca(OH)2, and Na2SiO3, specifically in CG precursor systems, at the phase evolution and microstructural level, has not been established.
To address the above issues, this study uses CG from Taiyuan, Shanxi as the sole precursor and systematically investigates the effects of three alkali activators—NaOH, Ca(OH)2, and Na2SiO3—at identical dosage levels (5%, 7%, 10%, and 12%) on the cementitious properties of CG. XRD phase analysis and SEM-EDS are employed to characterize phase evolution and microstructural development across activator types and curing ages. The specific objectives are as follows: (1) to determine the compressive strength development patterns and activation efficiency ranking of the three activators in a CG system; (2) to identify the phase assemblages and microstructural features associated with each activator type; (3) to provide practical guidance for optimizing alkali activator selection for large-scale CG valorization, such as mine backfill.

2. Materials and Methods

2.1. Experimental Materials

2.1.1. Coal Gangue

CG constitutes the lithic fraction discarded throughout coal extraction and processing operations, predominantly comprising mineral assemblages including kaolinite, mica, and quartz. The CG specimens investigated herein were sourced from a Taiyuan-based colliery, Shanxi, subjected to jaw crushing followed by ball milling for 2 h before sieving. The chemical composition of CG was determined by X-ray fluorescence (XRF) spectrometry using a PANalytical Axios spectrometer (Malvern Panalytical Ltd., Malvern, UK, as described in Section 2.3.2). The elemental oxide distribution is presented in Table 1. It can be seen that the main chemical components of CG are SiO2, Al2O3, and Fe2O3, with a silicon–aluminum ratio (SiO2/Al2O3) of 2.73. The XRD pattern shown in Figure 1a indicates that the main minerals in this CG are quartz, mica, calcite, and kaolinite, demonstrating its potential as a precursor for alkali-activated materials [15]. The micromorphology shown in Figure 1b reveals that CG consists of loose particles without agglomeration. Particle size distribution curve of CG shown in Figure 2.
Table 1. Main chemical composition of CG samples.
Figure 1. XRD pattern and micromorphology of CG: (a) XRD pattern; (b) SEM micrograph.
Figure 2. Particle size distribution curve of CG.

2.1.2. Activators

Three alkaline activators were employed: NaOH, Ca(OH)2, and Na2SiO3 solution. NaOH and Ca(OH)2 were analytical grade with 99% purity (Sinopharm Chemical Reagent Co., Ltd., Shanghai, China). Na2SiO3 had a modulus of 1.0 M, with Na2O content of 19.3% (industrial grade, Shandong Silicate Co., Ltd., Jinan, China).

2.2. Experimental Procedure and Design

This study examined how different alkali activators influence CG cementitious performance. Three activators, Ca(OH)2, NaOH, and Na2SiO3, were tested at varying dosages. Compressive strength measurements were used to evaluate the activation efficiency. The experimental procedure and mix proportions are presented in Figure 3 and Table 2, respectively. The activator dosage refers to the mass percentage of the alkali activator relative to the mass of coal gangue. The water-to-binder (W/B) ratio refers to the ratio of the mass of water to the sum of the masses of the alkali activator and coal gangue.
Figure 3. Experimental flow chart.
Table 2. Mix proportions for CG cementitious performance tests.

2.3. Test Methods

2.3.1. Particle Size Distribution Test

Laser particle size distribution tests were performed on CG using the dry method to avoid interference from water-soluble components. The test instrument was a Mastersizer 3000 laser particle size analyzer (Malvern Panalytical Ltd., Malvern, UK). An appropriate amount of powder was placed in the dry dispersion system, with dispersion pressure set at 0.2 MPa, 3 scans, using air as the dispersion medium, to determine the particle size distribution range (D10, D50, and D90) and distribution curves. This test aimed to characterize the particle gradation of CG raw material and assess its influence on the alkali-activation reaction rate and cementitious material performance.

2.3.2. Multi-Element Analysis

Multi-element analysis of CG raw materials was performed. Chemical analysis was conducted via XRF spectrometry. The test instrument was a PANalytical Axios X-ray fluorescence spectrometer (Malvern Panalytical Ltd., Malvern, UK). In total, 5 g of powder was pressed into a 40 mm diameter disk sample using the boric acid edge pressing method (pressure 30 MPa; holding time 30 s). Detection parameters were set as reference [14]. Analyzed elements included major oxides and trace heavy metal oxides, aiming to clarify key chemical characteristics of raw materials such as silicon–aluminum ratio and calcium content, providing data support for revealing the material basis of alkali-activation reactions in blended systems.

2.3.3. Preparation of Alkali-Activated CG Specimens

CG raw material, water, and alkali activator were sequentially added to the cement mortar mixer pot, followed by slow mixing for 180 s, pausing for 10 s, then fast mixing for 180 s. The mixed alkali-activated material was transferred into 40 mm cubic steel molds, followed by mechanical vibration (30 s) for void elimination. After smoothing the surface, specimens underwent controlled curing (>90% RH; 20 ± 1 °C) in a humidity chamber, with performance testing conducted after curing for 3 d, 7 d, and 28 d, respectively. Each group of experiments was performed in triplicate.

2.3.4. Compressive Strength Test

Compressive strength was measured on a YAW-300B servo-controlled testing machine at a loading rate of 2.4 kN/s, with reference to the loading procedure specified in GB/T 17671-2021 [19]. The compressive strength (Rc) was determined using Equation (1):
Rc = Fc/A
where Fc represents the maximum load applied at failure of the 40 mm cubic specimen (N), and A represents the compressed area of the cube face (40 mm × 40 mm = 1600 mm2).

2.3.5. XRD Analysis

Phase composition analysis of CG raw materials and specimens (ground into powder) was performed using a Bruker D8 Advance XRD. Parameters were adopted from prior work [14]. During analysis, the diffraction peak positions and intensities in the patterns were compared with standard phase databases (ICDD PDF-2 database) to determine the phases present in the samples.

2.3.6. SEM Analysis

Specimens were tested using an FEI Quanta 650 SEM coupled with a Bruker QUANTAX EDS spectrometer. Dried samples were cut into small pieces to form fresh fracture surfaces of approximately 0.5–1 cm2, gold-sputtered, and then observed under the SEM combined with EDS analysis.

3. Results and Discussion

3.1. Compressive Strength Analysis

The compressive strength development patterns of CG cementitious materials with different alkali activators and different dosages are shown in Figure 4a–c. Each group was tested in triplicate, and the results are presented as mean values with standard deviation.
Figure 4. Effects of different alkali activators and dosages on compressive strength: (a) Na2SiO3; (b) Ca(OH)2; (c) NaOH.
As shown in the figures, under the action of three different alkali activators, compressive strength exhibited a positive correlation with activator concentration. When the specimens were cured for 28 d, the strength without an alkali activator was 2.2 MPa. When the activator dosages were 5%, 7%, 10%, and 12%, the compressive strengths corresponding to Na2SiO3 were 4.51, 5.74, 6.4, and 6.76 MPa, with growth rates of 105.0%, 160.9%, 190.9%, and 207.3%, respectively; the compressive strengths corresponding to Ca(OH)2 were 2.84, 3.34, 3.73, and 3.97 MPa, with growth rates of 29.09%, 51.82%, 69.55%, and 80.45%, respectively; the compressive strengths corresponding to NaOH were 2.58, 3.23, 3.57, and 3.74 MPa, with growth rates of 17.27%, 46.82%, 62.27%, and 70.00%, respectively. The above results indicate the three activators exhibited markedly different activation capacities on CG, with efficiency ranking as follows: Na2SiO3 > Ca(OH)2 > NaOH. To further verify the differences in activation efficiency among the three activators, phase composition and microstructural analyses are presented in Section 3.2.
At the same activator dosage, Na2SiO3 shows the most significant activation effect. At 10% activator dosage, the compressive strengths at 3 d, 7 d, and 28 d curing were 1.47, 1.84, and 1.72 times those of Ca(OH)2, and 1.20, 1.19, and 1.79 times those of NaOH, respectively. Therefore, the advantage of Na2SiO3 is more significant at the same dosage. This is mainly because the hydrolysis of Na2SiO3 enhances the cementitious properties of CG through dual pathways: in addition to the OH− generated enhancing system alkalinity to promote dissociation of silicon–aluminum phases in the CG system and release of active components, it also provides silicate ions (SiO32−) as an external silicon source, which combines with dissolved aluminum species and sodium ions, forming dense cementitious structures dominated by amorphous hydrated sodium aluminosilicate (N-A-S-H) gel, as evidenced by the broad diffuse humps in XRD patterns rather than crystalline diffraction peaks through condensation reactions [20,21].
The formation of cementitious gel products in alkali-activated CG systems can be understood from a molecular chemistry perspective. Under alkaline conditions, OH− ions attack and cleave the Si-O-Si and Si-O-Al bonds in the CG mineral framework, releasing soluble silicon and aluminum monomers according to the following reactions:
Si-O-Si + OH− → H3SiO4−/H2SiO42−
Al-O-Al + OH− → Al(OH)4−
The released monomers subsequently undergo condensation polymerization. In the presence of Na+, aluminate and silicate ions cross-link to form amorphous N-A-S-H gel:
Na+ + Al(OH)4− + H3SiO4− → N-A-S-H gel
In systems where Ca2+ is available (Ca(OH)2, the activator or calcium released from CG), C-A-S-H gel forms through the following reaction:
Ca2+ + H3SiO4− + Al(OH)4− → C-A-S-H gel
In the sodium silicate system, the additional supply of SiO32− ions further promotes reactions Equations (4) and (5), accelerating gel network formation and contributing to the superior cementitious performance observed.
To further verify the action mechanisms of the three activators, phase and microstructure analyses were performed.

3.2. Hydration Reaction Mechanism Analysis

3.2.1. Phase Composition Analysis

Figure 5a,b show the XRD patterns of Na2SiO3, Ca(OH)2, and NaOH at 5% dosage after 7 d and 28 d curing; Figure 5c,d show the XRD patterns of each activator at 10% dosage after 7 d and 28 d curing. First, the CG samples mainly contain mineral phases such as quartz, kaolinite, calcite, and mica. After alkali activation, phase changes occurred in all systems.
Figure 5. XRD patterns of CG with different alkali activators and dosages: (a) 5% dosage, 7 d curing; (b) 5% dosage, 28 d curing; (c) 10% dosage, 7 d curing; (d) 10% dosage, 28 d curing.
As can be seen from the figures, following alkaline treatment, quartz diffraction intensities diminished universally. Moreover, after activation of CG with Na2SiO3 and NaOH, broad amorphous humps characteristic of N-A-S-H and C-A-S-H gels were observed in the 2θ = 10–35° region, consistent with their known amorphous to semi-crystalline nature. These gel phases do not produce sharp diffraction peaks but are identified by the broadened diffuse scattering features, which intensified with increasing activator dosage, indicating greater gel formation. After activation with Ca(OH)2, AFt and amorphous C-A-S-H gel were observed. With increasing activator dosage, the diffraction peaks of cementitious products significantly increased. At 10% dosage, activation product peaks were stronger, original mineral (quartz and kaolinite) peaks were weaker, reactions were more complete, and amorphous gel formation (N-A-S-H, C-A-S-H) and AFt precipitation (Ca(OH)2 activator) were more pronounced. According to Figure 5a–d, different activator types affect product phases: Na2SiO3 and NaOH systems are dominated by N-A-S-H and C-A-S-H, exhibiting persistent accumulation over extended durations; Ca(OH)2 activator, due to calcium ions, shows persistent prominent AFt peaks and enhanced C-A-S-H, reflecting its long-term contribution to ettringite and silicate gel [22]. Na2SiO3-activated samples exhibit the most prominent broad diffuse humps in the 2θ = 10–40° range, consistent with a greater extent of amorphous N-A-S-H gel formation [23,24,25] (Si-5-7, Si-5-28, Si-10-7, Si-10-28), with peak intensity significantly increasing with dosage, corresponding to the 28 d compressive strength growth rate of 207.3%, highly consistent with macroscopic mechanical properties. Therefore, the phase evolution results demonstrate that Na2SiO3 hydrolysis provides both an alkaline environment and an additional reactive silicon source, efficiently activating active silicon–aluminum components in CG and generating large amounts of amorphous cementitious products. In contrast, NaOH and Ca(OH)2-activated samples show relatively lower intensity of the amorphous hump in the XRD patterns, with inert phases (such as quartz) dominating, relying only on alkaline activation without active silicon supplementation, resulting in limited 28 d strength increases of 70.0% and 80.45%, respectively. This shows that Na2SiO3 has a dual activation effect, with its phase evolution highly consistent with macroscopic strength data, showing significant advantages in promoting cementitious product formation and improving later-age strength, while NaOH and Ca(OH)2 have weaker effects due to their single activation mechanism relying only on alkaline activation. Ca(OH)2 activator favors long-term AFt presence, while Na2SiO3 and NaOH activators dominate silicate gel accumulation, illustrating the long-term mineral phase evolution and activator regulation effects of alkali-activated materials.

3.2.2. Microstructure Analysis

Activation of CG Cementitious Properties by Na2SiO3
Figure 6 and Figure 7 show the SEM images of specimens at 5% and 10% Na2SiO3 dosage after 7 d and 28 d curing, respectively. Table 3 shows the elemental composition derived from the EDS spectra in Figure 6. As can be seen from Figure 6, at 5% Na2SiO3 dosage, CG hydration remained incomplete, yielding a porous microstructure, numerous cracks, and many unreacted particles. Extending curing time from 7 d to 28 d had a limited effect on performance improvement, indicating that low-dosage Na2SiO3 failed to effectively promote the formation of dense gel networks. At 28 d curing, C-A-S-H gel content slightly increased but was still insufficient to significantly improve structural compactness (Figure 6c,d).
Figure 6. SEM images of specimens with 5% Na2SiO3 at 7 d and 28 d curing: (a,b) 7 d curing; (c,d) 28 d curing.
Figure 7. SEM images of specimens with 10% Na2SiO3 at 7 d and 28 d curing: (a,b) 7 d curing; (c,d) 28 d curing.
Table 3. Based on the elemental composition derived from the EDS spectra in Figure 6.
In contrast, specimens at 10% Na2SiO3 dosage showed significantly enhanced compactness, reduced voids, and a tight structure compared to 5% specimens with extended curing time. At 7 d curing (Figure 7a,b), N-A-S-H gel constituted the predominant hydration phase, with small amounts of C-A-S-H gel formed in local areas. At 28 d curing in later hydration reactions (Figure 7c,d), N-A-S-H and C-A-S-H became the dominant phases, calcium content significantly increased (15–19%), Si/Al ratio stabilized at 6.0–8.0, and microstructural densification was markedly enhanced. Furthermore, Figure 7d shows that the two gels, N-A-S-H and C-A-S-H, are interconnected, indicating that they do not simply stack inside the solidified body but interact to jointly promote polymerization reactions in the system. This synergistic effect significantly improves solidification efficiency, thereby enhancing the mechanical properties of materials [26]. Combining Table 4, Na2SiO3 dosage has a significant influence on CG alkali-activated cementitious materialization reactions.
Table 4. Based on the elemental composition derived from the EDS spectra in Figure 7.
Activation of CG Cementitious Properties by Ca(OH)2
Figure 8 and Figure 9 show the SEM images of specimens at 5% and 10% Ca(OH)2 dosage after 7 d and 28 d curing, respectively. As can be seen from Figure 8, at 5% Ca(OH)2 dosage, the system structure was loose in early hydration (Figure 8a,b), with few hydration products, much residual Ca(OH)2, small amounts of C-A-S-H gel, and limited aluminosilicate products. At 28 d curing (Figure 8c,d), the structure was slightly denser, hydration products slightly increased, C-A-S-H gel was more typical, and AFt also formed, but overall reaction was slow, and according to EDS spectra (Table 5), aluminum phase participation was limited.
Figure 8. SEM images of specimens with 5% Ca(OH)2 at 7 d and 28 d curing: (a,b) 7 d curing; (c,d) 28 d curing.
Figure 9. SEM images of specimens with 10% Ca(OH)2 at 7 d and 28 d curing: (a,b) 7 d curing; (c,d) 28 d curing.
Table 5. Based on the elemental composition derived from the EDS spectra in Figure 8.
As can be seen from Figure 9, at 10% Ca(OH)2 dosage, early hydration showed loose structure, poor uniformity, and few hydration products. With curing time extended to 28 d, the structure became significantly dense, hydration products notably increased, C-A-S-H gel dominated the structure, and system cementitious properties improved. With the addition of alkaline activator, as the curing time extended from 7 d to 28 d, all systems transformed from loose and porous to dense structures, hydration reactions became more complete, product types became richer, and, in addition to AFt, CaCO3 also appeared according to EDS (Table 6). These products jointly filled pores and improved structural stability, reflecting the time-dependent characteristics of Ca(OH)2 activation of CG [27,28]. Meanwhile, prolonged curing is favorable for complete hydration reactions.
Table 6. Based on the elemental composition derived from the EDS spectra in Figure 9.
Activation of CG Cementitious Properties by NaOH
Figure 10 and Figure 11 show the SEM images of specimens at 5% and 10% NaOH dosage after 7 d and 28 d curing, respectively. At 5% NaOH dosage, at 7 d curing (Figure 10a,b), early hydration showed rough specimen surfaces, irregular particles, and many pores; at 28 d curing (Figure 10c,d), the structure was denser, large pores were reduced, and particles were tightly connected with network-like trends. At 5% NaOH dosage, according to EDS elemental ratios(Table 7), at 7 d curing (Figure 10b), mainly N-A-S-H gel formed with limited calcium participation; at 28 d curing (Figure 10d), the continued development of the gel network was observed morphologically, with Al-containing phases identified in local areas, while more continuous N-A-S-H networks also formed, and sodium-rich N-A-S-H gel also appeared.
Figure 10. SEM images of specimens with 5% NaOH at 7 d and 28 d curing: (a,b) 7 d curing; (c,d) 28 d curing.
Figure 11. SEM images of specimens with 10% NaOH at 7 d and 28 d curing: (a,b) 7 d curing; (c,d) 28 d curing.
Table 7. Based on the elemental composition derived from the EDS spectra in Figure 10.
As shown in Figure 11, at 10% NaOH dosage, at 7 d curing (Figure 11a,b), particle aggregates were relatively dispersed, with later-stage structure further densifying and particle boundaries becoming blurred. Early alkali-activation reactions were intense, generating large amounts of N-A-S-H gel with little calcium-based mineral participation; at 28 d curing (Figure 11c,d), N-A-S-H gel still dominated, with Na/Si ratio at some EDS measurement points decreasing (Table 8), gel structure transitioning to more stable networks, and silicon–aluminum polymerization degree increasing. In summary, with extended curing time, Na+ utilization became more complete, the microstructure progressively densified with extended curing time, suggesting continued reaction between the activator and CG particles. Meanwhile, the microstructure transformed from loose packing to dense, the element distribution became more uniform, and hydration product stability and cementing ability significantly improved.
Table 8. Based on the elemental composition derived from the EDS spectra in Figure 11.
Integrating the SEM-EDS analysis results, the microstructure evolution patterns of the three activator systems can be summarized as follows: (1) Extended curing time promotes structural densification in all systems, but the Na2SiO3 system achieves the highest degree of densification; (2) Alkali activators destroy CG crystal structures by providing an alkaline environment (OH−), causing Si-O-Si and Si-O-Al bond breakage, releasing soluble silicon–aluminum monomers (H3SiO4−, Al(OH)4−), which then cross-link and polymerize through Si-O-Al and Si-O-Si bonds to generate cementitious products (N-A-S-H, C-A-S-H, AFt, etc.), filling interparticle gaps and reducing porosity, ultimately improving material strength. In the Na2SiO3 system, N-A-S-H and C-A-S-H gels develop synergistically; in the Ca(OH)2 system, C-A-S-H dominates, accompanied by AFt; while the NaOH system is dominated by N-A-S-H; (3) 10% Na2SiO3 activator dosage combined with 28 d curing is the optimal condition for achieving sufficient reaction and structural densification.

4. Conclusions

(1) In terms of macroscopic properties, both activator chemistry and concentration exert strong control over the strength development of CG specimens. With increasing alkali activator dosage (5–12%), specimen compressive strength shows an increasing trend. Among them, Na2SiO3 has the best activation effect, with compressive strength reaching 6.4 MPa at 10% dosage after 28 d curing, a growth rate of 190.9%; Ca(OH)2 and NaOH have weaker activation effects, with strength growth rates of 69.55% and 62.27%, respectively, under the same conditions. The efficiency ranking of the three activators is as follows: Na2SiO3 > Ca(OH)2 > NaOH. Experimental results indicate that 10% Na2SiO3 dosage combined with 28 d curing is the optimal condition.
(2) Microstructure and phase evolution results further confirm the macroscopic property patterns. XRD analysis shows that Na2SiO3 sodium silicate activation leads to a greater reduction in crystalline mineral (quartz, kaolinite) peak intensities and more prominent amorphous gel formation compared to Ca(OH)2 and NaOH systems, with Ca(OH)2 additionally producing AFt.
(3) SEM-EDS analysis showed that at low activator dosage (5%), all systems exhibited loose, porous microstructures with substantial unreacted particles. At 10% dosage after 28 d curing, microstructural densification was significantly enhanced in all systems. In the sodium silicate system, co-existing N-A-S-H and C-A-S-H gels were observed with increased calcium content. In the Ca(OH)2 system, C-A-S-H and CaCO3 jointly filled interparticle pores. In the NaOH system, a more continuous N-A-S-H gel network developed compared to lower dosages and shorter curing durations. Na2SiO3, with its dual function of alkaline activation and active silicon supplementation, shows significant advantages in promoting CG activation.
It should be noted that the current study is limited to a pure CG system without supplementary cementitious materials, and the long-term durability and leaching behavior of the activated products remain to be investigated. Future work will focus on optimizing composite activator systems, evaluating the environmental safety of heavy metal immobilization, and scaling up the formulation for field application in mine backfill engineering.

Author Contributions

Conceptualization, C.G., Q.L. and Y.G.; Writing—original Draft Preparation, Y.G., C.G., and Y.W. (Yajie Wang); Writing—Review and Editing, Q.L., C.G., X.S. and Y.W. (Yajie Wang); Visualization, W.L., C.C., H.Z. and Y.W. (Yukai Wang); Supervision, Q.L., Z.M. and X.S. All authors have read and agreed to the published version of the manuscript.

Funding

This work was supported by the Outstanding Young Scientist Program Project of Beijing Universities (No. JWZQ20240101017), the Key Science and Technology Program of the Ministry of Emergency Management of China (No. 2025EMST080201).and the Scientific Research Foundation for North China University of Technology (No. 11005136025XN076-051) and Open Research Fund Program of the State Key Laboratory of Hydroscience and Engineering (sklhse-KF-2025-C-01).

Data Availability Statement

The original contributions presented in this study are included in the article. Further inquiries can be directed to the corresponding author.

Conflicts of Interest

Author Zongyuan Mao was employed by the company China Academy of Building Research and China Building Technique Group Co., Ltd. The remaining authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.

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