1. Introduction
Steel slag, a non-metallic byproduct generated during the steelmaking process, accounts for approximately 15%-20% of crude steel production [
1,
2,
3]. Globally, steel slag production is estimated to be around 190-280 million tons per year, with China contributing approximately 50% of the total and its production continuing to rise [
4,
5,
6]. By proper treatment and utilization, steel slag can not only contribute to resource conservation but also reduce environmental pollution. Additionally, the comprehensive utilization of steel slag has the potential to lower production costs and enhance economic benefits. Steel slag utilization in Japan, Europe, the United States, and China is shown in
Figure 1. Steel slag can be disposed in road construction, cement production, internal recycling, civil engineering, and agriculture in Japan, Europe, the United States, and China [
2,
3,
4,
5,
6]. It is noteworthy that 30%-50% of steel slag is used for road construction in other countries, while more than 70% of steel slag is final disposal. Therefore, compared to developed countries such as Japan and the United States, which achieve nearly 100% utilization rates, actual comprehensive utilization rate of steel slag in China is only 30% [
2,
3]. The low utilization rate of steel slag results in a significant accumulation of waste, occupying land resources and posing environmental risks due to the leaching of heavy metals like Mn and Cr. This situation impedes sustainable development of the steel industry [
7,
8,
9]. Consequently, it has become crucial to address how to improve the comprehensive utilization rate of steel slag and transform it from waste into a valuable resource.
The predominant form of steel slag in China is derived from the converter process, composing approximately 70% of the accumulated steel slag reserves. Its components, including tricalcium silicate (C
3S), dicalcium silicate (C
2S), calcium aluminate, and calcium iron aluminate, are similar to the active components of Portland cement clinker [
7,
8,
9,
10,
11,
12,
13]. Owing to these similarities, steel slag exhibits a measure of hydraulicity, which has led to its designation as a 'substandard cement' or low-quality cement. This identifies it as a prospective sustainable cementitious material with inherent green qualities. However, due to the limited amount of active components in steel slag, when it is used solely as a cementitious material, it has inherent drawbacks such as slow reaction rate, low degree of reaction, low and slow development early strength [
14,
15]. Given the shared metallurgical lineage between ground granulated blast furnace slag (GBFS) and steel slag, the former is being considered for co-treatment with the latter to improve its performance as a cementitious material. When steel slag is mixed with GBFS, the clinker-like characteristics of steel slag and the pozzolanic reaction characteristics of GBFS can mutually promote the hydration process, significantly improving the reaction degree of the composite system, especially the later strength of the composite system. However, steel slag-GBFS cementitious material (SGM) remains limited due to extended setting times and inadequate early strength, which fail to satisfy the demands of various engineering requirements [
16,
17,
18,
19,
20,
21,
22,
23,
24,
25,
26,
27,
28]. To remedy these deficiencies, the addition of modifiers such as gypsum, cement clinker, and alkaline activators has greatly improved the hydration behavior of SGM, accelerating the development and application of steel slag in the field of cementitious materials.
Based on extensive research by both domestic and international scholars on SGM, this paper analyzes and summarizes the existing research results from the perspectives of hydration characteristics, setting time and workability of fresh mortar, mechanical properties, durability, and volume shrinkage of hardened mortar. Furthermore, the paper delves into the effects of modifiers on the performance of SGM. It elucidates how these materials improve the overall characteristics of cementitious materials, while also providing an in-depth analysis of the underlying mechanisms that contribute to this enhancement. Finally, the existing issues in current research and future development trends are analyzed and discussed, aiming to provide theoretical and technical support for the application and promotion of SGM.
2. Synergistic Hydration of SGM
Steel slag itself exhibits a certain degree of hydraulicity and can react with water at room temperature, while GBFS has limited reactivity with water and requires activation in an alkaline environment with a pH value higher than 12.5 [
29,
30,
31,
32]. Studies have found that when steel slag and GBFS are mixed, there is a synergistic effect in terms of hydration [
33,
34]. The hydration mechanism of SGM is illustrated in
Figure 2. Upon contact with water, active components such as calcium aluminate and C
3S in steel slag dissolve, releasing Ca
2+, OH
-, and small amounts of Al
3+ and Si
4+. This results in an increase in the pH of the pore solution, represented by the "steep and high" first exothermic peak (S1) in the heat evolution rate curve [
34]. After a short induction period (S2), the early hydration of the small amount of calcium aluminate, C
3S, and β-C
2S in steel slag leads to the acceleration of hydration and the formation of the second peak (S3) [
34]. At this stage, Si-O-Al and Si-O-Si bonds in the GBFS are broken in the alkaline environment [
34]. The hydration products of steel slag, namely Ca(OH)
2 and C-S-H gel, precipitate and cover the surfaces of C
3S and C
2S particles, thereby reducing the hydration rate and entering the deceleration period (S4) [
34]. After a long stabilization period (S5), the hydration of Si-O-Al and Si-O-Si bonds in the GBFS, along with the reaction between [SiO
4]
4- and [AlO
4]
5- released from GBFS and Ca(OH)
2 in the system, lead to the reacceleration of the reaction rate and the appearance of the third exothermic peak (S6) [
34]. As hydration progresses, two types of gel products, namely calcium silicate hydrate (C-S-H) gel and calcium aluminate hydrate (C-A-H) gel, accumulate on the surfaces of mineral particle, and the rate of volcanic ash reaction gradually decreases and tends to stabilize (S7) [
34]. Some researchers have suggested that the highest reaction degree is achieved when the mass ratio of steel slag to GBFS is 1:1 or 2:3 [
16,
17,
18,
19,
20]. It is important to note that the products of volcanic ash reaction are not solely C-S-H and C-A-H gels, but also include calcium aluminosilicate hydrate (C-A-S-H) gel.
Due to the limited alkalinity provided by the self-hydration of steel slag, SGM is known to have slow reaction rates and a lack of early strength. In order to address this issue, SGM is commonly modified with materials such as gypsum (natural gypsum and industrial by-product gypsum), cement clinker, or alkaline activators (e.g., sodium silicate, Ca(OH)
2, NaOH, and Na
2CO
3) [
35,
36,
37,
38,
39,
40,
41,
42,
43]. Ca(OH)
2 generated by hydration of cement clinker and OH
- provided directly by alkaline activators create a more alkaline environment for cementitious materials, accelerating the dissociation of [SiO
4]
4- and [AlO
4]
5- in the GBFS and further improving the early strength of the composite system. However, it should be noted that excessive amounts of certain modifiers, such as excessive cement clinker, NaOH, and Na
2CO
3, may actually reduce the later strength of cementitious materials. This is because in the later stages of hydration, excessive OH
- or CO
32- combines with Ca
2+ on the surface of particles to form excessive Ca(OH)
2 and CaCO
3, hindering the continuous hydration of both steel slag and GBFS particles [
36]. On the other hand, sodium silicate plays a dual activation role by providing OH
- and [SiO
4]
4-, thereby not only offering an alkaline environment but also suppling the necessary silicon source for reactions, ensuring the development of later strength [
44,
45,
46].
Gypsum is an effective modifier, and steel SGM with gypsum system exhibits excellent performance. Studies have shown that steel slag, GBFS, and gypsum exhibit significant synergistic effects during the hydration process [
47,
48]. These effects are mainly attributed to the reactions where the OH
- provided by steel slag, the Al
3+ from steel slag and GBFS, and the SO
42- from gypsum react with the Ca
2+ in the system. This reaction leads to the formation of insoluble calcium aluminate (AFt), driving the continuous progress of the reaction. Xu et al. [
49] conducted a study on the effects of three types of industrial by-product gypsum, namely desulfurization gypsum (DG), desulfurization ash (DA), and fluorogypsum (FG), on the hydration and hardening properties of SGM. The results indicate that in the early stages, needle-rod-shaped AFt and amorphous gel are formed in all three cementitious systems. However, the DA system, which has a lower gypsum content, shows a significantly lower amount of AFt compared to the other systems. In the later stages, both the DG system and the FG system exhibit similar structures, characterized by interlaced AFt and gel filling and encapsulation. In contrast, DA system only shows gel formation without a distinct AFt structure. As a result, the presence of AFt in the DG and FG systems contributed to higher early strength of SGM. The microstructures of the hardened pastes in the DG and DA systems are shown in
Figure 3. It can be observed that the gel morphology differs significantly between the two systems. The gel in the DG system appears cluster-like (
Figure 3a), while the gel in the DA system exhibits a network-like structure due to the relatively higher amount of space provided by the lower AFt content (
Figure 3b). The hydration mechanism of these three composite systems using the DG system as an example is shown in
Figure 4. In the initial stages, the hydration of steel slag (Equation 1) and the dissolution of DG release OH
-, Ca
2+, and SO
42-. At the same time, under alkaline conditions, Si-O-Al and Si-O-Si bonds in the GBFS are broken, resulting in the formation of [SiO
4]
4- and [AlO
4]
5- monomers. Subsequently, the reaction between Ca
2+, SO
42-, and [AlO
4]
5- produces AFt (Equation 2), while the reaction between Ca
2+ and [SiO
4]
4- leads to the formation of C-S-H gel (Equation 3). Finally, the continuous production of C-S-H gel fills and encapsulates the interwoven AFt, ensuring the development of later strength. Therefore, the ultimate hydration products of SGM with gypsum are C-S-H gel and AFt.
When cement clinker is used as a modifier, its effectiveness is limited. Zhao et al. [
50] prepared various SGM and compared them with the Portland cement system to study the differences in hydration processes and pore structures. Overall, the cumulative heat of SGM at all ages is lower than that of Portland cement, and the cumulative heat within 72 h is less than 50% of that observed in the Portland cement system. This indicates that the alkaline environment provides solely by the hydration of cement clinker is relatively weak and insufficient to significantly enhance the initial hydration rate and reaction degree of steel slag and GBFS. Regarding the pore structure, the total porosity of hardened SGM pastes is observed to be higher compared to that of hardened Portland cement pastes. As a result, the ternary system exhibits lower density and significantly lower strength when compared to the Portland cement system. These findings suggest that the use of cement clinker as a modifier in SGM may have limitations in terms of improving the hydration process and enhancing the mechanical properties of the ternary composite. Therefore, alternative modifications such as the addition of gypsum or alkaline activators should be considered to optimize the performance of SGM.
When alkaline activators are used as modifiers, they generally provide a higher alkaline environment than cement clinker, resulting in higher hydration degree of steel slag and GBFS. You et al. [
51] studied the hydration process of alkali-activated SGM and compared the hydration rate and cumulative heat with the Portland cement system (
Figure 5). The heat evolution rate and cumulative heat of alkali-activated GBFS materials exhibit similar hydration processes to those of the Portland cement. However, alkali-activated SGM has a lower and delayed peak value of the main exothermic peak compared to the alkali-activated GBFS material. This is primarily due to the lower reactivity of steel slag, which causes a delay in the appearance and reduced the peak value of the main exothermic peak. The cumulative heat within 7 h of the alkali-activated SGM is higher than that of the Portland cement system, but within 72 h it was only 53% of that of Portland cement. This indicates that alkali-activated SGM has a higher early-stage heat and functions as a low-heat cementitious material. Furthermore, the incorporation of retarders effectively delays the occurrence of the main exothermic peak and reduces the hydration heat rate of alkali-activated SGM, prolonging the setting time of the cementitious system. In terms of hydration products, C-A-S-H gel is the main product in alkali-activated SGM. The relative content of steel slag and GBFS does not change the type of hydration products, but can affect the structure of gel products. With an increase in GBFS content, the Ca/Si ratio in C-A-S-H gel gradually decreases, while the Al/Si ratio increases, which is related to the higher aluminum content in GBFS. In relation to pore structure, compared to the Portland cement, alkali-activated SGM has a lower total porosity and a higher number of gel pores, but fewer capillary pores. This may be due to the higher content of C-A-S-H gel in alkali-activated SGM compared to C-S-H gel in Portland cement [
48,
49,
50,
51,
52,
53]. Compared to alkali-activated GBFS material, alkali-activated SGM has a higher porosity and fewer gel pores. Similarly, compared to alkali-activated steel slag material, alkali-activated SGM exhibits a reduced content of small pores and a decreasing trend in porosity with the increase in GBFS content, indicating that GBFS plays a role in refining the pore structure [
48,
49,
50,
51,
52,
53].
5. Conclusion and Outlook
While steel slag and GBFS can exhibit some degree of synergistic hydration in water, the slow pozzolanic reaction of GBFS is attributed to the weak alkalinity generated by steel slag. To enhance the hydration reaction rate, shorten the setting time, and improve the early strength, the addition of gypsum-based materials (such as natural gypsum and by-product gypsum), cement clinker, or alkali activators (such as sodium silicate, Ca(OH)2, NaOH, Na2CO3, etc.) can effectively optimize the SGM. Alkaline activators and clinker promote the hydration of steel slag and GBFS by increasing the alkalinity of the reaction system. In the case of SGM with gypsum, there is a clear ternary synergistic effect, resulting in the formation of a dense matrix with AFt and C-S-H gel as the main reaction products. Despite the attention given to the hydration and hardening mechanisms, as well as the performance improvement mechanisms of SGM, there are still some unresolved issues:
(1) A common issue with SGM is that as the steel slag content increases, the setting time lengthens and mechanical properties at early age decrease. Given the high utilization rate and cost of GBFS in the market, as well as the low utilization rate and cost of steel slag, further research is needed to maximize the utilization of steel slag, reduce raw material costs, and ensure critical early-age performance.
(2) There is limited research on the fresh properties of SGM. In practical engineering, fresh pastes need to meet certain requirements for setting time, workability, pumpability, and water retention. Therefore, identifying the factors and key indicators affecting fresh properties of SGM, as well as developing effective measures to improve them, requires further investigation.
(3) SGM with gypsum holds promise as solid waste system. However, there is still a lack of systematic research on the long-term mechanical properties, durability, and volume stability. In actual service environments, the secondary hydration of gypsum and the occurrence of "delayed AFt" may risk cracking in hardened pastes. Additionally, the presence of gypsum may lead to poor water resistance of the cementitious materials, necessitating further investigation.
In conclusion, the addition of gypsum-based materials, cement clinker, or alkaline activators effectively addresses the issues of slow reaction rate, long setting time, and poor mechanical properties in SGM. This contributes to the utilization of iron and steel smelting slag and holds practical significance for the green and sustainable development of construction materials.