| Literature DB >> 36013650 |
Mohammad Almadani1, Rafiza Abd Razak2,3, Mohd Mustafa Al Bakri Abdullah3,4, Rosnita Mohamed3.
Abstract
The depletion of aggregate-related natural resources is the primary concern of all researchers globally. Recent studies emphasize the significance of recycling and reusing various types of natural or by-product material waste from industry as a result of the building industry's rising demand for aggregate as the primary component in concrete production. It has been demonstrated that the geopolymer system has exceptional features, such as high strength, superior durability, and greater resistance to fire exposure, making it a viable alternative to ordinary Portland Cement (OPC) concrete. This study will examine the present method utilized to generate artificial aggregate-based geopolymers, including their physical and mechanical properties, as well as their characterization. The production process of geopolymer derived from synthetic aggregates will be highlighted. In conjunction with the bonding of aggregates and the cement matrix, the interfacial transition zone (ITZ) is highlighted in this work as an additional important property to be researched in the future. It will be discussed how to improve the properties of geopolymers based on artificial aggregates. It has been demonstrated that cold bonding provides superior qualities for artificial aggregate while conserving energy during production. The creation of ITZ has a significant impact on the bonding strength between artificial aggregates and the cement matrix. Additionally, improvement strategies demonstrate viable methods for enhancing the quality of manufactured aggregates. In addition, other recommendations are discussed in this study for future work.Entities:
Keywords: artificial aggregate; autoclaving; cold bonding; geopolymer; sintering
Year: 2022 PMID: 36013650 PMCID: PMC9410120 DOI: 10.3390/ma15165516
Source DB: PubMed Journal: Materials (Basel) ISSN: 1996-1944 Impact factor: 3.748
Past research on Geopolymer-based Artificial Aggregates with different mixing parameter ratios and processing methods.
| Researchers | Precursors | Addition of Additives | Mixing Parameter Ratio | Processing | |
|---|---|---|---|---|---|
| Raw Materials | Alkali Activator | ||||
| Tian et al. [ | Red mud, coal fly ash | Na2SiO3 | - | Solid-to-liquid ratio (0.34–0.39) | Shaping with disc pelletizer. Curing at temperature of 20 °C with relative humidity of 50% |
| Saleem et al. [ | Class F fly ash, silica fume | NaOH, | NaHCO3 | Alkali activator percentage (NaOH-Na2SiO3) 20–80, 30–70, 40–60 | Hand shaping and then microwave curing |
| UI Rehman et al. [ | Coal fly ash and slag | NaOH, | - | Different fly ash contents (80–90%), different slag contents (10–20%) | Cold-bond pelletization was applied. Dry curing with elevated temperature of 70 °C was used for curing aggregates |
| Parvathy et al. [ | Class C fly ash, Class F fly ash | NaOH, | - | The effect of different raw materials used on the performance of the fine aggregates (Class C fly ash and Class F fly ash) | Heating at 100 °C for 1 h and kept at ambient temperature for one day |
| Aslam et al. [ | Class F fly ash and silica fume | NaOH, | NaHCO3 | Alkali activator ratio (NaOH:Na2SiO3) (0.42,0.53) | Hand shaping followed by microwave radiation curing. |
| Huynh et al. [ | Class F fly ash and slag | NaOH, | - | Different alkali equivalent, AE (5–9%) and alkali modulus, Ms (0.6–1.0) | Shaping by crushing the hardened paste of alkali-activated fly ash-slag divided into coarse and fine sizes by sieving |
| Wang et al. [ | OPC, Class F fly ash, quarry tailings | NaOH, | - | Effect of curing temperature (25–150 °C) and curing pressure (0.50–1.25 MPa) | Disk pelletization followed by autoclaving |
NaHCO3 = Sodium carbonate, NaOH = Sodium hydroxide, Na2SiO3 = Sodium silicate.
Figure 1Illustration of Geopolymer Synthesis [47].
Chemical composition of aluminosilicate precursors that have been used by previous researchers [53,54,55,56,57,58].
| Chemical Composition | Class F FA | Kaolin | Metakaolin | GGBS | Red Mud | Rice Husk Ash |
|---|---|---|---|---|---|---|
| SiO2 | 54.40 | 48.10 | 55.57 | 32.00 | 22.82 | 87.40 |
| Al2O3 | 32.10 | 36.90 | 41.55 | 14.10 | 15.06 | 3.00 |
| CaO | 1.10 | 0.20 | - | 44.22 | 12.24 | 1.40 |
| K2O | 0.20 | 1.90 | 0.43 | 0.31 | 1.19 | 0.49 |
| MgO | 0.80 | 0.17 | 0.05 | 5.32 | 0.27 | - |
| Fe2O3 | 7.50 | 0.26 | 0.56 | 0.43 | 17.34 | 1.49 |
| TiO2 | 2.10 | 0.25 | 0.26 | 0.62 | 3.43 | - |
Notes: FA = fly ash, GGBS = ground granulated blast furnace slag.
Findings on the utilization of cold bonding, sintering, and autoclaving as curing methods for geopolymer-based artificial aggregates.
| Method | Raw Materials | Liquid | Significant Conclusion | References |
|---|---|---|---|---|
| Cold bonding | FA with the addition of GGBS and RHA | NaOH, Na2SiO3 | The addition of GGBS and RHA in both binary and ternary blends improved the crushing strength of the aggregates produced | Bui et al. [ |
| High calcium FA with different percentages of the addition of OPC and Ca(OH)2 | Water | An increase in OPC and calcium hydroxide enhanced the properties of fly ash aggregates including the density and strength performance. | Narattha et al. [ | |
| FA | NaOH, Na2SiO3 | The artificial aggregates were proven to have acceptable properties compared with the commercialized expanded clay aggregates with less energy consumption during manufacturing | Risdanareni et al. [ | |
| Sintering | POFA | NaOH, Na2SiO3 | The application of S-POFA LWC with optimized sintered S-POFA aggregate demonstrated the feasibility of this material, as evidenced by the concrete’s physical and mechanical performance. | Kwek et al. [ |
| FA | Na2SiO3 | Sintered FA aggregates showed a denser structure with smaller non-interconnected pores proven to have a low bulk density due to weight loss | Terzic et al. [ | |
| High calcium bottom ash (denoted as WP), Low calcium bottom ash (denoted as NV) | NaOH | Proven to outperform commercial aggregates due to the spherical shape, which enhances the workability of concrete and the sorption properties. | Balapour et al. [ | |
| Autoclaving | FA and quarry tailings | NaOH, Na2SiO3 | Based on reported properties, artificial aggregates lead to better use of the space and meet the environmental and economic needs of the commercial sector and are also capable of shortening the curing period through autoclave methods. | Wang et al. [ |
| FA and quarry tailings | Water | Artificial aggregates have the potential to partially replace CS in the production of concrete, hence reducing the consumption of non-renewable resources. | Wang et al. [ |
Notes: FA = fly ash, RHA = rice husk ash, POFA = palm oil fly ash and GGBS = ground granulated blast furnace slag.
Reported research on the physical and mechanical properties of artificial aggregates with the inclusion of geopolymers.
| References | Artificial | Physical Properties | Mechanical Properties | ||||
|---|---|---|---|---|---|---|---|
| Specific Gravity | Density, kg/m3 | Water Absorption, % | Aggregates: | Aggregates: | Crushing Strength, MPa | ||
| Tian et al. [ | FA-RM aggregates | NR | 1007–1132 | 9.80–12.10 | NR | NR | 1.46–6.18 |
| Saleem et al. [ | FA-SF aggregates | 1.700 | 738 | 18.98 | 10.24 | NR | 2.03–12.00 |
| UI Rehman et al. [ | FA-GGBS aggregates | NR | 764–878 | 18.73–28.30 | 25.00–39.00 | NR | NR |
| Aslam et al. [ | FA-SF aggregates | 1.800 | 710 | 17.95 | 10.03 | NR | 3.34–4.54 |
| Gomathi et al. [ | FA-BT, FA-MK, FA-GGBS aggregates | 1.68–1.89 | 848–983 | 13.01–21.26 | 31.96–50.47 | NR | 14.51–22.81 |
| Sharath et al. [ | FA-GGBS, FA-BL, FA-BT aggregates | 2.000–2.200 | NR | 13.40–24.30 | 20.40–50.20 | 18.5–49.40 | 0.4–4.3 |
| Risdanareni et al. [ | FA aggregates | NR | 1450–1500 | 22.00–23.00 | NR | NR | NR |
| Kasi et al. [ | FA aggregates | 2.058 | NR | 7.07 | 28.31 | 23.96 | NR |
| Parvathy et al. [ | CFA, FFA aggregates | 2.40–2.45 | NR | 5.51–6.05 | NR | NR | NR |
Notes: BT = Bentonite, BL = lime, CFA = Class C fly ash, FFA = Class F fly ash, FA = fly ash, GGBS = ground granulated blast furnace slag, MK = metakaolin, NR = not reported RM = red mud and SF = silica fume.
Figure 2SEM micrograph of POFA aggregates (a) before sintering and (b) after sintering with magnification ×1000.
Figure 3SEM images of S-POFA LWC ITZ (×6000) at 90 d [13].
Past research on the improvement techniques on artificial lightweight aggregates.
| Techniques | Researcher | Lightweight | Treatment Material | Inclusion |
|---|---|---|---|---|
| Two-step pelletization | Yang et al. (2021) [ | Soil | Fly ash | - |
| Two-step pelletization | Drissi et al. (2020) [ | Cement | Calcium hydroxide, waste concrete powder, and paraffin powder | - |
| Two-step pelletization | Tajra et al. (2018) [ | Fly ash | Cement | - |
| Two-step pelletization | Colangelo et al. (2015) [ | Municipal solid waste incinerator fly ash | Cement, hydrated lime, coal fly ash | - |
| Soaking in alkali solution | Kalinowska-Wichrowska et al. (2022) [ | Certyd | Sodium Hydroxide (NaOH) | Yes |
| Soaking in alkali solution | Venkata Suresh and Karthikeyan (2016) [ | Class C fly ash | Sodium Hydroxide (NaOH) | Yes |
| Soaking in alkali solution | Gesoǧlu et al. (2007) [ | Fly ash | Water glass (Na2O + Si2O) | Yes |
| Coating | Dixit and Pang (2022) [ | Expanded clay aggregate | Cement with silica fume, cement with fly ash | - |
| Coating | Ye et al. (2022) [ | Fly ash | Polypropylene (PP), linear low-density polyethylene | Yes |
| Coating | Pongsopha et al. (2021) [ | Porous aggregate | Phase change material and silica fume | - |
| Coating | Tajra et al. (2019) [ | Expanded perlite | Cement, fly ash, expanded perlite powder | - |
| Vacuum impregnation | Haider et al. (2022) [ | Volcanic stone | Paraffin, epoxy resin, silica fume | - |
| Vacuum impregnation | Hasanabadi et al. (2021) [ | Expanded perlite | Paraffin | - |
| Vacuum impregnation | Uthaichotirat et al. (2020) [ | Recycled waste | Paraffin | - |
Figure 4Two-step pelletization.
Figure 5Soaking in alkali solution.
Figure 6Coating.
Figure 7Vacuum impregnation.