| Literature DB >> 35547705 |
Shan Li1,2, Xiao Huang2, Faheem Muhammad2, Lin Yu2,3, Ming Xia2, Jian Zhao2, Binquan Jiao1,2,3, YanChyuan Shiau4, Dongwei Li1,2.
Abstract
Solidification/stabilization (S/S) is recognized as an effective technology for solid waste treatment. In S/S, the application of geopolymers synthesized by industrial waste (rich in active silicon and aluminum) to immobilize hazardous waste is a research focus. In this article, a fly ash based geopolymer was used to immobilize lead-zinc slag containing Pb, Ni, Zn and Mn. A fly ash based geopolymer with good mechanical strength was obtained through single factor experiments and the compressive strength of the geopolymer reached 29.72 MPa. The effects of immobilizing lead-zinc slag in the fly ash based geopolymer were discussed by means of compressive strength, leaching test and speciation analysis. The solidification/stabilization mechanism was further investigated using XRD, FTIR and SEM. The mechanical properties of the fly ash based geopolymer were negatively affected by addition of lead-zinc slag, and compressive strength decreased to 8.67 MPa when 60% lead-zinc slag was added. The geopolymer has the ability to reduce toxicity of lead-zinc slag by immobilizing heavy metals (Pb, Ni, Zn and Mn), but the ability was not unlimited. The migration of heavy metals to residual form indicates that heavy metals may either be bonded into the geopolymer matrix via the T-O bond (T = Si, Al) or captured in framework cavities to maintain the charge balance. The NASH (Na2O-Al2O3-SiO2-H2O) gel structure observed by XRD, FTIR and SEM can physically encapsulate the contaminants during geopolymerization. It is finally concluded that heavy metals were immobilized in the fly ash based geopolymer through a combination of chemical bonding and physical encapsulation. This journal is © The Royal Society of Chemistry.Entities:
Year: 2018 PMID: 35547705 PMCID: PMC9086302 DOI: 10.1039/c8ra06634e
Source DB: PubMed Journal: RSC Adv ISSN: 2046-2069 Impact factor: 3.361
The chemical components of LZS and FA (mass, %)a
| Oxide | LZS | FA |
|---|---|---|
| SiO2 | 30.67 | 49.74 |
| Fe2O3 | 29.73 | 10.78 |
| CaO | 12.48 | 3.38 |
| Al2O3 | 7.27 | 27.21 |
| ZnO | 6.39 | N.D. |
| MgO | 3.27 | 0.71 |
| SO3 | 3.06 | 1.41 |
| MnO | 2.97 | N.D. |
| K2O | 0.96 | 1.23 |
| TiO2 | 0.90 | 3.19 |
| Na2O | 0.72 | 1.46 |
| P2O5 | 0.15 | 0.32 |
| PbO | 0.03 | N.D. |
| NiO | 0.02 | N.D. |
N.D. Not detected.
Preparation and compressive strength of geopolymer productsa
| Samples | Activators Na2SiO3 : NaOH | Liquid : solid | Curing temperature (°C) | Compressive strength (MPa) |
|---|---|---|---|---|
| A1 | 1/4 | 0.22 | 60 | 15.93 |
| A2 | 2/3 | 0.22 | 60 | 18.67 |
| A3 | 3/2 | 0.22 | 60 | 12.38 |
| A4 | 4/1 | 0.22 | 60 | 5.74 |
| W1 | 2/3 | 0.21 | 60 | 12.09 |
| W2 | 2/3 | 0.22 | 60 | 18.67 |
| W3 | 2/3 | 0.23 | 60 | 14.00 |
| W4 | 2/3 | 0.24 | 60 | 11.37 |
| T1 | 2/3 | 0.22 | 45 | 4.72 |
| T2 | 2/3 | 0.22 | 60 | 18.67 |
| T3 | 2/3 | 0.22 | 75 | 28.29 |
| T4 | 2/3 | 0.22 | 90 | 29.72 |
FA and alkali activator (mixed Na2SiO3 and NaOH) represent solid, the ratio of FA to alkali activator was 17 : 3.
Tessier sequential extraction scheme
| Scheme | Step 1 | Step 2 | Step 3 | Step 4 | Step 5 |
| Chemical form | Exchangeable | Carbonates | Fe–Mn oxides | Organic matter | Residual |
| Method | Agitate with 8 mL of MgCl2 (1 M, pH = 7.0) for 1 h at room temperature | Agitate with 8 mL of NaOAc (1 M, pH = 5.0) for 5 h at room temperature | Agitate with 20 mL of NH2OH·HCl (0.04 M in 25% (v/v) HOAc) for 6 h at 96 ± 3 °C | Agitate with 3 mL of HNO3 (0.02 M) and 5 mL of H2O2 (30%) for 2 h at 85 ± 2 °C, then add 3 mL of H2O2 (30%) and agitate for 3 h at 85 ± 2 °C. After cooling, add 5 mL of NH4OAc (3.2 M in 20% (v/v) HNO3) and dilute to 20 mL and continuously agitate for 0.5 h | Digest in HF–HClO4 |
Preparation and compressive strength of solidified bodies
| Sample | Proportion of FA and LZS (%) | Activators Na2SiO3 : NaOH | Liquid : solid | Curing temperature (°C) | Compressive strength (MPa) | |
|---|---|---|---|---|---|---|
| FA | LZS | |||||
| FL10 | 90 | 10 | 2/3 | 0.22 | 90 | 28.96 |
| FL20 | 80 | 20 | 26.62 | |||
| FL30 | 70 | 30 | 23.63 | |||
| FL40 | 60 | 40 | 18.15 | |||
| FL50 | 50 | 50 | 12.09 | |||
| FL60 | 40 | 60 | 8.67 | |||
Leaching dataa
| Sample | Leaching Concentration (mg L−1) | |||
|---|---|---|---|---|
| Pb | Ni | Zn | Mn | |
| FL10 | N.D. | 0.184 | 93.17 | 38.85 |
| FL20 | 0.006 | 0.187 | 219.6 | 78.61 |
| FL30 | 0.101 | 0.205 | 320.4 | 120.8 |
| FL40 | 0.219 | 0.210 | 392.7 | 147.9 |
| FL50 | 0.328 | 0.212 | 425.4 | 155.9 |
| FL60 | 0.388 | 0.221 | 493.1 | 179.9 |
| LZS | 1.467 | 0.564 | 1289 | 621.5 |
| Limit in GB 16889-2008 | 0.25 | 0.50 | 100 | — |
N.D. Not detected.
Fig. 1Chemical forms of (a) Pb, (b) Ni, (c) Zn, and (d) Mn in LZS and FL50.
Fig. 2SEM micrographs of (a) T4 and (b) FL50.
Fig. 3XRD patterns of FA, T4, LZS and FL50.
Fig. 4FTIR spectra of FA, T4, LZS and FL50.