Journal of Inorganic Materials ›› 2026, Vol. 41 ›› Issue (8): 1087-1094.DOI: 10.15541/jim20250472
• RESEARCH ARTICLE • Previous Articles Next Articles
HUANG Qihan1,2(
), LIU Chang1,2, HAO Jiayu1,2,3,4, LI Zhihua1,2,3,4, XU Wenhua1,2,3,4(
)
Received:2025-11-26
Revised:2026-02-15
Published:2026-08-20
Online:2026-03-18
Contact:
XU Wenhua, associate professor. E-mail: xuwenhua@zzu.edu.cnAbout author:HUANG Qihan (2001-), female, Master candidate. E-mail: 15937751770@163.com
Supported by:CLC Number:
HUANG Qihan, LIU Chang, HAO Jiayu, LI Zhihua, XU Wenhua. Integrated Roasting-Alkali Leaching-Adsorption Strategy for Highly Efficient Lithium Extraction from Coal Fly Ash[J]. Journal of Inorganic Materials, 2026, 41(8): 1087-1094.
| Component | SiO2 | Al2O3 | SO3 | K2O | CaO | Fe2O3 | MgO | Na2O | Li2O |
|---|---|---|---|---|---|---|---|---|---|
| Content/% (in mass) | 64.22 | 19.62 | 1.594 | 3.42 | 4.37 | 3.77 | 2.36 | 0.518 | 0.128 |
Table 1 Chemical composition of CFA
| Component | SiO2 | Al2O3 | SO3 | K2O | CaO | Fe2O3 | MgO | Na2O | Li2O |
|---|---|---|---|---|---|---|---|---|---|
| Content/% (in mass) | 64.22 | 19.62 | 1.594 | 3.42 | 4.37 | 3.77 | 2.36 | 0.518 | 0.128 |
Fig. 2 Phase transition behavior during the calcination of CFA and Na2SO4/CFA (a) Schematic diagram of the phase transformation mechanism; (b, c) TG/DTG curves of (b) CFA and (c) Na2SO4/CFA; (d, e) XRD patterns of calcine from (d) CFA and (e) Na2SO4/CFA; (f, g) EPMA elemental mappings of calcine from (f) CFA and (g) Na2SO4/CFA
Fig. 3 (a, c, d) R1 from the Na2SO4/CFA mixture under different calcination conditions and (b, e, f) XRD patterns of the corresponding calcine Colorful figures are available on website
Fig. 4 Leaching behavior of Li, Al and Si under different alkaline conditions (a-c) Leaching ratios of (a) Li, (b) Al and (c) Si under different NaOH concentrations; (d, e) Leaching behavior of Li under different (d) leaching temperatures and (e) liquid-to-solid ratios; (f) XRD pattern of optimally-leached residue
Fig. 5 Selective adsorption behavior of Li4Ti5O12 for lithium ions in alkaline leachate (a) Lithium concentration and recovery during adsorption process; (b) XRD patterns
| Cycle number | q/(mg·g-1) | R3/% | Ti4+ dissolution rate/% |
|---|---|---|---|
| 1 | 19.0 | 99.70 | 0.040 |
| 2 | 19.2 | 99.48 | 0.039 |
| 3 | 18.3 | 98.60 | 0.042 |
| 4 | 18.0 | 98.05 | 0.048 |
| 5 | 17.7 | 97.75 | 0.053 |
Table 2 Cycling stability of adsorbent
| Cycle number | q/(mg·g-1) | R3/% | Ti4+ dissolution rate/% |
|---|---|---|---|
| 1 | 19.0 | 99.70 | 0.040 |
| 2 | 19.2 | 99.48 | 0.039 |
| 3 | 18.3 | 98.60 | 0.042 |
| 4 | 18.0 | 98.05 | 0.048 |
| 5 | 17.7 | 97.75 | 0.053 |
Fig. 6 Phosphate precipitation to prepare lithium phosphate (a) Evolution of ion concentrations during enrichment; (b) Li+ concentration, Li+ precipitation ratio, and (c) Na+ concentration during Li3PO4 precipitation; (d) Compositions during water washing; (e) XRD pattern and (f) SEM image of obtained Li3PO4
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