SinoGreenTech Academic Portal
ZA
Verified CAS / Academic Author2 Decoded Studies

Prof. ZHOU Anning

School of Chemistry and Chemical Engineering, Xi'an University of Science and Technology, Xi'an 710054, China

Co-Affiliations:School of Chemical Engineering, Xi'an University of Science and Technology, Xi'an 710054, China

Research Publications & English Decoded Briefs

Showing 2 publications
Journal of Fuel Chemistry and Technology2026DOI: 10.1016/S1872-5813(25)60612-8

Efficient Leaching and Separation of Iron, Aluminum, and Calcium from Carbon-Rich Components in Coal Gasification Fine Slag Using Organic Acids

Coal gasification fine slag (CGFS) is a solid waste generated in large quantities during coal gasification, containing residual carbon and inorganic ash rich in SiO2, Al2O3, CaO, Fe2O3, and MgO. The carbon-rich components (CGFS-H) of CGFS, typically comprising 20–50% residual carbon, present both environmental challenges and opportunities for resource recovery. This study systematically investigates the selective leaching behavior of Fe3+, Al3+, and Ca2+ from CGFS-H using three organic acid extractants: citric acid, tartaric acid, and tetrasodium iminodisuccinate (IDS-4Na). The results demonstrate distinct selectivity: IDS-4Na exhibits the highest leaching yield and selectivity for Fe3+, achieving a single leaching yield of 41.2% while suppressing Ca2+ and Al3+ leaching to below 4%, with a selectivity ratio of Fe3+ to Al3+ and Ca2+ of 10.73. Tartaric acid effectively leaches both Fe3+ and Al3+, with single yields of 38.7% and 33.5%, respectively, while Ca2+ leaching remains below 5%, yielding a selectivity of Fe3+ and Al3+ relative to Ca2+ of 14.73. Citric acid preferentially leaches Ca2+, achieving a single yield of 71.5%, but also leaches Fe3+ and Al3+ at 35.2% and 39.1%, respectively, resulting in a low selectivity ratio of Ca2+ to Fe3+ and Al3+ of 0.96. Based on these selective affinities, a green stepwise separation method was developed using sequential leaching with IDS-4Na, tartaric acid, and citric acid. Under optimal conditions, cumulative leaching yields of 79.8% for Fe3+, 65.08% for Al3+, and 78.6% for Ca2+ were achieved. XRD, XRF, and SEM analyses elucidate the complexation mechanisms, indicating that the synergistic effects of selective coordination between structurally diverse organic acids and metal ions drive the process. This advancement provides a critical foundation for developing Ca/Fe/Al hydrotalcite materials using CGFS-H as a sustainable feedstock, promoting resource-efficient utilization of coal gasification fine slag.

Journal of Fuel Chemistry and Technology2026DOI: 10.1016/S1872-5813(25)60615-3

Mechanistic Study on the Enhanced Synergistic Effect in Co-pyrolysis of Huangling Coal and Enzymatic Hydrolysis Lignin via Hydrothermal Pretreatment

Co-pyrolysis of oil-rich coal and biomass is a promising route to enhance oil and gas production, yet the underlying synergistic mechanisms remain poorly understood. This study investigates the effect of hydrothermal pretreatment (HTP) on the co-pyrolysis of Huangling coal (H) and enzymatic hydrolysis lignin (E). Raw and pretreated samples were characterized via proximate/ultimate analysis, SEM, ICP-OES, and 13C-NMR. Fixed-bed pyrolysis experiments were conducted to evaluate synergistic performance. Results show that HTP reduces oxygen content, develops pore structure, and increases concentrations of inorganic metal ions (Ca, K, Fe) in the aqueous phase. Structural modifications bring the carbon skeleton of E closer to that of H, with increased bridge carbon ratio and improved thermal stability, aligning pyrolysis temperature ranges. For the H/E blend (8:2) after 24 h HTP, tar yield increases by 80.52% compared to untreated blend, with significant rises in aliphatic compounds and monocyclic aromatic hydrocarbons. Gas yields of H2, CO, and CH4 increase by 5.47%, 10.98%, and 9.27%, respectively, while CO2 and pyrolysis water generation are inhibited (water yield decreases by 93.98%). Semi-coke pore structure becomes more developed. The enhanced synergistic effect is attributed to a multi-fold mechanism of 'component interaction-structural modification-catalytic cracking'. These findings provide theoretical support for developing technologies to improve co-pyrolysis of oil-rich coal and biomass, advancing low-carbon, high-quality utilization.