Fuel· 2026Q1
Novel bimetallic ZIF (Cu-Zn-ZIF-8) for enhanced and stable carbon capture from industrial moisture-laden flue gas through systematic and hierarchical material and process optimization
- 0citations
- Q1SCImago
- 2026year
Short summary
Cu-Zn-ZIF-8 captures 5.6 mmol/g CO2 from humid flue gas under optimized conditions (40°C, 5g adsorbent, 150 ml/min flow, 220 min carbonation), retaining 80.4% capacity after 10 cycles.
AI-generated from the title and abstract; the full text is not read.
Key points
- Cu-Zn-ZIF-8 achieved a CO2 uptake of 5.6 mmol/g from simulated flue gas containing 10% H2O.
- Optimal capture conditions were determined as 40°C, 5g adsorbent, 150 ml/min flow rate, and 220 min carbonation time.
- The bimetallic ZIF retained 80.4% of its adsorption capacity after 10 cycles, demonstrating good stability under humid conditions.
- Cu-Zn-ZIF-8 possesses a BET surface area of 974 m²/g and a pore volume of 0.47 cm³/g.
AI-generated from the title and abstract; the full text is not read.
Abstract
Post-combustion carbon capture (PCCC) in the presence of moisture faces challenges due to competition between CO 2 and H 2 O for adsorption sites, thereby impacting both efficiency and stability. Ten adsorbents, including metal–organic frameworks and bimetallic ZIFs, were investigated using simulated flue gas conditions: 12 vol% CO 2 , 10 vol% H 2 O, 8 vol% O 2 , and the balance N 2 . Cu-Zn-ZIF-8 demonstrated good performance among the evaluated adsorbents and was selected for further work. The adsorption process was optimized using a Central Composite Design (RSM-CCD) and an Artificial Neural Network (ANN) model to confirm the results. An increase in CO 2 uptake to 5.6 mmol/g was observed under optimal conditions, viz., 40 °C, 5 g of Cu-Zn-ZIF-8, flow rate of 150 ml/min, and carbonation time of 220 min. Integration of Cu 2+ into the ZIF-8 framework was evidenced by Cu 2p XPS and corroborated by XRD, which showed preservation of the parent ZIF-8 framework. The Cu-Zn-ZIF-8 showed a BET surface area of 974 m 2 /g and a pore volume of 0.47 cm 3 /g. The Elovich model provided an accurate fit to the adsorption kinetics, and the Langmuir isotherm accurately fit the experimental data. A preliminary techno-economic analysis determined that the adsorbent lifetime is the key factor affecting the overall CO 2 capture cost. Even under humid conditions, the adsorbent retained 80.4% of its adsorption capacity after 10 cycles, confirming its good stability.
The authors' abstract, as published at the source. Fuel, 2026 · DOI ↗
Continue with a free account
Ask the paper: 3 free questions a day about this paper; save it, get its citation, new summaries every day for your field. Takeaways are Premium.
Continue free on the webSign in with Google or Apple; no card needed. You come back to this paper.
On your phone:
Field: Mechanical Engineering
Mechanical EngineeringEngineering