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  • New
  • Research Article
  • 10.1016/j.fuel.2026.138377
A novel effective thermal conductivity model of loose remnant coal porous medium for coal spontaneous combustion in goaf
  • Jul 1, 2026
  • Fuel
  • Jiahui Shen + 7 more

  • New
  • Research Article
  • 10.1016/j.fuel.2026.138594
Low-temperature potassium migration mechanism of rice husk thermal treatment high-purity SiO2 extraction: An experimental and molecular dynamics study
  • Jul 1, 2026
  • Fuel
  • Kunqian Zhu + 3 more

  • New
  • Research Article
  • 10.1016/j.fuel.2026.138517
Super-adiabatic temperature in the homogeneous ignition of NH3/O2/N2 mixtures
  • Jul 1, 2026
  • Fuel
  • Han Zhang + 2 more

  • New
  • Addendum
  • 10.1016/j.fuel.2026.139201
Erratum to “Effects of oxygen enrichment in iron ore sintering: combustion characteristics & CO emissions” [Fuel 420 (2026) 138808
  • Jul 1, 2026
  • Fuel
  • Sida Li + 6 more

  • New
  • Research Article
  • Cite Count Icon 1
  • 10.1016/j.fuel.2026.138424
Optimized adsorption-hydration hybrid methane storage: Study on methane hydrate formation controlled by the pores of mesoporous ZIF-8@AC composite materials
  • Jul 1, 2026
  • Fuel
  • Qilin Han + 4 more

  • New
  • Research Article
  • 10.1016/j.fuel.2026.138573
The evaluation of wellbore stability performance of a hydrophobic shale inhibitor using “macroscopic − mesoscopic − microscopic” methods
  • Jul 1, 2026
  • Fuel
  • Xianbin Huang + 4 more

  • New
  • Research Article
  • 10.1016/j.fuel.2026.138582
Boosting photocatalytic hydrogen evolution by engineering a Yb-O-Ti electron bridge in ytterbium metalloporphyrin MOFs nanohybrid
  • Jul 1, 2026
  • Fuel
  • Zhiyong Ou + 5 more

  • New
  • Research Article
  • Cite Count Icon 1
  • 10.1016/j.fuel.2026.138528
Hydrodynamic behavior and design implications in continuous-flow hydrothermal liquefaction systems
  • Jul 1, 2026
  • Fuel
  • Dylan J Cronin + 6 more

  • New
  • Research Article
  • Cite Count Icon 1
  • 10.1016/j.fuel.2026.138476
Optimal operating parameters for NH3/CH4 axial-staging combustion under different fuel/air mixing patterns towards cleaner emission
  • Jul 1, 2026
  • Fuel
  • Zirui Liu + 7 more

  • New
  • Open Access Icon
  • Research Article
  • Cite Count Icon 1
  • 10.1016/j.fuel.2026.138339
Techno-economics analysis of green ammonia system under continuous and dynamic operations in semi-islanded system
  • Jul 1, 2026
  • Fuel
  • Riadh M Habour + 2 more

• A Python model for semi-islanded green ammonia production was developed. • The LCOA ranges from 669.30 to 867.94 €/tNH 3 . • Power generation represents the largest share of total system costs. • The LCOA decreases by up to 15.15 % over the next two decades. • Dynamic operation achieves up to a 6 % reduction compared with continuous operation. The study presents a technical and economic assessment of green ammonia production in several counties in Ireland. The system is based on renewable energy sources, namely photovoltaic and offshore wind. Three locations were chosen based on their renewable potential and the availability of export ports to EU (European Union) markets. A high-temporal-resolution model for green ammonia production has been developed for the first time in Ireland. The WSA (Wind Solar Ammonia) model was developed specifically for this research. It uses MILP (Mixed Integer Linear Programming) and optimisation techniques to simulate scenarios at the lowest possible cost. The Python-based model incorporates all relevant energy subsystems and use functions from specialised libraries. The WSA model includes large-scale hydrogen production with proton exchange membrane electrolysers, air separation to produce nitrogen, Haber-Bosch ammonia synthesis, desalination unit. Storages buffers were implemented for green hydrogen, green ammonia, purified sea water, and nitrogen. Both continuous and dynamic operation were simulated, continuous operation reflects industrial reliability, stable equipment performance, and maximised lifetime, while dynamic operation captures renewable intermittency, curtailment reduction, and system flexibility. Cork is identified as the least-cost location, with the dynamic operation system achieving the lowest LCOA (Levelised Cost Of Ammonia) at 791.07 €/t in 2030 and 731.45 €/t in 2040, outperforming the continuous operation system, which records 834.27 €/t in 2030 and 741.62 €/t in 2040. The system achieve a carbon saving up to 94.63 % compared to the ammonia fossil fuel-based comparator.