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Item type:Publication, Investigating the synergy of fast co-pyrolysis of spent coffee ground and disposed urban facemask: analysis of kinetics and product compositions(2025-12-01) ;Idris, Imad A. ;Nisamaneenate, Jurarat ;Atong, Duangduen; Sricharoenchaikul, ViboonThis study investigates the thermo-kinetic behavior and product distribution during the co-pyrolysis of spent coffee grounds (SCG) and facemasks (FM). TGA was employed to evaluate the kinetics and thermodynamics of the pyrolysis process by segmenting the thermal decomposition into stage I (200 – 360 °C) and stage II (360 – 550 °C), while Py-GC/MS was used to analyse the product composition. SCG and FM blends with varying ratios by wt.% (SCG:FM = 100:0, 75:25, 50:50, 25:100, and 0:100) were subjected to pyrolysis at four heating rates (5, 10, and 30 °C/min). The decomposition curves were deconvoluted using Fraser-Suzuki deconvolution method into four peaks related to biomass pseudo-components and FM degradation. The deconvoluted curves showed potential synergistic interaction at the lignin and FM decomposition zone (460 – 500 °C). The kinetic analyses were carried out using three model-free methods to investigate the activation energy (Ea) and thermodynamics of co-pyrolysis. The lowest Ea value was obtained at SCG25 %FM%75 % (305.1 – 239 kJ/mol), mostly pronounced in stage II. Py-GC/MS analysis of the co-pyrolysis products demonstrates that the decomposition of polypropylene polymer of the FM promoted the formation of aliphatic hydrocarbons and reduces the overall acidity. This effect was further amplified at higher pyrolysis temperatures (450 – 650 °C). The blending ratio also plays a significant role, with a higher polymer content (SCG25 %FM75 %) leading to a more aliphatic products and a significant decline in carboxylic acids and anhydro-sugars. Moreover, co-pyrolysis reduced the N containing compounds significantly. Finally, policy implications and recommendations for co-pyrolysis adoption were incorporated. Overall, this study highlights the potential of utilizing waste material like SCG and FM for the sustainable production of valuable chemicals and fuels.3 - Some of the metrics are blocked by yourconsent settings
Item type:Publication, Physical and Functional Properties of Spent Coffee Ground after Various Drying Techniques(2025-01-01) ;Maiyah, Nur ;Auenchitr, Yatima; ;Sirijariyawat, ArpassornSpent coffee ground (SCG) consists of impact compositions and functional ingredients that could be applied to food products. Drying techniques and conditions had an impact on the qualities of SCG. The aim of this research was to investigate the chemical compositions of roasted coffee ground (CG) and SCG from Arabica (A) and Robusta (R) coffee, as well as the physical and functional properties of SCG before and after different drying using hot air tray dryer and freeze dryer. It was found that SCG had moisture and carbohydrate content of 64.79–65.87% wb and 16.55 18.57%. Arabica spent coffee ground (ASCG) had more lipid and less protein, caffeine and phenolic content than that of Robusta spent coffee ground (RSCG). The dried SCG had moisture content lower than 5% for all drying conditions. Moreover, the dried SCG had Aw, solubility, and rehydration in a range of 0.25-0.55, 6.02-6.92%, and 140.67-180.37%, respectively. Freeze-dried SCG retained more functional ingredients than tray-dried SCG across all drying conditions.7 - Some of the metrics are blocked by yourconsent settings
Item type:Publication, Ethyl acetate as extracting solvent and reactant for producing biodiesel from spent coffee grounds: A catalyst- and glycerol-free process(2022-07-01) ;Supang, Wirasinee ;Ngamprasertsith, Somkiat; Sawangkeaw, RuengwitOil was extracted from spent coffee grounds (SCGs) using ethyl acetate at atmospheric pressure; then, the ethyl acetate–SCG oil mixture was reacted under supercritical conditions, which involve a catalyst-free process. Moreover, ethyl acetate reacted with glycerol to form triacetin, which dissolves in biodiesel and acts as a fuel additive. Using this approach, the solvent removal step and glycerol byproducts are eliminated. The highest fatty acid ethyl ester contents of 91.80 wt% ± 1.62 wt% and 86.44 wt% ± 2.12 wt%. were obtained under optimal conditions in batch and continuous reactors, respectively. Based on gas chromatography–mass spectrometric analysis, no trace of glycerol was detected and triacetin was yielded at 4.22 wt%. This novel process simultaneously minimizes the number of chemicals used and the amount of waste generated because it employs only dried SCGs and ethyl acetate as the feedstock.3
