TY - JOUR
T1 - Steam gasification of plastic and woody biomass for hydrogen-rich syngas production with CO2 reduction, emission and energy analysis
AU - Bakhtiar, Muhammad
AU - Shahbaz, Muhammad
AU - Ayub, Hafiz Muhammad Uzair
AU - Ali, Usman
N1 - Publisher Copyright:
© 2025 Elsevier Ltd
PY - 2025/10/15
Y1 - 2025/10/15
N2 - This study investigates the steam gasification of high-density polyethylene (HDPE), wood waste, and their blend into H2-rich syngas using a simulation model under varying temperatures (650°C-950 °C) and steam/feed (S/F) ratios (0.5–2). Results show temperature enhances H2 and CO and reduction of CO2 and CH4. The S/F ratio exhibits varying effects: H2 decreases for plastic (69–63.6 mol%) but increases for wood (53.2–63.2 mol%), remaining stable for the 50:50 blend. Lower heating value and higher heating value of syngas at optimal conditions were 10.87/12.83 MJ/m3 for plastic, 9.26/10.35 MJ/m3 for wood, and 10.13/11.46 MJ/m3 for the blend. The study also investigate CO2 capture with CaO which enhances syngas composition. For plastic, H2 increases by 8 % (72.7 mol%) and CO2 decreases by 5 % (2.4 mol%); for wood, H2 rises by 17 % (78.4 mol%) and CO2 reductions of 9 % (10.9 %); and for blend, H2 increases to 75.8 % while CO2 drops to 6.5 %. CO2 emissions are highest for plastic (5.545 kg/h), lowest for wood (1.350 kg/h), and intermediate for blend (3.464 kg/h), highlighting the environmental benefits of co-gasification. The utility analysis shows energy-saving potentials: 37.6 % (plastic), 14.9 % (wood), and 31.8 % for the blend, with process heat integration identified as a key strategy for optimizing energy use.
AB - This study investigates the steam gasification of high-density polyethylene (HDPE), wood waste, and their blend into H2-rich syngas using a simulation model under varying temperatures (650°C-950 °C) and steam/feed (S/F) ratios (0.5–2). Results show temperature enhances H2 and CO and reduction of CO2 and CH4. The S/F ratio exhibits varying effects: H2 decreases for plastic (69–63.6 mol%) but increases for wood (53.2–63.2 mol%), remaining stable for the 50:50 blend. Lower heating value and higher heating value of syngas at optimal conditions were 10.87/12.83 MJ/m3 for plastic, 9.26/10.35 MJ/m3 for wood, and 10.13/11.46 MJ/m3 for the blend. The study also investigate CO2 capture with CaO which enhances syngas composition. For plastic, H2 increases by 8 % (72.7 mol%) and CO2 decreases by 5 % (2.4 mol%); for wood, H2 rises by 17 % (78.4 mol%) and CO2 reductions of 9 % (10.9 %); and for blend, H2 increases to 75.8 % while CO2 drops to 6.5 %. CO2 emissions are highest for plastic (5.545 kg/h), lowest for wood (1.350 kg/h), and intermediate for blend (3.464 kg/h), highlighting the environmental benefits of co-gasification. The utility analysis shows energy-saving potentials: 37.6 % (plastic), 14.9 % (wood), and 31.8 % for the blend, with process heat integration identified as a key strategy for optimizing energy use.
UR - https://www.scopus.com/pages/publications/105011486113
U2 - 10.1016/j.energy.2025.137718
DO - 10.1016/j.energy.2025.137718
M3 - Article
AN - SCOPUS:105011486113
SN - 0360-5442
VL - 334
JO - Energy
JF - Energy
M1 - 137718
ER -