Feasibility evaluation of municipal solid waste (MSW), pecan shell and cotton gin trash co-gasification for decentralized hydrogen enriched syngas production

With growing interest in energy resiliency and effective waste management, biomass and municipal solid waste (MSW) have emerged as valuable feedstocks for thermochemical conversion processes that produce energy-dense fuels, enhancing national energy security. Gasification offers a flexible and efficient pathway for converting waste materials and solid residues into syngas for power generation, fuel synthesis, and hydrogen recovery. However, its performance depends on feedstock properties, gasifying agents, and operating conditions. This study investigates the co-gasification of MSW, pecan shells (PS), and cotton gin trash (CGT) in a fluidized bed gasifier using Aspen Plus simulation. A co-gasification blend of 60% MSW, 30% PS, and 10% CGT was selected based on regional availability and fuel characteristics. The model explores ranges of operating temperatures, supply of oxygen, steam, carbon dioxide, and their blends as gasifying agents at 1 bar pressure. The novelty of this work lies in evaluating a region-specific ternary MSW-biomass blend over a multi-agent operating window. The optimal condition was selected through a balanced assessment of hydrogen production, syngas lower heating value (LHV), carbon conversion efficiency (CCE), and cold gas efficiency (CGE). The optimal combination of equivalence ratio (ER) of 0.18, steam-to-biomass ratio of 0.3, and carbon dioxide-to-biomass ratio of 0.2 balanced hydrogen production and syngas calorific value. Under this condition, the syngas LHV was 7.8 MJ/Nm 3 for the co-gasification case. The co-gasification blend stayed at an intermediate position compared to individual feedstocks, achieving a CCE of 91.21% and a CGE of 62.06%. The model predictions aligned with published co-gasification studies, demonstrating the feasibility of MSW-biomass co-gasification for clean energy production and providing insight for optimizing gasifying-agent composition and fluidized-bed gasifier design for complex, heterogeneous feedstocks.

Authors

Institutions

Publication Details

Journal
Next Energy
Published
2026-05-29
DOI
https://doi.org/10.1016/j.nxener.2026.100671
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
Field-Weighted Citation Impact
0.00

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Feasibility evaluation of municipal solid waste (MSW), pecan shell and cotton gin trash co-gasification for decentralized hydrogen enriched syngas production

Safwan Shafquat, Anika Tasnim, Afsana Mustari Itul, Ahsan Choudhuri et al.
Next Energy
Thermochemical Biomass Conversion Processes
article

Feasibility evaluation of municipal solid waste (MSW), pecan shell and cotton gin trash co-gasification for decentralized hydrogen enriched syngas production

Safwan Shafquat, Anika Tasnim, Afsana Mustari Itul, Ahsan Choudhuri, Arfan Nabil, Sumit Chanda, Nawshad Arslan Islam, Md Ismail Hassan Udoy
article en

Abstract

With growing interest in energy resiliency and effective waste management, biomass and municipal solid waste (MSW) have emerged as valuable feedstocks for thermochemical conversion processes that produce energy-dense fuels, enhancing national energy security. Gasification offers a flexible and efficient pathway for converting waste materials and solid residues into syngas for power generation, fuel synthesis, and hydrogen recovery. However, its performance depends on feedstock properties, gasifying agents, and operating conditions. This study investigates the co-gasification of MSW, pecan shells (PS), and cotton gin trash (CGT) in a fluidized bed gasifier using Aspen Plus simulation. A co-gasification blend of 60% MSW, 30% PS, and 10% CGT was selected based on regional availability and fuel characteristics. The model explores ranges of operating temperatures, supply of oxygen, steam, carbon dioxide, and their blends as gasifying agents at 1 bar pressure. The novelty of this work lies in evaluating a region-specific ternary MSW-biomass blend over a multi-agent operating window. The optimal condition was selected through a balanced assessment of hydrogen production, syngas lower heating value (LHV), carbon conversion efficiency (CCE), and cold gas efficiency (CGE). The optimal combination of equivalence ratio (ER) of 0.18, steam-to-biomass ratio of 0.3, and carbon dioxide-to-biomass ratio of 0.2 balanced hydrogen production and syngas calorific value. Under this condition, the syngas LHV was 7.8 MJ/Nm 3 for the co-gasification case. The co-gasification blend stayed at an intermediate position compared to individual feedstocks, achieving a CCE of 91.21% and a CGE of 62.06%. The model predictions aligned with published co-gasification studies, demonstrating the feasibility of MSW-biomass co-gasification for clean energy production and providing insight for optimizing gasifying-agent composition and fluidized-bed gasifier design for complex, heterogeneous feedstocks.

Next EnergyVol. 12
The University of Texas at El Paso (US)
U.S. Department of Energy
Industry, innovation and infrastructure
Openalex Percentile: Top 9%
Thermochemical Biomass Conversion Processes
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.