Industrial-Scale Thermophilic Anaerobic Digestion of Untreated Cafeteria Waste: Techno-Economic Assessment of Renewable Energy and Digestate Valorization

Thermophilic anaerobic digestion (TAD) of solid organic wastes for biogas production offers dual human-health and environmental benefits: source-separated waste management with reduced pathogen burden and renewable energy generation with reduced greenhouse-gas emissions. This study investigated a “Techno-Economic Assessment (TEA)” of an industrial-scale TAD process integrated with combined heat and power (CHP) generation and alternative digestate-management strategies. Two processing capacities, 7000 tons/year (Case I) and 2000 tons/year (Case II), were evaluated under four digestate-management scenarios using economic assumptions. For Case I, the total capital investment (TCI), including working capital equivalent to 5% of fixed capital investment, was estimated at $4.055 million, while the annual operation and maintenance (O&M) cost was estimated at $0.434 million. Scenario 1, involving solid–liquid separation with recovery of separated compost and liquid digestate, generated an annual revenue of $1.070 million, a 20-year net present value (NPV) of $0.869 million, a discounted payback period of 12.3 years, and an internal rate of return (IRR) of 13.2%. Scenario 2, based on direct utilization of whole digestate, produced the highest modeled economic return, with an NPV of $5.998 million and an IRR of 30.1%; however, its feasibility depends strongly on securing a reliable whole digestate offtake market. In contrast, Scenarios 3 and 4 resulted in negative NPVs under the base-case assumptions. A normalized one-at-a-time sensitivity analysis identified process-cycle duration and effective throughput, liquid digestate netback, tipping fee, CHP energy value, methane yield, capital cost, processing capacity, and discount rate as the principal economic drivers. Zero-revenue digestate cases produced negative NPVs for Scenarios 1 and 2, with estimated break-even plant-gate netbacks of $0.134/gal for liquid digestate and $0.121/gal for whole digestate. Overall, industrial TAD can be economically feasible, but commercial viability depends on feedstock supply, reactor productivity, internal energy demand, digestate offtake, heat utilization, and site-specific waste-management revenue.

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Publication Details

Journal
Sustainability
Published
2026-10-05
DOI
https://doi.org/10.3390/su181910158
Primary Topic
Anaerobic Digestion and Biogas Production
Type
article
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article

Industrial-Scale Thermophilic Anaerobic Digestion of Untreated Cafeteria Waste: Techno-Economic Assessment of Renewable Energy and Digestate Valorization

Dipayan Samanta, Sudhir Kumar, Anjali Thapliyal, Aditi David et al.
Sustainability
Anaerobic Digestion and Biogas Production
article

Industrial-Scale Thermophilic Anaerobic Digestion of Untreated Cafeteria Waste: Techno-Economic Assessment of Renewable Energy and Digestate Valorization

Dipayan Samanta, Sudhir Kumar, Anjali Thapliyal, Aditi David, Tanvi Govil, Rajesh Kumar Sani, Prasoon K. Diwakar, Agastya Sani, Samantha Harris
article en

Abstract

Thermophilic anaerobic digestion (TAD) of solid organic wastes for biogas production offers dual human-health and environmental benefits: source-separated waste management with reduced pathogen burden and renewable energy generation with reduced greenhouse-gas emissions. This study investigated a “Techno-Economic Assessment (TEA)” of an industrial-scale TAD process integrated with combined heat and power (CHP) generation and alternative digestate-management strategies. Two processing capacities, 7000 tons/year (Case I) and 2000 tons/year (Case II), were evaluated under four digestate-management scenarios using economic assumptions. For Case I, the total capital investment (TCI), including working capital equivalent to 5% of fixed capital investment, was estimated at $4.055 million, while the annual operation and maintenance (O&M) cost was estimated at $0.434 million. Scenario 1, involving solid–liquid separation with recovery of separated compost and liquid digestate, generated an annual revenue of $1.070 million, a 20-year net present value (NPV) of $0.869 million, a discounted payback period of 12.3 years, and an internal rate of return (IRR) of 13.2%. Scenario 2, based on direct utilization of whole digestate, produced the highest modeled economic return, with an NPV of $5.998 million and an IRR of 30.1%; however, its feasibility depends strongly on securing a reliable whole digestate offtake market. In contrast, Scenarios 3 and 4 resulted in negative NPVs under the base-case assumptions. A normalized one-at-a-time sensitivity analysis identified process-cycle duration and effective throughput, liquid digestate netback, tipping fee, CHP energy value, methane yield, capital cost, processing capacity, and discount rate as the principal economic drivers. Zero-revenue digestate cases produced negative NPVs for Scenarios 1 and 2, with estimated break-even plant-gate netbacks of $0.134/gal for liquid digestate and $0.121/gal for whole digestate. Overall, industrial TAD can be economically feasible, but commercial viability depends on feedstock supply, reactor productivity, internal energy demand, digestate offtake, heat utilization, and site-specific waste-management revenue.

SustainabilityVol. 18(19)
Jaypee University of Information Technology (IN), South Dakota School of Mines and Technology (US), Colorado College (US), University of Colorado Colorado Springs (US)
Openalex Percentile: Top 15%
Anaerobic Digestion and Biogas Production
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