Direct biogas methanation via renewable-based Power-to-Gas: Techno-economic assessment based on real industrial data

• Solar electricity-assisted industrial biogas methanation is investigated. • Batteries, compressed H 2 , or their combination are used as solar energy storage. • Compressed H 2 storage ensured the lowest production cost of methane (1.1 €/Sm 3 ). • A 40 MW photovoltaic park is required for optimized methanation of 800 Nm 3 biogas /h. • H 2 production/storage capital cost reduction is required for economic feasibility. This paper presents a design and techno-economic assessment of different Power-to-Gas configurations based on direct biogas methanation and renewable electricity. The proposed concept integrates the anaerobic digestion of organic waste with the methanation of carbon dioxide using green hydrogen. Yearly data of an anaerobic digestion process operating at the industrial scale were considered. The methanation unit was designed through two cooled fixed-bed reactors in series; the first had 14 parallel tubes that were 2.5 m long, and the second one had 18 tubes (each one 1.5 m long). A global carbon dioxide conversion above 98 % occurs in the unit, ensuring an outlet composition suitable for injection into the natural gas distribution grid. Different options for energy storage were thus considered; hydrogen storage in pressurized tanks (‘Buffer’), electrochemical storage in batteries (‘Battery’), and a hybrid combination of the two systems (‘Hybrid’). A ≈40 MW photovoltaic park provided the required energy input. The configuration with hydrogen storage tanks was established as the most promising option based on current trends, medium-term, and target projections scenarios of capital costs. These three cost scenarios led to a synthetic natural gas (SNG) production cost range of 2.3–4.2, 1.6–2.9, and 1.1–2.0 euros per cubic meter, respectively. This configuration requires a ≈35 MW electrolysis unit and about 100 tons of hydrogen storage capacity. Considering the current methane price, results indicate that current capital costs of photovoltaics, electrolysis, and H 2 storage still represent an obstacle to overcome, before achieving the profitability of the concept.

Authors

Institutions

Publication Details

Journal
Energy Conversion and Management
Published
2025-04-05
DOI
https://doi.org/10.1016/j.enconman.2025.119775
Citations
10
Primary Topic
Hybrid Renewable Energy Systems
Type
article
Field-Weighted Citation Impact
5.32

Funders

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

Direct biogas methanation via renewable-based Power-to-Gas: Techno-economic assessment based on real industrial data

Massimo Migliori, Giuseppe Zanardi, G. Giordano, Enrico Catizzone et al.
10 citations
Energy Conversion and Management
Hybrid Renewable Energy Systems
5.32
article

Direct biogas methanation via renewable-based Power-to-Gas: Techno-economic assessment based on real industrial data

Massimo Migliori, Giuseppe Zanardi, G. Giordano, Enrico Catizzone, Micaela Bianco, Emanuele Giglio
article en
10 citations

Abstract

• Solar electricity-assisted industrial biogas methanation is investigated. • Batteries, compressed H 2 , or their combination are used as solar energy storage. • Compressed H 2 storage ensured the lowest production cost of methane (1.1 €/Sm 3 ). • A 40 MW photovoltaic park is required for optimized methanation of 800 Nm 3 biogas /h. • H 2 production/storage capital cost reduction is required for economic feasibility. This paper presents a design and techno-economic assessment of different Power-to-Gas configurations based on direct biogas methanation and renewable electricity. The proposed concept integrates the anaerobic digestion of organic waste with the methanation of carbon dioxide using green hydrogen. Yearly data of an anaerobic digestion process operating at the industrial scale were considered. The methanation unit was designed through two cooled fixed-bed reactors in series; the first had 14 parallel tubes that were 2.5 m long, and the second one had 18 tubes (each one 1.5 m long). A global carbon dioxide conversion above 98 % occurs in the unit, ensuring an outlet composition suitable for injection into the natural gas distribution grid. Different options for energy storage were thus considered; hydrogen storage in pressurized tanks (‘Buffer’), electrochemical storage in batteries (‘Battery’), and a hybrid combination of the two systems (‘Hybrid’). A ≈40 MW photovoltaic park provided the required energy input. The configuration with hydrogen storage tanks was established as the most promising option based on current trends, medium-term, and target projections scenarios of capital costs. These three cost scenarios led to a synthetic natural gas (SNG) production cost range of 2.3–4.2, 1.6–2.9, and 1.1–2.0 euros per cubic meter, respectively. This configuration requires a ≈35 MW electrolysis unit and about 100 tons of hydrogen storage capacity. Considering the current methane price, results indicate that current capital costs of photovoltaics, electrolysis, and H 2 storage still represent an obstacle to overcome, before achieving the profitability of the concept.

Energy Conversion and ManagementVol. 332
Polo d’Innovazione di Genomica (IT), University of Calabria (IT)
European Commission
Affordable and clean energy
Openalex Percentile: Top 5%
Hybrid Renewable Energy Systems
5.32
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.