Read time : 11 min
Updated on 9 April 2026

Technical proposal for anaerobic digestion & biogas projects

Anaerobic digestion is booming in France: the national biogas plan targets 10% renewable gas by 2030. Local authorities, waste management bodies and farms regularly tender for the construction, operation or maintenance of biogas plants. This guide covers the specifics of technical proposals in this fast-growing sector.

Regulatory framework for anaerobic digestion

Anaerobic digestion is governed by several regulations that shape the technical proposal.

ICPE 2781: the applicable regime

Any biogas plant falls under ICPE classification 2781 (anaerobic digestion of non-hazardous waste). Depending on capacity, the installation requires declaration (under 30 t/d), registration (30-100 t/d) or full authorisation (over 100 t/d). The proposal must state the applicable regime and demonstrate compliance with setback distances, risk prevention (ATEX, fire), effluent management and nuisance control.

Feed-in tariffs and guarantees of origin

For biomethane injection, feed-in tariffs are set by decree and depend on production capacity and feedstock type. For CHP, the electricity purchase tariff is guaranteed for 20 years. The economic section must reference current tariffs and biogas production certificates (guarantees of origin).

Spreading plan and digestate management

Digestate must be managed in compliance with regulations. The spreading plan is mandatory, defining receiving plots, maximum doses, exclusion periods and analysis programme. The proposal must present the digestate valorisation strategy: direct spreading, phase separation, composting or drying.

Structuring the biogas technical proposal

The technical proposal for a biogas project covers plant design, feedstock management and biogas valorisation.

Mass balance and feedstock assessment

Present: feedstock list with annual tonnages, biochemical methane potential (BMP) per substrate, overall mass balance (inputs, biogas produced, digestate), and supply security (contracts, transport distances, storage). A 15-20 year supply plan with alternatives is highly valued.

Digester design and process

Detail the digester type (CSTR, plug flow, dry digestion), operating conditions (mesophilic 38°C or thermophilic 55°C), hydraulic retention time (HRT), organic loading rate, and associated equipment. Justify wet vs dry process based on feedstock characteristics.

Biogas valorisation: CHP vs grid injection

The valorisation choice is structural. Present a techno-economic analysis comparing: grid proximity, heat offtake opportunities, applicable tariffs, investment and comparative profitability.

Safety: ATEX, fire, odour

Biogas contains methane (55-65%) and hydrogen sulphide: present ATEX zoning, gas detectors, safety flare, ventilation, emergency response plan, and staff training. Odour management is often an explicit scoring criterion.

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