High space and investment demand
A separate hydrolysis stage and an independent digester require additional foundations, vessels, pipework and technical equipment.
Compact technical solution for bioenergy plants
The reactor combines a centrally arranged hydrolysis vessel with a surrounding anaerobic digester, post-digester or digestate store. Hydrolysis and methane fermentation remain spatially separated while sharing structural, thermal and gas-related functions.
Initial challenge
A separate hydrolysis stage and an independent digester require additional foundations, vessels, pipework and technical equipment.
Hydrolysis and fermentation require different stable temperature levels. Separate heating systems increase investment, maintenance and energy consumption.
Hydrolysis gases can contain oxygen, hydrogen and vapours of short-chain fatty acids. Inappropriate handling wastes energy and process potential.
Existing digesters or open digestate stores can often be converted into efficient gas-tight process stages only with considerable structural effort.
Operating principle
The corrosion-resistant hydrolysis vessel is arranged centrally inside a larger vessel for fermentation substrate. Both stages remain materially and biologically separated.
Metered air or oxygen supply through air lances or via the vortex generated by the central agitator enables demand-based hydrolysis.
The wall of the hydrolysis vessel is partly designed as a hot-water heating surface. It heats the hydrolysis stage and simultaneously transfers heat to the surrounding digester.
Oxygen-containing hydrolysis gases are routed into the gas space of the surrounding digester. The oxygen can support biological hydrogen-sulphide removal, while hydrogen and fatty-acid vapours can contribute to further biogas formation.
The surrounding vessel can be operated as a main digester, post-digester or heated gas-tight digestate store.
With at least two apparatus units, hydrolysis and fermentation can be operated alternately in batch mode. This enables defined hydrolysis periods, longer minimum anaerobic retention times and thermophilic hygienisation.
Design features
The central reaction zone is made of corrosion-resistant materials suitable for the acidic and oxygen-containing hydrolysis conditions.
The hydrolysis vessel can also serve as a structural central support for a rigid roof or the supporting system of a gas-storage membrane.
Immersion sleeves for mixing equipment allow replacement or maintenance without completely emptying the reaction zones when operated appropriately.
The solution can be integrated into new plants or used to upgrade existing digesters, post-digesters and previously open digestate stores.
Client benefits
Hydrolysis and fermentation are implemented within one combined vessel geometry without mixing the biological reaction zones.
The heated wall of the hydrolysis vessel also controls the temperature of the surrounding substrate zone. Separate heating surfaces in the outer vessel can be omitted.
Defined temperature, aeration and treatment time improve the biological breakdown of lignocellulosic feedstocks and can increase methane yield.
Upstream hydrolysis can reduce viscosity and floating-layer formation, accelerate carbon degradation and protect the methanation stage against over-acidification.
Hydrolysis gases are not discharged unused but are integrated into the anaerobic process and, where appropriate, into biological gas desulphurisation.
Existing digestate stores can be upgraded with a central hydrolysis vessel, heating and a gas-tight roof to form an additional biologically active gas-producing stage.
Technical background
The technical solution presented is based on European patent application EP 2 982 739 A1. Vessel volumes, heating surfaces, corrosion protection, mixing systems, gas routing and safety equipment must be designed specifically for the project, site and feedstock.
Technical project assessment