Reception & pretreatment
Weighbridge, enclosed reception, depackaging, maceration, screening and buffer storage. Sized around what actually arrives, including contamination and grit, not a clean design feed.
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Expertise · Process engineering
Anaerobic digestion, biogas and biomethane plants live or die on the process. Redrock designs, sizes and troubleshoots them from first principles: mass and energy balances, reaction kinetics, unit-operation design and hazardous-area engineering, grounded in how the biology actually behaves. This runs through every project we develop.
The flow sheet
Weighbridge, enclosed reception, depackaging, maceration, screening and buffer storage. Sized around what actually arrives, including contamination and grit, not a clean design feed.
Batch or continuous pasteurisation to the animal by-products rules, 70°C for one hour at a maximum 12 mm particle size, with heat recovered back into the process.
Mesophilic or thermophilic digestion, single or multi-stage, sized on retention time and organic loading and stabilised around the microbiology, not the equipment datasheet.
Biogas collection, hydrogen sulfide removal, drying, and gas storage, engineered for a safe, steady feed to upgrading or CHP.
Removing carbon dioxide to grid specification by the route that fits the site: water scrubbing, PSA, membrane, amine or a metal-organic-framework sorbent.
Separation, dewatering, concentration and nutrient recovery, turning digestate into a compliant product rather than a disposal liability.
Sizing & balances
A digester is sized on hydraulic retention time and organic loading rate, then checked against mixing power, heat demand and the biology's tolerance for ammonia, volatile fatty acids and sulfide. We build the mass and energy balance that ties feedstock, gas yield, heat and power together, so parasitic load and net export are known before anything is ordered.
Heat integration is where margin is won or lost. Pasteurisation heat, digester heating and upgrading demand are recovered against CHP and process streams, so the plant runs on its own energy wherever it can. Scale-up from bench and pilot BMP data to full scale is done with the same discipline, not by extrapolation.
Upgrading
There is no single best upgrading technology. The right choice depends on scale, the gas market, the site's power and heat, and the tolerance for methane slip. We specify across the full set.
Robust, water-only, well understood. Higher parasitic power and footprint, no chemicals.
Adsorbent beds cycling on pressure. Compact and dry, with methane slip to manage.
Selective polymer membranes, modular and low-maintenance, sensitive to gas conditioning upstream.
Chemical absorption for very high methane recovery and very low slip, at a heat cost.
A high-selectivity sorbent route. Redrock holds a licence to a MOF-based upgrading technology, a distinctive option in our toolkit.
To market
Where a grid connection exists, biomethane is conditioned and metered to network specification for injection. Where it does not, we design the CNG virtual pipeline: compression to around 250 bar, cascade filling, multiple-element gas containers for road transport, and the decompression and metering skid at the receiving end.
Both routes are engineered to the hazardous-area rules from the outset, with ATEX zoning, gas detection and the transport code requirements built into the layout rather than added afterward.
Safety by design
Biogas is flammable and plants handle it at pressure. Safety is engineered in, not bolted on: process and instrumentation diagrams, HAZOP and LOPA studies, ATEX and DSEAR hazardous-area classification, relief and blowdown, and the control and shutdown philosophy. The result is a plant that is safe to operate and straightforward to permit.
From a flow sheet on a new project to troubleshooting an existing digester, let's talk about the process.
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