Feedstock

Feedstock is the organic raw material fed into a biogas plant - cattle dung, crop residues, press mud, food and municipal organic waste, and energy grasses. Its type and quality decide how much gas the plant makes, and its reliability decides whether the plant runs at all.

Paddy straw is the stalk left after the rice harvest - abundant across India and often burned, which is a major air-pollution source. It is fibrous and lignocellulosic, so it digests slowly and usually needs size reduction and co-digestion with a nitrogen-rich feed.

Press mud, or filter cake, is the residue left after sugarcane juice is clarified. It yields roughly 140-160 cubic metres of biogas per tonne and, crucially, arrives in bulk at a single site - which removes the aggregation problem that starves plants running on scattered residues.

Yes. Napier, or elephant grass, is a fast-growing energy crop that gives methane-rich biogas - about 63.5% methane as a mono-substrate in one study. It is lignocellulosic, so pretreatment and co-digestion improve yield, and it is water-hungry despite its drought tolerance.

Different feedstocks carry very different volatile-solids content and biogas yield per tonne, so the same plant produces very different gas volumes depending on what is fed. Wet, energy-dense feedstocks such as press mud, food waste and energy grass yield more per tonne than dry dung.

Cattle dung is a stable but modest feedstock, giving roughly 100-140 cubic metres of biogas per tonne, or about 0.20-0.30 cubic metres per kg VS. Much of its energy was already extracted by the animal, so its value is process stability and a nutrient-rich digestate rather than peak yield.

Poultry litter is high in nitrogen and protein, giving relatively high gas yield per tonne - often cited above 60-100 cubic metres. But its C:N ratio of around 10-12:1 makes ammonia inhibition a live risk, so it is normally co-digested with a carbon-rich substrate such as dung or straw.

Yes - segregated food waste and the organic fraction of MSW yield roughly 120-140 cubic metres per tonne, and using them solves a disposal problem at the same time. The hard part is contamination: plastics and grit demand robust pre-sorting, and they push project cost up sharply.

Indicative ranges per tonne: energy biomass and Napier about 220-290 cubic metres, horticulture waste 140-180, press mud 140-160, kitchen waste and MSW 120-140, cattle dung 100-140, chicken litter 90-120. Treat these as ranges for comparison, not as guarantees for sizing - real yield depends on TS/VS, pretreatment and operation.

Because moisture varies enormously between feedstocks - a wet tonne of dung is mostly water. Reporting per kg volatile solids lets you compare feedstocks fairly and size the digester on the organic load it actually has to process.

Co-digestion means feeding two or more feedstocks together to balance C:N, dilute inhibitors and stabilise the microbial community. It is usually a yield gain as well as a stability gain: adding just 5% paddy straw to cattle dung raised biogas to about 53.7 L/kg in one study.

Crop residues arrive in short harvest windows, so a plant that runs year-round has to store months of feedstock through baling or ensiling. Poor storage means dry-matter loss, lost methane potential, and idle capacity in the months between harvests.

Ensiling stores wet biomass such as Napier or straw under anaerobic, acidic conditions so it keeps its digestibility between harvests. Baling and covered storage protect dry residues from rain and rot. Both are how a seasonal crop becomes a year-round feed.

Headline biomass estimates far exceed what actually reaches a plant gate reliably; informal, sporadic supply starves digesters and collapses utilisation. GAIL's Executive Director for CBG puts it bluntly: India cannot build a large CBG industry around sporadic and informal feedstock procurement.

Spent wash, also called vinasse, is the high-COD liquid effluent from molasses-based distilleries. It is a strong but acidic, sulfate-rich substrate, usually digested in high-rate reactors, and it needs careful pH and sulfide management to stay stable.

Maize silage is among the highest-yielding crop substrates, at roughly 160-200 cubic metres per tonne, and it is the backbone of the European biogas fleet. Sorghum offers a similar structure with better drought tolerance. Both compete with food and fodder land use, which is politically sensitive in India.

Bagasse is heavily lignified, so it digests poorly, and it is normally burned in the mill's own boiler for captive power - meaning it carries a high opportunity cost as well as low digestibility. It is a co-substrate at most, not a base feed.

All three are lignocellulosic residues with high C:N and slow hydrolysis, so they need size reduction and often pretreatment before methane is released at a useful rate. Yields per tonne are moderate; their appeal is abundance and low gate cost, not ease of digestion.

Both are high-moisture, high-cellulose materials that digest reasonably well but carry very low dry-matter content, so large wet tonnages are needed per unit of gas. Water hyacinth also carries harvesting cost. Treat both as local, opportunistic feedstocks rather than a base load.

STP sludge is digestible but comparatively low-yielding per tonne, and it carries pathogen and heavy-metal considerations that affect what you can legally do with the digestate. It is more often a co-substrate or a municipal solution than a standalone CBG base.

Reported Napier biomass ranges from roughly 130 tonnes per acre per year on poorly managed land to nearly 280 with drip irrigation and disciplined fertigation, with Super Napier brochures claiming 350-400. One well-managed interior Andhra farm reached close to 280 while a farm 40 km away on similar soil but saline borewell water struggled past 130. Require location-specific, multi-season data before believing any figure.

As Napier matures, tonnage rises but lignin climbs and digestibility falls, so methane per tonne declines. The practical window is roughly 70-90 days, at 23-30% dry matter. Cut at 50 days it is mostly water; left past 120 days it is lignin-rich and hard to digest.

Traditional yields are about 90-110 cubic metres of biogas per tonne, equivalent to roughly 38-46 kg of CBG, with SSS-NIBE reporting a process reaching 150 cubic metres per tonne at 15-20 day HRT. A common rule of thumb is that about 20 tonnes of Napier make one tonne of Bio-CNG.

Vendor sizing suggests roughly 500 acres of Napier to feed a 10 TPD Bio-CNG plant, about 120 tonnes a day at around 33% solids. Napier is water-hungry despite its drought tolerance, so water availability must be checked against local supply before the land is committed - and that land is leased, not owned.

Ensiling preserves Napier for year-round feeding and can improve biogas yield, but the methane potential of a pile changes with silage age - a 30-day pile reads differently from a 45-day one. Farmers often skip silage on cost or risk grounds, which is exactly how a plant ends up with a seasonal supply and an annual target.

The core set is TS, VS, COD, lignin content and a BMP assay, which together predict achievable methane far better than a supplier's brochure. Running low-cost tests in-house across several silage ages - not one sample - is what makes plant design match the feedstock you will actually have.

Baling and collection, a collection radius that keeps haulage economic, and a per-tonne haulage cost that rises with distance. Past a certain radius transport eats the margin. A bankable radius with firm contracts matters more to output than nameplate capacity does.

There is no universal figure - the economic radius is set by bulk density, moisture and haulage rate. Wet, low-density biomass such as fresh Napier or water hyacinth travels economically for far shorter distances than baled straw does. The supply calendar exists to expose when radius and seasonality break supply together.

Open storage of wet biomass loses dry matter and methane potential to aerobic decay, and contamination with soil, grit or plastics abrades equipment while diluting gas yield. Covered storage, ensiling and clean handling protect both the yield and the machinery.

Specify price, quantity, quality - moisture and age window - and a delivery schedule that matches the plant's supply calendar, with penalties tied to feedstock that is realistically deliverable. Price discovery for energy crops is weak, so anchor the price to multi-season, location-specific data rather than a brochure.

Laboratory and field studies repeatedly show Napier co-digested with cattle dung or food waste yields more and runs more stably than Napier alone, because the co-substrate balances C:N and buffers pH. Mono-digestion of a single lignocellulosic crop is operationally fragile.

Feedstock and its logistics are the largest recurring cost and the main swing factor in IRR, which is why lenders treat secured, contracted supply as the first test of bankability. Feedstock choice alone can move project IRR from around 7% to over 20%.

Captive supply - a sugar mill's own press mud, or dedicated Napier on leased land - de-risks supply but ties up land and capital. Aggregated agri-residue is cheaper at the gate but exposes the plant to collection risk. Reliance's Andhra model leases barren land for captive Napier precisely to close that exposure.

Feedstock availability, price and quality determine utilisation, and utilisation drives IRR more than any single equipment choice. A plant with assured captive feedstock is far more bankable than one dependent on scattered aggregation, so investors should demand long-dated supply visibility and treat yield claims sceptically.

A hammer mill shreds and grinds biomass with rapidly spinning hammers, cutting particle size so microbes can attack more surface area. It is a common first step for fibrous feedstocks such as straw, and it draws real power - on the order of 25 kWh per tonne.

Smaller particles digest faster and more completely because enzymes can reach more surface. Choppers, shredders and hammer mills do that size reduction, and for lignocellulosic feed it is the difference between a digester that keeps up and one that silts up.

Pretreatment reduces particle size and disrupts lignocellulosic structure, exposing more surface to microbes and raising both the rate and the extent of digestion. For fibrous crops such as Napier or straw it is essential, because untreated lignocellulose resists microbial hydrolysis.

Raw biogas carries CO2, water vapour and corrosive, toxic hydrogen sulphide. H2S and moisture must go to protect engines, compressors and pipelines; CO2 is removed to raise energy density. Cleaning is the difference between a corrosive raw gas and a saleable fuel.

A chaff cutter or chopper cuts coarsely; a hammer mill grinds finer, typically to 1-5 cm for straw; twin-screw extruders and macerators additionally rupture fibre and pump the slurry. Finer size costs more energy, so this is a yield-versus-parasitic-load trade, not a straight upgrade.

Wet digestion runs at roughly 4-8% total solids as a pumpable slurry; dry digestion runs at about 15-40% TS. Dry and high-load reactors suit high-solids biomass, use less water and take a smaller footprint, but they need different handling equipment throughout.

A continuously stirred tank reactor is the general-purpose workhorse for slurries; plug-flow suits higher-solids feed and can reach higher loading rates, with dry plug-flow reactors claiming OLR up to about 11 kg VS per cubic metre per day; dry batch or garage-type suits stackable solids. The choice follows feedstock TS and yield target, not preference.

Heating holds the mesophilic window near 35-40 degrees C, usually with external heat exchangers or in-tank coils fed by a boiler burning a slice of the biogas - a heat demand on the order of 0.3 kWh per cubic metre of biogas. Mixing keeps microbes in contact with feed and prevents scum, settling and dead zones. Both draw parasitic energy.

Iron oxide on a wood-chip or pellet carrier reacts with hydrogen sulphide to form iron sulphide and water, exceeding 99.9% removal when properly sized - at ambient temperature and with no electricity. The media saturates and must be replaced or regenerated, and excess water has to be drained or the bed floods.

Activated carbon adsorbs hydrogen sulphide - often iron-impregnated for higher capacity - and is valued for simplicity and very low residual levels, usually as a polishing step after bulk removal. Like an iron sponge it saturates, so it needs periodic replacement or regeneration.

Sulfur-oxidising bacteria convert H2S to elemental sulfur or sulfate, either by dosing a small amount of air into the digester headspace or in a separate biotrickling filter - commercial trickling filters report over 94% removal on average. Air dosing must be tightly controlled: too much dilutes the methane and can create an explosive mixture.

Hammer mills, choppers and extruders reduce size mechanically, with twin-screw extrusion additionally shearing and defibrating. Thermal hydrolysis and steam explosion use heat and pressure to disrupt lignocellulose, while alkali, lime and enzymatic routes act chemically. Thermal-pressure hydrolysis has been shown to raise straw methane yield about 32% over milling alone.

Reinforced concrete, glass-fused-to-steel tanks, and HDPE-lined lagoons with floating covers are the common constructions, with mechanical, gas-mix or pump-recirculation agitation. The choice trades capital cost against corrosion resistance and lifespan - and an H2S-laden environment argues for the corrosion-resistant option.

Warm, water-saturated biogas drops liquid condensate as it cools in the pipework, which can block lines and is mildly acidic from dissolved H2S and CO2. Condensate traps and drain points are designed in to remove it continuously rather than at a shutdown.

A flare safely burns biogas that cannot be used - during commissioning, upgrading downtime or overproduction - converting methane to CO2 rather than venting a gas with far higher warming potential. An operational flare is a carbon-integrity device as much as a safety one.

Online analysers for CH4, CO2, O2 and H2S, plus pressure, temperature and flow, feeding a control system that can trip or divert off-spec gas. Reliable H2S measurement in particular lets operators dose scrubbing media to the actual load instead of over- or under-dosing it.

Upgrading - H2S removal plus CO2 separation - commonly accounts for roughly 20-25% of plant capex, making it a major technology line item. Because methane recovery and purity drive both revenue and the carbon claim, it is a spend where written guarantees matter more than brochure figures.

Pre-processing and handling is a major swing item and a common reason two nominally identical plants cost different amounts to build. Fibrous residues and segregated MSW need far more handling than press mud arriving by conveyor from the mill next door.

Heavier pretreatment such as extrusion or thermal hydrolysis raises yield but adds capital and parasitic energy, so it only pays where the feedstock is fibrous enough that the incremental methane exceeds the added cost. The answer is feedstock-specific, which is why the simulator lets you test it rather than assume it.