Components

needs a citation Cite Indian napier BMP study (IARI / TERI range 260-320 Nm3/t-VS)

needs a citation Cite Indian napier BMP study (IARI / TERI range 260-320 Nm3/t-VS)

needs a citation Cite Indian napier BMP study (IARI / TERI range 260-320 Nm3/t-VS)

needs a citation Cite Indian napier BMP study (IARI / TERI range 260-320 Nm3/t-VS)

needs a citation Cite Indian napier BMP study (IARI / TERI range 260-320 Nm3/t-VS)

projection Ensiled energy grass. Lignocellulosic, but ensiling partly pre-hydrolyses the feed, so it sits above untreated straw and below mixed organics. Supersede with a measured value from the Kalaburagi trial the moment BMP-by-cut-age exists. Literature range for this substrate class. First-order hydrolysis constants for anaerobic digestion are conventionally reported in the 0.02-0.7 /d band, clustering by class: soluble sugars fastest, untreated lignocellulose slowest, manures and mixed organics between. Reviews of particulate hydrolysis kinetics (Vavilin and co-workers) and the ADM1 model report (Batstone and co-workers, IWA STR 13) are the basis for the bands.

derived Total solids × volatile fraction. The plant is sized off this, not off the tonnage on the weighbridge.

derived BMP at infinite retention. A real reactor reaches a fraction of it, set by the hydrolysis constant above and the retention time of the digester it feeds.

projection National reference, not a quote. Delivered price is a per-project number and the node dial overrides it.

assumed Palette default only. Never a modelling input once the author sets tonnage.

derived Ported from the config engine's four feedstock buckets. Replaced by per-feedstock sourced figures at stage 6.

projection Soil carbon under a perennial energy crop.

projection Reception, weighbridge, storage pad and bunker on delivered tonnage. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

needs a citation Cite ISMA / NSI pressmud characterisation

needs a citation Cite ISMA / NSI pressmud characterisation

needs a citation Cite ISMA / NSI pressmud characterisation

needs a citation Cite ISMA / NSI pressmud characterisation

needs a citation Cite ISMA / NSI pressmud characterisation

projection Sugar-mill filter cake. Already partly degraded by the milling process, but waxy, which slows the accessible fraction. Literature range for this substrate class. First-order hydrolysis constants for anaerobic digestion are conventionally reported in the 0.02-0.7 /d band, clustering by class: soluble sugars fastest, untreated lignocellulose slowest, manures and mixed organics between. Reviews of particulate hydrolysis kinetics (Vavilin and co-workers) and the ADM1 model report (Batstone and co-workers, IWA STR 13) are the basis for the bands.

derived Total solids × volatile fraction. The plant is sized off this, not off the tonnage on the weighbridge.

derived BMP at infinite retention. A real reactor reaches a fraction of it, set by the hydrolysis constant above and the retention time of the digester it feeds.

projection National reference, not a quote. Delivered price is a per-project number and the node dial overrides it.

assumed Palette default only. Never a modelling input once the author sets tonnage.

derived Ported from the config engine's four feedstock buckets. Replaced by per-feedstock sourced figures at stage 6.

projection Reception, weighbridge, storage pad and bunker on delivered tonnage. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

needs a citation Cite molasses BMP (commonly 350-400 Nm3/t-VS)

needs a citation Cite molasses BMP (commonly 350-400 Nm3/t-VS)

needs a citation Cite molasses BMP (commonly 350-400 Nm3/t-VS)

needs a citation Cite molasses BMP (commonly 350-400 Nm3/t-VS)

needs a citation Cite molasses BMP (commonly 350-400 Nm3/t-VS)

projection Soluble sugars. Hydrolysis is not the rate-limiting step at all here — the band is wide upward because for this substrate the model's assumption stops mattering rather than becoming more precise. Literature range for this substrate class. First-order hydrolysis constants for anaerobic digestion are conventionally reported in the 0.02-0.7 /d band, clustering by class: soluble sugars fastest, untreated lignocellulose slowest, manures and mixed organics between. Reviews of particulate hydrolysis kinetics (Vavilin and co-workers) and the ADM1 model report (Batstone and co-workers, IWA STR 13) are the basis for the bands.

derived Total solids × volatile fraction. The plant is sized off this, not off the tonnage on the weighbridge.

derived BMP at infinite retention. A real reactor reaches a fraction of it, set by the hydrolysis constant above and the retention time of the digester it feeds.

projection National reference, not a quote. Delivered price is a per-project number and the node dial overrides it.

assumed Palette default only. Never a modelling input once the author sets tonnage.

derived Ported from the config engine's four feedstock buckets. Replaced by per-feedstock sourced figures at stage 6.

projection Reception, weighbridge, storage pad and bunker on delivered tonnage. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

needs a citation Cite ICAR paddy straw BMP (Punjab/Haryana stubble studies)

needs a citation Cite ICAR paddy straw BMP (Punjab/Haryana stubble studies)

needs a citation Cite ICAR paddy straw BMP (Punjab/Haryana stubble studies)

needs a citation Cite ICAR paddy straw BMP (Punjab/Haryana stubble studies)

needs a citation Cite ICAR paddy straw BMP (Punjab/Haryana stubble studies)

projection Untreated lignocellulose, high lignin. The slowest thing in the catalogue and a factor of four across the band, which is an honest statement about untreated straw. Pretreatment would move this and the engine claims no such uplift (law 3). Literature range for this substrate class. First-order hydrolysis constants for anaerobic digestion are conventionally reported in the 0.02-0.7 /d band, clustering by class: soluble sugars fastest, untreated lignocellulose slowest, manures and mixed organics between. Reviews of particulate hydrolysis kinetics (Vavilin and co-workers) and the ADM1 model report (Batstone and co-workers, IWA STR 13) are the basis for the bands.

derived Total solids × volatile fraction. The plant is sized off this, not off the tonnage on the weighbridge.

derived BMP at infinite retention. A real reactor reaches a fraction of it, set by the hydrolysis constant above and the retention time of the digester it feeds.

projection National reference, not a quote. Delivered price is a per-project number and the node dial overrides it.

assumed Palette default only. Never a modelling input once the author sets tonnage.

derived Ported from the config engine's four feedstock buckets. Replaced by per-feedstock sourced figures at stage 6.

projection Reception, weighbridge, storage pad and bunker on delivered tonnage. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

needs a citation Cite cane trash characterisation (VSI / SBI)

needs a citation Cite cane trash characterisation (VSI / SBI)

needs a citation Cite cane trash characterisation (VSI / SBI)

needs a citation Cite cane trash characterisation (VSI / SBI)

needs a citation Cite cane trash characterisation (VSI / SBI)

projection Untreated lignocellulose, comparable to straw and marginally more accessible. Literature range for this substrate class. First-order hydrolysis constants for anaerobic digestion are conventionally reported in the 0.02-0.7 /d band, clustering by class: soluble sugars fastest, untreated lignocellulose slowest, manures and mixed organics between. Reviews of particulate hydrolysis kinetics (Vavilin and co-workers) and the ADM1 model report (Batstone and co-workers, IWA STR 13) are the basis for the bands.

derived Total solids × volatile fraction. The plant is sized off this, not off the tonnage on the weighbridge.

derived BMP at infinite retention. A real reactor reaches a fraction of it, set by the hydrolysis constant above and the retention time of the digester it feeds.

projection National reference, not a quote. Delivered price is a per-project number and the node dial overrides it.

assumed Palette default only. Never a modelling input once the author sets tonnage.

derived Ported from the config engine's four feedstock buckets. Replaced by per-feedstock sourced figures at stage 6.

projection Reception, weighbridge, storage pad and bunker on delivered tonnage. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

needs a citation Cite Indian dairy manure BMP (NDDB / IGFRI)

needs a citation Cite Indian dairy manure BMP (NDDB / IGFRI)

needs a citation Cite Indian dairy manure BMP (NDDB / IGFRI)

needs a citation Cite Indian dairy manure BMP (NDDB / IGFRI)

needs a citation Cite Indian dairy manure BMP (NDDB / IGFRI)

projection Ruminant manure is the best-characterised substrate in this table; roughly 0.13 /d is the figure most commonly reported for mesophilic cattle slurry. Literature range for this substrate class. First-order hydrolysis constants for anaerobic digestion are conventionally reported in the 0.02-0.7 /d band, clustering by class: soluble sugars fastest, untreated lignocellulose slowest, manures and mixed organics between. Reviews of particulate hydrolysis kinetics (Vavilin and co-workers) and the ADM1 model report (Batstone and co-workers, IWA STR 13) are the basis for the bands.

derived Total solids × volatile fraction. The plant is sized off this, not off the tonnage on the weighbridge.

derived BMP at infinite retention. A real reactor reaches a fraction of it, set by the hydrolysis constant above and the retention time of the digester it feeds.

projection National reference, not a quote. Delivered price is a per-project number and the node dial overrides it.

assumed Palette default only. Never a modelling input once the author sets tonnage.

derived Ported from the config engine's four feedstock buckets. Replaced by per-feedstock sourced figures at stage 6.

projection Manure that would otherwise have emitted methane from an open lagoon.

projection Reception, weighbridge, storage pad and bunker on delivered tonnage. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

needs a citation Cite CPCB / SBM-U MSW organic fraction BMP

needs a citation Cite CPCB / SBM-U MSW organic fraction BMP

needs a citation Cite CPCB / SBM-U MSW organic fraction BMP

needs a citation Cite CPCB / SBM-U MSW organic fraction BMP

needs a citation Cite CPCB / SBM-U MSW organic fraction BMP

projection Organic fraction of municipal solid waste. The band is wide because the substrate is: composition varies with collection, season and how well segregation actually works. Literature range for this substrate class. First-order hydrolysis constants for anaerobic digestion are conventionally reported in the 0.02-0.7 /d band, clustering by class: soluble sugars fastest, untreated lignocellulose slowest, manures and mixed organics between. Reviews of particulate hydrolysis kinetics (Vavilin and co-workers) and the ADM1 model report (Batstone and co-workers, IWA STR 13) are the basis for the bands.

derived Total solids × volatile fraction. The plant is sized off this, not off the tonnage on the weighbridge.

derived BMP at infinite retention. A real reactor reaches a fraction of it, set by the hydrolysis constant above and the retention time of the digester it feeds.

projection National reference, not a quote. Delivered price is a per-project number and the node dial overrides it.

assumed Palette default only. Never a modelling input once the author sets tonnage.

derived Ported from the config engine's four feedstock buckets. Replaced by per-feedstock sourced figures at stage 6.

projection Organic fraction diverted from a landfill that would have emitted it.

projection Reception, weighbridge, storage pad and bunker on delivered tonnage. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

needs a citation Cite urban food waste BMP (commonly 300-400 Nm3/t-VS)

needs a citation Cite urban food waste BMP (commonly 300-400 Nm3/t-VS)

needs a citation Cite urban food waste BMP (commonly 300-400 Nm3/t-VS)

needs a citation Cite urban food waste BMP (commonly 300-400 Nm3/t-VS)

needs a citation Cite urban food waste BMP (commonly 300-400 Nm3/t-VS)

projection Source-segregated food waste. Readily hydrolysable, second only to soluble sugars. Literature range for this substrate class. First-order hydrolysis constants for anaerobic digestion are conventionally reported in the 0.02-0.7 /d band, clustering by class: soluble sugars fastest, untreated lignocellulose slowest, manures and mixed organics between. Reviews of particulate hydrolysis kinetics (Vavilin and co-workers) and the ADM1 model report (Batstone and co-workers, IWA STR 13) are the basis for the bands.

derived Total solids × volatile fraction. The plant is sized off this, not off the tonnage on the weighbridge.

derived BMP at infinite retention. A real reactor reaches a fraction of it, set by the hydrolysis constant above and the retention time of the digester it feeds.

projection National reference, not a quote. Delivered price is a per-project number and the node dial overrides it.

assumed Palette default only. Never a modelling input once the author sets tonnage.

derived Ported from the config engine's four feedstock buckets. Replaced by per-feedstock sourced figures at stage 6.

projection Organic fraction diverted from a landfill that would have emitted it.

projection Reception, weighbridge, storage pad and bunker on delivered tonnage. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

needs a citation Cite shredder specific energy for green biomass (4-8 kWh/t typical)

projection Handling cost per tonne through the machine.

projection Indicative industrial tariff. State-specific, and one of the first inputs a developer should replace with their own.

projection Prep machine base rate before the specific-energy term. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Added to the prep base rate per kWh/t of specific energy. Apportionment of published project costs, not a quoted price — never present as one.

needs a citation Cite hammer mill specific energy for cereal straw (20-40 kWh/t typical)

projection Handling cost per tonne through the machine.

projection Indicative industrial tariff. State-specific, and one of the first inputs a developer should replace with their own.

projection Prep machine base rate before the specific-energy term. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Added to the prep base rate per kWh/t of specific energy. Apportionment of published project costs, not a quoted price — never present as one.

needs a citation Extruder BMP uplift is real but uncited here - cost only, no yield claim

projection Handling cost per tonne through the machine.

projection Indicative industrial tariff. State-specific, and one of the first inputs a developer should replace with their own.

projection Prep machine base rate before the specific-energy term. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Added to the prep base rate per kWh/t of specific energy. Apportionment of published project costs, not a quoted price — never present as one.

needs a citation Cite conveying specific energy

projection Handling cost per tonne through the machine.

projection Indicative industrial tariff. State-specific, and one of the first inputs a developer should replace with their own.

projection Prep machine base rate before the specific-energy term. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Added to the prep base rate per kWh/t of specific energy. Apportionment of published project costs, not a quoted price — never present as one.

projection Blending and feed preparation on tonnes mixed. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Workable above this, but with no headroom left for a feed swing.

projection Acidification risk above this loading.

projection Below this the microbial population washes out.

projection Above this the feed stops being pumpable, which is what a CSTR requires.

projection Optimum for the bell-curve derate. Mesophilic communities peak near 35C; dry plug-flow runs warmer.

projection Spread of the derate curve. Wider means the reactor tolerates more temperature swing.

derived Sets how retention time turns into gas. A plug-flow reactor gets more out of the same HRT than a fully mixed tank, because nothing short-circuits the outlet.

projection Tank, mixers, heating, gas holder, on active volume. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Workable above this, but with no headroom left for a feed swing.

projection Acidification risk above this loading.

projection Below this the microbial population washes out.

projection Below this the feed is too wet to stack and move through a dry reactor without channelling.

projection Optimum for the bell-curve derate. Mesophilic communities peak near 35C; dry plug-flow runs warmer.

projection Spread of the derate curve. Wider means the reactor tolerates more temperature swing.

derived Sets how retention time turns into gas. A plug-flow reactor gets more out of the same HRT than a fully mixed tank, because nothing short-circuits the outlet.

projection Tank, mixers, heating, gas holder, on active volume. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Methane purity the upgrading skid is specified to. IS 16087 requires at least 90%.

projection Methane retained through upgrading. The 3% lost is vented in this model and is not yet counted as a fugitive emission — stage 6.

projection Methane fraction assumed when converting CBG mass to delivered energy.

projection Upgrading skid on raw biogas throughput, Nm3/h. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Mass retained through compression and dispensing. What is lost is venting and heel, not conversion.

sourced Physical constant, methane density at STP

sourced Lower heating value of methane, 35.8 MJ/Nm3

projection Compressor, cascade storage and dispensing on CBG capacity. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Biochar mass per unit of dry digestate. Varies with pyrolysis temperature and residence time, neither of which is modelled yet.

projection Biochar carbon held out of the atmosphere. A removal, never summed with avoidance.

projection Pyrolysis reactor on biochar output. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Digestate recovered as FOM per tonne of fresh feed. Replaced by a digestate mass balance at stage 2.

projection Indicative bulk price. FOM in particular is an estimate pending a digestate assay and a real offtake quote, and must not be presented as sourced until both exist.

projection Digestate displacing synthetic fertiliser when recovered as FOM.

projection Separation, drying yard and bagging on FOM tonnage. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Indicative bulk price. FOM in particular is an estimate pending a digestate assay and a real offtake quote, and must not be presented as sourced until both exist.

projection Biochar carbon held out of the atmosphere. A removal, never summed with avoidance.

sourced Physical constant, carbon dioxide density at STP

projection Indicative bulk price. FOM in particular is an estimate pending a digestate assay and a real offtake quote, and must not be presented as sourced until both exist.

projection Liquefaction, purification to food grade, and storage. Apportionment of published project costs, not a quoted price — never present as one.

derived Reference duty at which the unit rate applies. Moving it without moving the rate re-prices every plant size.

projection Six-tenths-rule capacity factor: unit cost moves as (duty/ref)^(exponent-1). Held in the 0.88-0.97 band because Indian CBG equipment is modular rather than refinery-scale, and because the three sourced anchors themselves show only mild scale economy. A structural claim about how cost behaves, not a measured quantity.

projection Gate price is a scenario input, not a constant. The author's dial overrides it and the brief prints whichever was used.

projection Cost of reaching the buyer on this route. Distance-specific, and a real per-project input.

pending verification Administered floor, GOBARdhan — National Circular Bioenergy Scheme, Union Cabinet 6 Aug 2026 (guaranteed minimum, 10 years)

projection Tankered to an OMC retail outlet under SATAT.

projection Loading bay only. The tanker fleet is the buyer's.

derived Global scale factor, set against the two internally consistent anchors (10 and 25 TPD) built at their own stated feed and reactor volume. Residuals after calibration: -3.3% at 10 TPD, +3.3% at 25 TPD. The residual spread between the two anchors is set by the scale exponents, not by this constant, so 3.3% is the best a single factor can do; narrowing it means refitting the exponents.

projection Gate price is a scenario input, not a constant. The author's dial overrides it and the brief prints whichever was used.

projection Cost of reaching the buyer on this route. Distance-specific, and a real per-project input.

pending verification Administered floor, GOBARdhan — National Circular Bioenergy Scheme, Union Cabinet 6 Aug 2026 (guaranteed minimum, 10 years)

projection Injected into a city gas grid at the plant boundary.

projection Grid injection point: metering, odorisation, custody transfer.

derived Global scale factor, set against the two internally consistent anchors (10 and 25 TPD) built at their own stated feed and reactor volume. Residuals after calibration: -3.3% at 10 TPD, +3.3% at 25 TPD. The residual spread between the two anchors is set by the scale exponents, not by this constant, so 3.3% is the best a single factor can do; narrowing it means refitting the exponents.