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Energy Meter Allocation per Good Kilogram or Metre

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The kilograms you scrapped were heated, dried and finished at full price.

Plant Meters for the Period One period, one boundary, all four utilities
kWh

Site import for the period, compressor motors included

kWh

Stenters, singeing, direct dryers. Exclude boiler fuel - it is derived from the steam figure. Meter m3 x calorific value, about 10.55 kWh/m3 for natural gas

t

From the boiler-house flow meter, not the fuel meter

kWh/t

Enthalpy rise over feedwater: about 680 kWh/t for saturated steam at 8 bar g raised from 85 deg C feedwater

Conversion Losses & Sub-Meters What the utilities cost before the fabric sees them
%

Carries flue, blowdown, standing and distribution losses together, on the same calorific-value basis as the gas bill

Nm3

Free air delivered for the period, measured as in ISO 1217

kWh/Nm3

Package figure at the working pressure: 0.10 to 0.13 kWh/Nm3 for a 7 bar g screw compressor

Output, Losses & Standby What the energy actually turned into
kg

Everything the plant ran, good and rejected together

kg

Scrapped or downgraded to waste - not first quality at any price

g/m

Width x mass per m2: 1.8 m at 233 g/m2 is 420 g/m

kWh

Read the weekend or night floor off the half-hourly profile and add the banked boiler

Energy per Good Kilogram

— kWh/kg

All site energy over saleable output only - the EnPI to quote

Allocation Across Product, Scrap & Standby

Energy per Kilogram Processed (the shortcut)
— kWh/kg
Energy per Good Metre
— kWh/m
Production-Related Energy per Good Kilogram
— kWh/kg
Site Energy at the Fuel Boundary
— kWh
Energy Carried Out by Scrap
— kWh
Site Energy That Made Nothing Saleable
— %
Boiler House & Steam Main Loss
— kWh
Compressed Air Share of the Electricity Meter
— %

Allocation here is by mass at average intensity, which is a deliberate simplification with two known biases. Fabric rejected at final inspection carried the full process energy, while fabric pulled at grey inspection carried almost none, so a mass-weighted scrap charge is an upper bound when rejects are found early and an underestimate when they are found late; if your rejection point is known, weight the scrap by the fraction of the route it completed. Product mix cuts the same way, because a heavy navy at long liquor ratio can take twice the energy per kilogram of a pale continuous run, so mass allocation quietly subsidises the difficult product. The compressed air figure is a sub-meter of electricity and must never be added to the site total; the tool reports it as a share for exactly that reason. Direct-fired gas must exclude boiler fuel, which is reconstructed from the steam and efficiency figures instead. Boiler efficiency is intended as a boiler-house-to-process figure covering flue, blowdown, standing and distribution loss on the same calorific-value basis as the gas bill - a net-basis efficiency against a gross-basis bill overstates performance by about ten per cent for natural gas. Steam heat per tonne must match the working pressure and the real feedwater temperature; the 680 kWh/t default corresponds to saturated steam near 8 bar g from 85 deg C feedwater with no condensate return credit, and a site returning hot condensate should lower it. Standby energy is usually estimated rather than metered, read off the half-hourly profile floor, and it is the input most worth improving. The per-metre result is only meaningful for a single fabric construction, since it is simply the per-kilogram figure multiplied by mass per metre. Finally, this is a plant-boundary allocation tool and not a machine study: it will tell you how much of the site bill made nothing saleable, but it cannot tell you which machine spent it.

Using this calculator

About the Energy Meter Allocation per Good Kilogram or Metre

The formula

This is the expression the tool evaluates. Every term is named underneath, with the unit it must be supplied in.

Four meters onto one kWh basis at the fuel boundary
steamFuel = steamTonnes x steamHeatPerTonne / ( boilerEfficiency / 100 ) E_site = electricityKwh + gasKwh + steamFuel

Steam is metered as mass, so it has to be valued in heat: by IAPWS-IF97 saturated steam at 9 bar absolute carries about 2773 kJ/kg and feedwater at 85 deg C about 356 kJ/kg, so a tonne delivers roughly 2417 MJ or 671 kWh. Dividing by the boiler-house efficiency puts the flue, blowdown and mains losses back inside the boundary, which is where a plant that owns its boiler has to keep them.

The same numerator over two different denominators
energyPerGoodKg = E_site / ( grossOutputKg - rejectedKg ) energyPerGrossKg = E_site / grossOutputKg

The ratio between the two figures is exactly one over the yield, so a plant running 96 per cent first quality understates its true specific energy consumption by about 4 per cent every month it uses the shortcut. Nothing in the meters changes; only the honesty of the denominator does.

Energy that left as waste and energy that left as heat
scrapEnergy = ( E_site - standbyKwh ) x rejectedKg / grossOutputKg nonProductiveShare = ( standbyKwh + scrapEnergy ) / E_site x 100

Standby energy made nothing, so it is not spread over mass - it is a fixed loss reported on its own. Scrap is charged only with production energy, at the average intensity of the mass that went through. Together they are the share of the bill that bought no saleable product, and it is normally the largest single line on a wet processing site.

Compressed air as a slice, never as an addition
airKwh = compressedAirNm3 x airSpecificPower airShareOfElectricity = airKwh / electricityKwh x 100

The compressor motors are already on the electricity meter, so adding their kWh to the site total counts them twice - the commonest arithmetic error in plant energy accounting. Reported against electricity instead, air becomes comparable with the fan, pump and drive loads it competes with for capital.

Symbols used above
SymbolStands forUnit
E_siteTotal site energy on one kWh basis at the purchase boundarykWh
m_grossOutput processed in the period, good plus rejectedkg
m_goodSaleable output in the periodkg
eta_bBoiler-house-to-process efficiency, flue and distribution losses included%
E_sbEnergy consumed in hours when nothing was producedkWh

How the result is derived

Step by step, from the values you type to the figure on screen.

  1. The 11 inputs are read from the form on every keystroke: Electricity Imported, Direct-Fired Process Gas, Steam Delivered to Process, Heat Content of the Steam, Boiler House to Process Efficiency, Compressed Air Delivered, Compressor Specific Power, Output Processed, Output Not Saleable, Fabric Mass per Metre and Energy in Non-Production Hours.
  2. Each value is checked against the accepted range in the input table below. A value outside its range stops the calculation rather than producing a misleading figure — the results blank out and a message appears.
  3. The validated values are substituted into the expression above, which resolves Energy per Good Kilogram together with every supporting figure in one pass — no value is carried over from a previous entry.
  4. The supporting outputs — Energy per Kilogram Processed (the shortcut), Energy per Good Metre, Production-Related Energy per Good Kilogram, Site Energy at the Fuel Boundary, Energy Carried Out by Scrap, Site Energy That Made Nothing Saleable, Boiler House & Steam Main Loss and Compressed Air Share of the Electricity Meter — come from the same pass, so they always describe the same case as the headline figure.
  5. Results are rounded for display only. The full-precision value is used throughout the chain, so reading a rounded intermediate figure back into the tool by hand can shift the last digit.

What each input means

Where to read each value on the floor, the unit it must be in, and the range the tool accepts.

InputUnitAccepted rangeDefaultWhat it means
Electricity ImportedkWh100 to 50000000 kWh214000Site import for the period, compressor motors included
Direct-Fired Process GaskWh0 to 50000000 kWh190000Stenters, singeing, direct dryers. Exclude boiler fuel - it is derived from the steam figure. Meter m3 x calorific value, about 10.55 kWh/m3 for natural gas
Steam Delivered to Processt0 to 100000 t690From the boiler-house flow meter, not the fuel meter
Heat Content of the SteamkWh/t350 to 900 kWh/t680Enthalpy rise over feedwater: about 680 kWh/t for saturated steam at 8 bar g raised from 85 deg C feedwater
Boiler House to Process Efficiency%40 to 98 %82Carries flue, blowdown, standing and distribution losses together, on the same calorific-value basis as the gas bill
Compressed Air DeliveredNm30 to 20000000 Nm3380000Free air delivered for the period, measured as in ISO 1217
Compressor Specific PowerkWh/Nm30.06 to 0.3 kWh/Nm30.115Package figure at the working pressure: 0.10 to 0.13 kWh/Nm3 for a 7 bar g screw compressor
Output Processedkg100 to 20000000 kg186000Everything the plant ran, good and rejected together
Output Not Saleablekg0 to 5000000 kg7400Scrapped or downgraded to waste - not first quality at any price
Fabric Mass per Metreg/m20 to 3000 g/m420Width x mass per m2: 1.8 m at 233 g/m2 is 420 g/m
Energy in Non-Production HourskWh0 to 20000000 kWh78000Read the weekend or night floor off the half-hourly profile and add the banked boiler

What the tool returns

The headline figure and every supporting value it is built from.

OutputUnitWhat it tells you
Energy per Good Kilogram (headline result)kWh/kgAll site energy over saleable output only - the EnPI to quote
Energy per Kilogram Processed (the shortcut)kWh/kg
Energy per Good MetrekWh/m
Production-Related Energy per Good KilogramkWh/kg
Site Energy at the Fuel BoundarykWh
Energy Carried Out by ScrapkWh
Site Energy That Made Nothing Saleable%
Boiler House & Steam Main LosskWh
Compressed Air Share of the Electricity Meter%

Worked example

Given

0
Electricity imported 214,000 kWh; direct-fired process gas 190,000 kWh
1
Steam to process 690 t at 680 kWh/t, boiler house to process 82 per cent
2
Compressed air 380,000 Nm3 at 0.115 kWh/Nm3
3
Processed 186,000 kg, of which 7,400 kg not saleable
4
Fabric 420 g/m; 78,000 kWh consumed in non-production hours

Substituting

Steam heat delivered = 690 x 680 = 469200 kWh; fuel behind it = 469200 / 0.82 = 572195.122 kWhboilerLossKwh = 572195.122 - 469200 = 102995.122 kWhtotalEnergyKwh = 214000 + 190000 + 572195.122 = 976195.122 kWhGood output = 186000 - 7400 = 178600 kg, so energyPerGoodKg = 976195.122 / 178600 = 5.4658 against energyPerGrossKg = 976195.122 / 186000 = 5.2484 kWh/kgGood metres = 178600 x 1000 / 420 = 425238.0952 m, so energyPerGoodMetre = 976195.122 / 425238.0952 = 2.2956 kWh/mProduction energy = 976195.122 - 78000 = 898195.122 kWh; scrapEnergyKwh = 898195.122 x 7400 / 186000 = 35734.6446 kWhnonProductiveSharePct = ( 78000 + 35734.6446 ) / 976195.122 x 100 = 11.6508 per centAir = 380000 x 0.115 = 43700 kWh, which is 20.4206 per cent of electricity but 43700 / 976195.122 = 4.48 per cent of site energy, against the boiler loss at 102995.122 / 976195.122 = 10.55 per cent

Answer

0
energyPerGoodKg 5.4658 kWh/kg
1
energyPerGrossKg 5.2484 kWh/kg
2
energyPerGoodMetre 2.2956 kWh/m
3
variableEnergyPerGoodKg 5.0291 kWh/kg
4
totalEnergyKwh 976195.122 kWh
5
scrapEnergyKwh 35734.6446 kWh
6
nonProductiveSharePct 11.6508 per cent
7
boilerLossKwh 102995.122 kWh
8
airShareOfElectricityPct 20.4206 per cent

The plant quotes 5.2484 kWh/kg, because that is the meters divided by the production report. The figure it owes its customers and its own baseline is 5.4658 kWh/kg, and the 4.1 per cent between them is 7,400 kg of fabric that was scoured, dyed, dried and finished at full energy cost and then sold as waste. Two further numbers reorder the whole improvement plan. The compressed air system, which the last audit called twenty per cent of the load, is 20.4206 per cent of the electricity meter but only 4.48 per cent of site energy. The boiler house and steam mains lose 102995.122 kWh, or 10.55 per cent - two and a third times the entire air system, and on most sites the only one of the two nobody has metered.

How to use it

  1. Work through the input groups in order — Plant Meters for the Period, Conversion Losses & Sub-Meters and Output, Losses & Standby. The defaults are a realistic case, so you can change one value at a time and watch what moves.
  2. There is no calculate button. Every figure recalculates as you type or drag, which is what makes this usable for a what-if sweep rather than a single answer.
  3. Read Energy per Good Kilogram in the dark results panel — that is the headline figure, expressed in kWh/kg.
  4. Check the supporting rows underneath (Energy per Kilogram Processed (the shortcut), Energy per Good Metre, Production-Related Energy per Good Kilogram, Site Energy at the Fuel Boundary, Energy Carried Out by Scrap, Site Energy That Made Nothing Saleable, Boiler House & Steam Main Loss and Compressed Air Share of the Electricity Meter) before acting on the headline — they are where an implausible input usually shows itself first.
  5. Reset to defaults returns every field to the reference case, which is the quickest way to check whether a surprising result came from the tool or from an input you had changed earlier.

Where this is used

  • Process planning — establishing Energy per Good Kilogram before a trial is booked, so machine time and material in Quality Systems, Traceability, Utilities & Factory Decisions are committed against a calculated figure rather than an estimate.
  • Costing and quotation — Energy per Good Kilogram is an input to the cost sheet, and quoting from a worked number rather than a remembered one is what keeps a margin intact.
  • Troubleshooting — when the floor result drifts from plan, entering the measured values (starting with Electricity Imported) shows how much of the gap in Energy per Good Kilogram each variable explains.
  • Teaching and study — the accepted ranges bracket normal Quality Systems, Traceability, Utilities & Factory Decisions practice, so moving one variable at a time shows the shape of the relationship rather than a single answer.

Reading the result

Typical bands and what each one is telling you.

ValueWhat it indicates
2 to 4 kWh per good kgSpinning or making-up site: almost all electrical, so the boiler terms are small and the air share of electricity is the number that matters.
4 to 7 kWh per good kgIntegrated dyeing and finishing at the fuel boundary. Thermal energy is three quarters of it, so a purely electrical improvement plan can only reach a quarter of the bill.
Above 9 kWh per good kgCheck the boundary before the plant: double-counted boiler fuel, a net-basis efficiency against a gross-basis gas bill, heavy shades at long liquor ratio, poor condensate return, or a month of low utilisation.
Good-to-gross gap above 5 per centRight-first-time is now the cheapest energy project on site. No burner, motor or inverter returns as much as the rework it removes.
Non-productive share above 15 per centStandby and scrap together. Look at the weekend base load and the trap survey before approving capital: this energy is being bought without any product attached to it.

Assumptions and limits

  • Allocation here is by mass at average intensity, which is a deliberate simplification with two known biases. Fabric rejected at final inspection carried the full process energy, while fabric pulled at grey inspection carried almost none, so a mass-weighted scrap charge is an upper bound when rejects are found early and an underestimate when they are found late; if your rejection point is known, weight the scrap by the fraction of the route it completed. Product mix cuts the same way, because a heavy navy at long liquor ratio can take twice the energy per kilogram of a pale continuous run, so mass allocation quietly subsidises the difficult product. The compressed air figure is a sub-meter of electricity and must never be added to the site total; the tool reports it as a share for exactly that reason. Direct-fired gas must exclude boiler fuel, which is reconstructed from the steam and efficiency figures instead. Boiler efficiency is intended as a boiler-house-to-process figure covering flue, blowdown, standing and distribution loss on the same calorific-value basis as the gas bill - a net-basis efficiency against a gross-basis bill overstates performance by about ten per cent for natural gas. Steam heat per tonne must match the working pressure and the real feedwater temperature; the 680 kWh/t default corresponds to saturated steam near 8 bar g from 85 deg C feedwater with no condensate return credit, and a site returning hot condensate should lower it. Standby energy is usually estimated rather than metered, read off the half-hourly profile floor, and it is the input most worth improving. The per-metre result is only meaningful for a single fabric construction, since it is simply the per-kilogram figure multiplied by mass per metre. Finally, this is a plant-boundary allocation tool and not a machine study: it will tell you how much of the site bill made nothing saleable, but it cannot tell you which machine spent it.
  • Every input is bounded to the range normal practice occupies (Electricity Imported 100 to 50000000 kWh, Direct-Fired Process Gas 0 to 50000000 kWh and Steam Delivered to Process 0 to 100000 t, and so on for the rest). Those bounds are guard rails against typing errors, not a claim that the formula fails one unit outside them.
  • The calculation is deterministic: the same inputs always give the same result. It carries no allowance for machine condition, operator skill, ambient conditions or lot-to-lot material variation unless an input above explicitly represents one.
  • Nothing is sent anywhere. The maths runs in your browser, so the numbers you type never leave the page.

Standards and further reading

  • ISO 50001:2018 - Energy management systems, requirements with guidance for use. Clause 6.4 requires energy performance indicators appropriate for measuring energy performance, clause 6.5 requires an energy baseline on the same basis, and clause 9.1.1 requires the two to remain comparable when they are monitored.
  • ISO 50006 - Evaluating energy performance using energy performance indicators and energy baselines. This is where the boundary, the relevant variable and the normalisation of a specific-energy figure against production are defined.
  • ISO 50015:2014 - Measurement and verification of energy performance of organizations, general principles and guidance, which governs how a claimed saving is proved against a baseline period rather than asserted from two monthly numbers.
  • EN 12953-11 for shell boiler acceptance tests and ISO 1217 for displacement compressor acceptance tests, including free air delivery and specific power. These give the boiler efficiency and compressed air figures entered here a measurable meaning rather than a nameplate one.

Questions people ask

Why is energy per good kilogram higher than energy per kilogram processed, and which one belongs in the ISO 50001 report?

The two differ by exactly the yield, because the numerator is identical and only the denominator changes. Every kilogram that was scoured, dyed, dried and finished before it failed inspection consumed the same energy as the kilogram beside it that shipped, so putting it in the denominator credits the plant for work it cannot sell. In the default case the shortcut reads 5.2484 kWh/kg and the honest figure 5.4658 kWh/kg. The reporting rule follows from ISO 50006: the denominator of an energy performance indicator has to be the relevant variable that actually drives the energy use and that the organisation is in business to produce. Quote the per-good-kilogram figure as the EnPI, keep the per-processed-kilogram figure as the process diagnostic, and put the gap between them on the quality report, because it closes only with right-first-time and never with a burner.

Our compressed air survey said air was twenty per cent of our energy. This tool says under five per cent. Which is right?

Both, and the difference is the denominator again. Air is 20.4206 per cent of the electricity meter and 4.48 per cent of site energy, because a wet processing plant is thermal-dominated: three quarters of what it buys arrives as fuel, not as electricity. An air survey that quotes a share of electricity is correct and useful, but it cannot be read as a share of the bill. There is a second trap in the same place. The compressors sit on the electricity meter already, so adding the air kWh to the site total counts them twice and inflates every specific-energy figure derived from it - which is why this tool reports air as a share and never as a sum. None of this makes leak repair a bad idea: compressed air is the most expensive energy vector on the site per useful joule delivered, and leaks are cheap to find. It just means the boiler-house loss of 102995.122 kWh, two and a third times larger, gets the engineer first.

Our kWh per kilogram rose nine per cent last month and nothing on the plant changed. What happened?

Utilisation, almost certainly. Site energy has a fixed part that runs whether or not fabric moves - effluent treatment, a banked boiler, standing losses in the steam mains, lighting, humidification, compressors idling on unload - and in the default case that is 78,000 kWh of 976,195 kWh. When production falls, the fixed part spreads over fewer kilograms and the specific figure rises with no loss of efficiency anywhere. This is why ISO 50006 asks for normalisation against relevant variables, and why a specific-energy figure quoted without the production figure beside it carries no information at all. The practical form is a regression of period energy on period production, E = a + b x P, where a is the standing load and b is the true marginal energy per kilogram; only b should be compared month to month. The production-related figure here, 5.0291 kWh/kg, strips the standby energy out and moves far less than the headline. Two other relevant variables bite in textiles: heating degree days, which change the steam mains and space-heating load, and product mix, since heavy shades at long liquor ratio can use twice the energy per kilogram of a pale continuous run.

How do we set the boundary for steam, purchased utilities and on-site generation without double counting?

Choose one accounting basis and hold it for every meter and every period. This tool works at the fuel boundary, meaning energy as it is bought: metered steam mass is valued in delivered heat and then divided by the boiler-house efficiency so the flue, blowdown, standing and distribution losses stay inside the site. That has a direct consequence for the gas field, which must exclude boiler fuel entirely, because the boiler fuel is already being reconstructed from the steam figure and entering it again counts it twice. If steam is bought over the fence, set the efficiency to 100 and enter the supplier delivered heat - their boiler loss belongs on their EnPI, not yours. Calorific value basis matters as much: gas is billed on gross calorific value in most countries while boiler efficiencies are often quoted on net, and mixing the two overstates efficiency by roughly ten per cent for natural gas, which is why ISO 6976 exists. On-site generation is counted at what it displaces - metered renewable or CHP electricity is real energy that did work, but it is not purchased energy, so record it explicitly rather than letting it hide in a falling import figure and be mistaken for an efficiency gain.

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