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Latent heat is four fifths of the bill. The cheapest drying is the water squeezed out at the pad and never boiled.
Burner Duty Required
—kW
Fuel energy per hour, after oven efficiency
Heat Balance
Fabric Throughput
—kg/h
Water to Evaporate
—kg/h
Heating the Water
—kJ/h
Boiling the Water
—kJ/h
Heating the Cloth
—kJ/h
Latent Share of Useful Heat
—%
Useful Heat
—kJ/h
Fuel Energy Required
—kJ/h
Energy per kg of Fabric
—kJ/kg
Energy per kg of Water
—kJ/kg
Energy Cost
—cost/h
Saved by 5 Points Less Pick-Up
—cost/h
The balance is steady-state and counts only what leaves in the fabric and the vapour; it does not model the air actually moved through the oven, which is where a badly set exhaust throws away far more than any of these terms. Energy per kilogram of water is the number to benchmark against, and a well-run stenter sits near 3,000 to 3,500 kJ per kilogram evaporated - a figure well above that points at exhaust humidity rather than at anything in this calculation, because an oven exhausting drier air than it needs to is heating fresh air for no purpose. Oven efficiency is therefore doing a great deal of work as a single input and should be measured rather than assumed. Cure is treated as a temperature to reach rather than a time to hold, so a resin needing dwell at temperature will need a longer oven than the heat balance alone suggests. The pick-up sensitivity assumes the same efficiency at the lower loading, which is slightly conservative: a stenter with less water to remove usually runs at a better exhaust setting as well, so the real saving tends to exceed the figure shown.
Using this calculator
About the Pad-Dry-Cure Thermal Load & Pick-Up Sensitivity
The formula
This is the expression the tool evaluates. Every term is named underneath, with the unit it must be supplied in.
Water arriving at the oven every hourwater = gsm x width x speed x 60 / 1000 x pickUp / 100
Wet pick-up is on dry fabric weight, so the water load is the throughput scaled by it directly.
Sensible water, latent, sensible clothQ = m_w x cw x (100 - Tin) + m_w x L + m_f x cf x (Tcure - Tin)
The latent term uses 2,257 kJ/kg and swamps the other two: at 65 percent pick-up it is close to four fifths of the useful heat.
From useful heat to fuel and dutyfuel = Q / efficiency burner_kW = fuel / 3600
Dividing by oven efficiency is what turns a thermodynamic figure into a gas bill.
Symbols used above
Symbol
Stands for
Unit
fabricGsm
Fabric GSM
g/m2
fabricWidth
Working Width
m
lineSpeed
Line Speed
m/min
wetPickUp
Wet Pick-Up
%
inletTemp
Fabric Inlet Temperature
degC
cureTemp
Cure Temperature
degC
waterSpecificHeat
Specific Heat of Water
kJ/kg.K
latentHeat
Latent Heat of Evaporation
kJ/kg
fabricSpecificHeat
Specific Heat of Fabric
kJ/kg.K
thermalEfficiency
Oven Thermal Efficiency
%
energyCost
Energy Cost
cost/kWh
burnerRating
Burner Duty Required
kW
throughput
Fabric Throughput
kg/h
waterLoad
Water to Evaporate
kg/h
sensibleWaterHeat
Heating the Water
kJ/h
latentHeat
Boiling the Water
kJ/h
sensibleFabricHeat
Heating the Cloth
kJ/h
latentShare
Latent Share of Useful Heat
%
usefulHeat
Useful Heat
kJ/h
deliveredHeat
Fuel Energy Required
kJ/h
specificEnergy
Energy per kg of Fabric
kJ/kg
energyPerKgWater
Energy per kg of Water
kJ/kg
costPerHour
Energy Cost
cost/h
savingPer5PointsPickUp
Saved by 5 Points Less Pick-Up
cost/h
How the result is derived
Step by step, from the values you type to the figure on screen.
The 11 inputs are read from the form on every keystroke: Fabric GSM, Working Width, Line Speed, Wet Pick-Up, Fabric Inlet Temperature, Cure Temperature, Specific Heat of Water, Latent Heat of Evaporation, Specific Heat of Fabric, Oven Thermal Efficiency and Energy Cost.
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.
The validated values are substituted into the expression above, which resolves Burner Duty Required together with every supporting figure in one pass — no value is carried over from a previous entry.
The supporting outputs — Fabric Throughput, Water to Evaporate, Heating the Water, Boiling the Water, Heating the Cloth, Latent Share of Useful Heat, Useful Heat, Fuel Energy Required, Energy per kg of Fabric, Energy per kg of Water, Energy Cost and Saved by 5 Points Less Pick-Up — come from the same pass, so they always describe the same case as the headline figure.
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.
Input
Unit
Accepted range
Default
What it means
Fabric GSM
g/m2
20 to 900 g/m2
180
Working Width
m
0.3 to 6 m
1.8
Line Speed
m/min
1 to 200 m/min
40
Wet Pick-Up
%
5 to 300 %
65
Liquor carried out of the mangle, on dry fabric weight
Fabric Inlet Temperature
degC
0 to 90 degC
25
Cure Temperature
degC
80 to 230 degC
170
Specific Heat of Water
kJ/kg.K
4 to 4.3 kJ/kg.K
4.186
Latent Heat of Evaporation
kJ/kg
2200 to 2400 kJ/kg
2257
At atmospheric pressure. This term dominates everything
Specific Heat of Fabric
kJ/kg.K
0.8 to 2.5 kJ/kg.K
1.34
Oven Thermal Efficiency
%
20 to 95 %
62
Useful heat as a share of fuel energy, after exhaust and shell losses
Energy Cost
cost/kWh
0 to 5 cost/kWh
0.075
What the tool returns
The headline figure and every supporting value it is built from.
Output
Unit
What it tells you
Burner Duty Required (headline result)
kW
Fuel energy per hour, after oven efficiency
Fabric Throughput
kg/h
Water to Evaporate
kg/h
Heating the Water
kJ/h
Boiling the Water
kJ/h
Heating the Cloth
kJ/h
Latent Share of Useful Heat
%
Useful Heat
kJ/h
Fuel Energy Required
kJ/h
Energy per kg of Fabric
kJ/kg
Energy per kg of Water
kJ/kg
Energy Cost
cost/h
Saved by 5 Points Less Pick-Up
cost/h
Worked example
Given
Fabric GSM
180 g/m2
Working Width
1.8 m
Line Speed
40 m/min
Wet Pick-Up
65 %
Fabric Inlet Temperature
25 degC
Cure Temperature
170 degC
Specific Heat of Water
4.186 kJ/kg.K
Latent Heat of Evaporation
2257 kJ/kg
Specific Heat of Fabric
1.34 kJ/kg.K
Oven Thermal Efficiency
62 %
Energy Cost
0.075 cost/kWh
The tool loads with this case already solved — the Burner Duty Required shown above is its answer. Change one value and the difference from this baseline is the sensitivity of the result to that variable.
How to use it
Work through the input groups in order — Line, Temperatures and Thermal Constants & Cost. The defaults are a realistic case, so you can change one value at a time and watch what moves.
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.
Read Burner Duty Required in the dark results panel — that is the headline figure, expressed in kW.
Check the supporting rows underneath (Fabric Throughput, Water to Evaporate, Heating the Water, Boiling the Water, Heating the Cloth, Latent Share of Useful Heat, Useful Heat, Fuel Energy Required, Energy per kg of Fabric, Energy per kg of Water, Energy Cost and Saved by 5 Points Less Pick-Up) before acting on the headline — they are where an implausible input usually shows itself first.
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 Burner Duty Required before a trial is booked, so machine time and material in Finishing, Coating, Lamination & Functional Performance are committed against a calculated figure rather than an estimate.
Costing and quotation — Burner Duty Required 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 Fabric GSM) shows how much of the gap in Burner Duty Required each variable explains.
Teaching and study — the accepted ranges bracket normal Finishing, Coating, Lamination & Functional Performance practice, so moving one variable at a time shows the shape of the relationship rather than a single answer.
Assumptions and limits
The balance is steady-state and counts only what leaves in the fabric and the vapour; it does not model the air actually moved through the oven, which is where a badly set exhaust throws away far more than any of these terms. Energy per kilogram of water is the number to benchmark against, and a well-run stenter sits near 3,000 to 3,500 kJ per kilogram evaporated - a figure well above that points at exhaust humidity rather than at anything in this calculation, because an oven exhausting drier air than it needs to is heating fresh air for no purpose. Oven efficiency is therefore doing a great deal of work as a single input and should be measured rather than assumed. Cure is treated as a temperature to reach rather than a time to hold, so a resin needing dwell at temperature will need a longer oven than the heat balance alone suggests. The pick-up sensitivity assumes the same efficiency at the lower loading, which is slightly conservative: a stenter with less water to remove usually runs at a better exhaust setting as well, so the real saving tends to exceed the figure shown.
Every input is bounded to the range normal practice occupies (Fabric GSM 20 to 900 g/m2, Working Width 0.3 to 6 m and Line Speed 1 to 200 m/min, 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.
Questions people ask
What do I need to know before using the Pad-Dry-Cure Thermal Load & Pick-Up Sensitivity?
Have these to hand: Fabric GSM, Working Width, Line Speed, Wet Pick-Up, Fabric Inlet Temperature, Cure Temperature, Specific Heat of Water, Latent Heat of Evaporation, Specific Heat of Fabric, Oven Thermal Efficiency and Energy Cost. With those entered, the tool returns Burner Duty Required immediately.
What exactly is Burner Duty Required?
Fuel energy per hour, after oven efficiency. It is reported in kW. It is derived from Fabric GSM, Working Width, Line Speed, Wet Pick-Up, Fabric Inlet Temperature, Cure Temperature, Specific Heat of Water, Latent Heat of Evaporation, Specific Heat of Fabric, Oven Thermal Efficiency and Energy Cost, and is the figure the rest of the Finishing, Coating, Lamination & Functional Performance calculation is built around.
Which units does this calculator expect?
Enter Fabric GSM in g/m2, Working Width in m, Line Speed in m/min, Wet Pick-Up in %, Fabric Inlet Temperature in degC, Cure Temperature in degC, Specific Heat of Water in kJ/kg.K, Latent Heat of Evaporation in kJ/kg, Specific Heat of Fabric in kJ/kg.K, Oven Thermal Efficiency in % and Energy Cost in cost/kWh. Mixing unit systems is the most common cause of a result that looks an order of magnitude wrong — convert before typing, not after reading.
What are the other figures under the main result?
They are the intermediate quantities the calculation passes through: Fabric Throughput, Water to Evaporate, Heating the Water, Boiling the Water, Heating the Cloth, Latent Share of Useful Heat, Useful Heat, Fuel Energy Required, Energy per kg of Fabric, Energy per kg of Water, Energy Cost and Saved by 5 Points Less Pick-Up. They are shown because a headline number nobody can trace is a number nobody trusts — checking them against your own expectation is the fastest way to confirm the inputs were read as you intended.
Can I rely on this for a production decision?
The balance is steady-state and counts only what leaves in the fabric and the vapour; it does not model the air actually moved through the oven, which is where a badly set exhaust throws away far more than any of these terms. Energy per kilogram of water is the number to benchmark against, and a well-run stenter sits near 3,000 to 3,500 kJ per kilogram evaporated - a figure well above that points at exhaust humidity rather than at anything in this calculation, because an oven exhausting drier air than it needs to is heating fresh air for no purpose. Oven efficiency is therefore doing a great deal of work as a single input and should be measured rather than assumed. Cure is treated as a temperature to reach rather than a time to hold, so a resin needing dwell at temperature will need a longer oven than the heat balance alone suggests. The pick-up sensitivity assumes the same efficiency at the lower loading, which is slightly conservative: a stenter with less water to remove usually runs at a better exhaust setting as well, so the real saving tends to exceed the figure shown. Treat the output as an engineering estimate that narrows the trial window, not as a substitute for the trial.