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Pad-Dry-Cure Thermal Load & Pick-Up Sensitivity

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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.

Line Fabric through the oven
g/m2
m
m/min
%

Liquor carried out of the mangle, on dry fabric weight

Temperatures What has to be heated, and to what
degC
degC
Thermal Constants & Cost Properties and plant efficiency
kJ/kg.K
kJ/kg

At atmospheric pressure. This term dominates everything

kJ/kg.K
%

Useful heat as a share of fuel energy, after exhaust and shell losses

cost/kWh

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 hour
water = 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 cloth
Q = 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 duty
fuel = Q / efficiency burner_kW = fuel / 3600

Dividing by oven efficiency is what turns a thermodynamic figure into a gas bill.

Symbols used above
SymbolStands forUnit
fabricGsmFabric GSMg/m2
fabricWidthWorking Widthm
lineSpeedLine Speedm/min
wetPickUpWet Pick-Up%
inletTempFabric Inlet TemperaturedegC
cureTempCure TemperaturedegC
waterSpecificHeatSpecific Heat of WaterkJ/kg.K
latentHeatLatent Heat of EvaporationkJ/kg
fabricSpecificHeatSpecific Heat of FabrickJ/kg.K
thermalEfficiencyOven Thermal Efficiency%
energyCostEnergy Costcost/kWh
burnerRatingBurner Duty RequiredkW
throughputFabric Throughputkg/h
waterLoadWater to Evaporatekg/h
sensibleWaterHeatHeating the WaterkJ/h
latentHeatBoiling the WaterkJ/h
sensibleFabricHeatHeating the ClothkJ/h
latentShareLatent Share of Useful Heat%
usefulHeatUseful HeatkJ/h
deliveredHeatFuel Energy RequiredkJ/h
specificEnergyEnergy per kg of FabrickJ/kg
energyPerKgWaterEnergy per kg of WaterkJ/kg
costPerHourEnergy Costcost/h
savingPer5PointsPickUpSaved by 5 Points Less Pick-Upcost/h

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: 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.
  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 Burner Duty Required together with every supporting figure in one pass — no value is carried over from a previous entry.
  4. 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.
  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
Fabric GSMg/m220 to 900 g/m2180
Working Widthm0.3 to 6 m1.8
Line Speedm/min1 to 200 m/min40
Wet Pick-Up%5 to 300 %65Liquor carried out of the mangle, on dry fabric weight
Fabric Inlet TemperaturedegC0 to 90 degC25
Cure TemperaturedegC80 to 230 degC170
Specific Heat of WaterkJ/kg.K4 to 4.3 kJ/kg.K4.186
Latent Heat of EvaporationkJ/kg2200 to 2400 kJ/kg2257At atmospheric pressure. This term dominates everything
Specific Heat of FabrickJ/kg.K0.8 to 2.5 kJ/kg.K1.34
Oven Thermal Efficiency%20 to 95 %62Useful heat as a share of fuel energy, after exhaust and shell losses
Energy Costcost/kWh0 to 5 cost/kWh0.075

What the tool returns

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

OutputUnitWhat it tells you
Burner Duty Required (headline result)kWFuel energy per hour, after oven efficiency
Fabric Throughputkg/h
Water to Evaporatekg/h
Heating the WaterkJ/h
Boiling the WaterkJ/h
Heating the ClothkJ/h
Latent Share of Useful Heat%
Useful HeatkJ/h
Fuel Energy RequiredkJ/h
Energy per kg of FabrickJ/kg
Energy per kg of WaterkJ/kg
Energy Costcost/h
Saved by 5 Points Less Pick-Upcost/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

  1. 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.
  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 Burner Duty Required in the dark results panel — that is the headline figure, expressed in kW.
  4. 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.
  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 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.

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