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Hydroextraction: G-Force, Residual Moisture & Drying Load

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Every point of residual moisture left in the load is bought again at the dryer, at about a kilowatt-hour per hundred kilos.

Extractor Basket, speed and duty
mm
rpm
kW
min
Load & Dryer Moisture in, moisture out, and the cost of the difference
kg
%
%
%
cur/kWh

Return on Extraction

— x

Drying energy avoided per unit of extractor energy

Force, Water & Energy

G-Force at the Basket Wall
— g
Water Entering the Extractor
— kg
Water Spun Out
— kg
Water Handed to the Dryer
— kg
Drying Energy Required
— kWh
Drying Cost for this Load
— cur
Drying Energy Avoided
— kWh
Extractor Electricity Used
— kWh
Net Energy Saved
— kWh
Energy per Point of Residual Moisture
— kWh
Cost per Point of Residual Moisture
— cur

Moisture is expressed on the dry mass, which is why a figure above one hundred per cent is ordinary rather than an error: a hundred kilos of dry cloth carrying a hundred and twenty per cent is holding a hundred and twenty kilos of water. The drying energy is latent heat alone, at 2257 kJ per kilogram, divided by a stated thermal efficiency. That makes it a floor and not a forecast: it counts nothing for heating the cloth and the machine to temperature, nothing for the air changes a dryer needs to carry vapour away, and nothing for the last few per cent of moisture, which comes out far more slowly than the first. A real dryer will use more than this figure and never less. Residual moisture is deliberately an input rather than something predicted from g-force and time, because that relationship depends on the fibre, the construction, the batch density and how the load sits in the basket, and no general curve for it belongs in a calculator. Measure it off the machine, or enter the figure the process is specified to. The g-force is geometry and holds regardless: it is the force at the basket wall, and cloth packed toward the centre sees less.

Using this calculator

About the Hydroextraction: G-Force, Residual Moisture & Drying Load

The formula

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

Force at the basket wall
RCF = 1.118e-5 x radius(cm) x rpm^2

A 1,200 mm basket at 700 rpm is about 329 g. Doubling the speed quadruples the force; doubling the diameter only doubles it.

What a kilogram of water costs to boil off
drying energy = water x 2257 / efficiency

At 65 per cent thermal efficiency a kilogram of water takes about 0.96 kWh, so 55 kg handed to the dryer is 53 kWh.

Why the machine exists
return = drying energy avoided / extractor energy used

Eleven kilowatts for eight minutes is 1.47 kWh, and it saves 62.7 kWh of drying. Forty-three to one, and it does not appear on either machine's specification.

Symbols used above
SymbolStands forUnit
drumDiameterBasket Diametermm
spinSpeedExtraction Speedrpm
extractorPowerMotor PowerkW
extractionTimeExtraction Timemin
dryLoadDry Mass of Loadkg
initialMoistureMoisture Before Extraction%
residualMoistureResidual Moisture After Extraction%
dryerEfficiencyDryer Thermal Efficiency%
energyPriceEnergy Pricecur/kWh
returnOnExtractionReturn on Extractionx
gForceG-Force at the Basket Wallg
waterIntoExtractorWater Entering the Extractorkg
waterRemovedWater Spun Outkg
waterToDryerWater Handed to the Dryerkg
dryingEnergyDrying Energy RequiredkWh
dryingCostDrying Cost for this Loadcur
dryingAvoidedDrying Energy AvoidedkWh
extractorEnergyExtractor Electricity UsedkWh
netEnergySavedNet Energy SavedkWh
energyPerMoisturePointEnergy per Point of Residual MoisturekWh
costPerMoisturePointCost per Point of Residual Moisturecur

How the result is derived

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

  1. The 9 inputs are read from the form on every keystroke: Basket Diameter, Extraction Speed, Motor Power, Extraction Time, Dry Mass of Load, Moisture Before Extraction, Residual Moisture After Extraction, Dryer Thermal Efficiency and Energy Price.
  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 Return on Extraction together with every supporting figure in one pass — no value is carried over from a previous entry.
  4. The supporting outputs — G-Force at the Basket Wall, Water Entering the Extractor, Water Spun Out, Water Handed to the Dryer, Drying Energy Required, Drying Cost for this Load, Drying Energy Avoided, Extractor Electricity Used, Net Energy Saved, Energy per Point of Residual Moisture and Cost per Point of Residual Moisture — 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
Basket Diametermm200 to 2000 mm1200
Extraction Speedrpm100 to 2000 rpm700
Motor PowerkW0.5 to 60 kW11
Extraction Timemin1 to 40 min8
Dry Mass of Loadkg1 to 500 kg100
Moisture Before Extraction%20 to 300 %120
Residual Moisture After Extraction%5 to 200 %55
Dryer Thermal Efficiency%20 to 95 %65
Energy Pricecur/kWh0.01 to 1 cur/kWh0.09

What the tool returns

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

OutputUnitWhat it tells you
Return on Extraction (headline result)xDrying energy avoided per unit of extractor energy
G-Force at the Basket Wallg
Water Entering the Extractorkg
Water Spun Outkg
Water Handed to the Dryerkg
Drying Energy RequiredkWh
Drying Cost for this Loadcur
Drying Energy AvoidedkWh
Extractor Electricity UsedkWh
Net Energy SavedkWh
Energy per Point of Residual MoisturekWh
Cost per Point of Residual Moisturecur

Worked example

Given

Basket Diameter
1200 mm
Extraction Speed
700 rpm
Motor Power
11 kW
Extraction Time
8 min
Dry Mass of Load
100 kg
Moisture Before Extraction
120 %
Residual Moisture After Extraction
55 %
Dryer Thermal Efficiency
65 %
Energy Price
0.09 cur/kWh

The tool loads with this case already solved — the Return on Extraction 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 — Extractor and Load & Dryer. 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 Return on Extraction in the dark results panel — that is the headline figure, expressed in x.
  4. Check the supporting rows underneath (G-Force at the Basket Wall, Water Entering the Extractor, Water Spun Out, Water Handed to the Dryer, Drying Energy Required, Drying Cost for this Load, Drying Energy Avoided, Extractor Electricity Used, Net Energy Saved, Energy per Point of Residual Moisture and Cost per Point of Residual Moisture) 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 Return on Extraction before a trial is booked, so machine time and material in Sustainability, ETP & Utilities are committed against a calculated figure rather than an estimate.
  • Costing and quotation — Return on Extraction 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 Basket Diameter) shows how much of the gap in Return on Extraction each variable explains.
  • Teaching and study — the accepted ranges bracket normal Sustainability, ETP & Utilities practice, so moving one variable at a time shows the shape of the relationship rather than a single answer.

Assumptions and limits

  • Moisture is expressed on the dry mass, which is why a figure above one hundred per cent is ordinary rather than an error: a hundred kilos of dry cloth carrying a hundred and twenty per cent is holding a hundred and twenty kilos of water. The drying energy is latent heat alone, at 2257 kJ per kilogram, divided by a stated thermal efficiency. That makes it a floor and not a forecast: it counts nothing for heating the cloth and the machine to temperature, nothing for the air changes a dryer needs to carry vapour away, and nothing for the last few per cent of moisture, which comes out far more slowly than the first. A real dryer will use more than this figure and never less. Residual moisture is deliberately an input rather than something predicted from g-force and time, because that relationship depends on the fibre, the construction, the batch density and how the load sits in the basket, and no general curve for it belongs in a calculator. Measure it off the machine, or enter the figure the process is specified to. The g-force is geometry and holds regardless: it is the force at the basket wall, and cloth packed toward the centre sees less.
  • Every input is bounded to the range normal practice occupies (Basket Diameter 200 to 2000 mm, Extraction Speed 100 to 2000 rpm and Motor Power 0.5 to 60 kW, 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 Hydroextraction: G-Force, Residual Moisture & Drying Load?

Have these to hand: Basket Diameter, Extraction Speed, Motor Power, Extraction Time, Dry Mass of Load, Moisture Before Extraction, Residual Moisture After Extraction, Dryer Thermal Efficiency and Energy Price. With those entered, the tool returns Return on Extraction immediately.

What exactly is Return on Extraction?

Drying energy avoided per unit of extractor energy. It is reported in x. It is derived from Basket Diameter, Extraction Speed, Motor Power, Extraction Time, Dry Mass of Load, Moisture Before Extraction, Residual Moisture After Extraction, Dryer Thermal Efficiency and Energy Price, and is the figure the rest of the Sustainability, ETP & Utilities calculation is built around.

Which units does this calculator expect?

Enter Basket Diameter in mm, Extraction Speed in rpm, Motor Power in kW, Extraction Time in min, Dry Mass of Load in kg, Moisture Before Extraction in %, Residual Moisture After Extraction in %, Dryer Thermal Efficiency in % and Energy Price in cur/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: G-Force at the Basket Wall, Water Entering the Extractor, Water Spun Out, Water Handed to the Dryer, Drying Energy Required, Drying Cost for this Load, Drying Energy Avoided, Extractor Electricity Used, Net Energy Saved, Energy per Point of Residual Moisture and Cost per Point of Residual Moisture. 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?

Moisture is expressed on the dry mass, which is why a figure above one hundred per cent is ordinary rather than an error: a hundred kilos of dry cloth carrying a hundred and twenty per cent is holding a hundred and twenty kilos of water. The drying energy is latent heat alone, at 2257 kJ per kilogram, divided by a stated thermal efficiency. That makes it a floor and not a forecast: it counts nothing for heating the cloth and the machine to temperature, nothing for the air changes a dryer needs to carry vapour away, and nothing for the last few per cent of moisture, which comes out far more slowly than the first. A real dryer will use more than this figure and never less. Residual moisture is deliberately an input rather than something predicted from g-force and time, because that relationship depends on the fibre, the construction, the batch density and how the load sits in the basket, and no general curve for it belongs in a calculator. Measure it off the machine, or enter the figure the process is specified to. The g-force is geometry and holds regardless: it is the force at the basket wall, and cloth packed toward the centre sees less. Treat the output as an engineering estimate that narrows the trial window, not as a substitute for the trial.

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