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Caustic Soda Recovery Plant Efficiency & Payback Modeler

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See what it looks like

Recovering caustic is really an exercise in boiling water. Whether it pays depends on the steam price, not the caustic price.

Weak Lye From the range
m³/h
% NaOH
kg/L
Recovery Plant Evaporator
% NaOH
%
kg/kg

Multi-effect evaporators reach 0.3–0.4; single effect is above 1.

Economics Prices
/kg
/tonne

Net Saving

— /h

Caustic recovered less the steam spent recovering it

Recovery Balance

Caustic Recovered
— kg/h
Strong Lye Produced
— kg/h
Water Evaporated
— kg/h
Steam Required
— kg/h
Value of Caustic Recovered
— /h
Steam Cost
— /h

Recovered lye carries the dyes, sizes and impurities picked up on the range, so a mercerising plant cannot usually return it to full-strength duty without purification. Caustic is severely corrosive and the recovery loop runs hot — this sizes a process, not a safety case.

Using this calculator

About the Caustic Soda Recovery Plant Efficiency & Payback Modeler

The formula

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

Net Saving
netSaving = f( weakLyeFlow, weakLyeConc, lyeDensity, recoveredConc, recoveryEfficiency, steamRatio, causticPrice, steamCost )

Each input feeds the expression evaluated in the browser; the symbol table below names every term and its unit.

Symbols used above
SymbolStands forUnit
weakLyeFlowWeak Lye Flowm³/h
weakLyeConcWeak Lye Concentration% NaOH
lyeDensityWeak Lye Densitykg/L
recoveredConcRecovered Lye Concentration% NaOH
recoveryEfficiencyNaOH Recovery Efficiency%
steamRatioSteam per kg Water Evaporatedkg/kg
causticPriceCaustic Soda Price/kg
steamCostSteam Cost/tonne
netSavingNet Saving/h
naohRecoveredCaustic Recoveredkg/h
recoveredLyeMassStrong Lye Producedkg/h
waterEvaporatedWater Evaporatedkg/h
steamRequiredSteam Requiredkg/h
causticValueValue of Caustic Recovered/h
steamCostPerHourSteam Cost/h

How the result is derived

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

  1. The 8 inputs are read from the form on every keystroke: Weak Lye Flow, Weak Lye Concentration, Weak Lye Density, Recovered Lye Concentration, NaOH Recovery Efficiency, Steam per kg Water Evaporated, Caustic Soda Price and Steam 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 Net Saving together with every supporting figure in one pass — no value is carried over from a previous entry.
  4. The supporting outputs — Caustic Recovered, Strong Lye Produced, Water Evaporated, Steam Required, Value of Caustic Recovered and Steam Cost — 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
Weak Lye Flowm³/h0.1 to 200 m³/h12
Weak Lye Concentration% NaOH0.5 to 20 % NaOH6
Weak Lye Densitykg/L1 to 1.6 kg/L1.07
Recovered Lye Concentration% NaOH10 to 55 % NaOH30
NaOH Recovery Efficiency%40 to 100 %92
Steam per kg Water Evaporatedkg/kg0.1 to 1.5 kg/kg0.35Multi-effect evaporators reach 0.3–0.4; single effect is above 1.
Caustic Soda Price/kg0.01 to 10 /kg0.45
Steam Cost/tonne1 to 200 /tonne25

What the tool returns

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

OutputUnitWhat it tells you
Net Saving (headline result)/hCaustic recovered less the steam spent recovering it
Caustic Recoveredkg/h
Strong Lye Producedkg/h
Water Evaporatedkg/h
Steam Requiredkg/h
Value of Caustic Recovered/h
Steam Cost/h

Worked example

Given

Weak Lye Flow
12 m³/h
Weak Lye Concentration
6 % NaOH
Weak Lye Density
1.07 kg/L
Recovered Lye Concentration
30 % NaOH
NaOH Recovery Efficiency
92 %
Steam per kg Water Evaporated
0.35 kg/kg
Caustic Soda Price
0.45 /kg
Steam Cost
25 /tonne

The tool loads with this case already solved — the Net Saving 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 — Weak Lye, Recovery Plant and Economics. 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 Net Saving in the dark results panel — that is the headline figure, expressed in /h.
  4. Check the supporting rows underneath (Caustic Recovered, Strong Lye Produced, Water Evaporated, Steam Required, Value of Caustic Recovered and Steam Cost) 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 Net Saving 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 — Net Saving 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 Weak Lye Flow) shows how much of the gap in Net Saving 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

  • Recovered lye carries the dyes, sizes and impurities picked up on the range, so a mercerising plant cannot usually return it to full-strength duty without purification. Caustic is severely corrosive and the recovery loop runs hot — this sizes a process, not a safety case.
  • Every input is bounded to the range normal practice occupies (Weak Lye Flow 0.1 to 200 m³/h, Weak Lye Concentration 0.5 to 20 % NaOH and Weak Lye Density 1 to 1.6 kg/L, 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 Caustic Soda Recovery Plant Efficiency & Payback Modeler?

Have these to hand: Weak Lye Flow, Weak Lye Concentration, Weak Lye Density, Recovered Lye Concentration, NaOH Recovery Efficiency, Steam per kg Water Evaporated, Caustic Soda Price and Steam Cost. With those entered, the tool returns Net Saving immediately.

What exactly is Net Saving?

Caustic recovered less the steam spent recovering it. It is reported in /h. It is derived from Weak Lye Flow, Weak Lye Concentration, Weak Lye Density, Recovered Lye Concentration, NaOH Recovery Efficiency, Steam per kg Water Evaporated, Caustic Soda Price and Steam Cost, and is the figure the rest of the Sustainability, ETP & Utilities calculation is built around.

Which units does this calculator expect?

Enter Weak Lye Flow in m³/h, Weak Lye Concentration in % NaOH, Weak Lye Density in kg/L, Recovered Lye Concentration in % NaOH, NaOH Recovery Efficiency in %, Steam per kg Water Evaporated in kg/kg, Caustic Soda Price in /kg and Steam Cost in /tonne. 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: Caustic Recovered, Strong Lye Produced, Water Evaporated, Steam Required, Value of Caustic Recovered and Steam Cost. 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?

Recovered lye carries the dyes, sizes and impurities picked up on the range, so a mercerising plant cannot usually return it to full-strength duty without purification. Caustic is severely corrosive and the recovery loop runs hot — this sizes a process, not a safety case. Treat the output as an engineering estimate that narrows the trial window, not as a substitute for the trial.

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