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Effluent Treatment

Dyehouse RO Recovery & Brine Reject Modeler (ZLD)

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See what it looks like

Raising recovery makes less brine and worse brine. The evaporator, not the membrane, is where that trade is settled.

RO Stage Membrane
m³/h
%
mg/L
%
ZLD & Costs Evaporator
kWh/m³
/kWh
/m³

Brine Reject Flow

— m³/h

Concentrate the ZLD stage has to deal with

Streams & Duty

Permeate Recovered
— m³/h
Permeate TDS
— mg/L
Brine TDS
— mg/L
Concentration Factor
— ×
Evaporator Load
— kW
Net Utility Cost
— /h

A negative net cost means the evaporator is spending more on energy than the recovered water is worth — which is often true, and is why ZLD is usually a discharge-compliance decision rather than a savings one. Watch the concentration factor against the saturation limits of the actual salts present; sulphate and silica scale long before sodium chloride does.

Using this calculator

About the Dyehouse RO Recovery & Brine Reject Modeler (ZLD)

The formula

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

Brine Reject Flow
brineFlow = f( feedFlow, recoveryRate, feedTds, saltRejection, evaporatorEnergy, energyCost, freshWaterCost )

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

Symbols used above
SymbolStands forUnit
feedFlowFeed Flowm³/h
recoveryRateRecovery Rate%
feedTdsFeed TDSmg/L
saltRejectionSalt Rejection%
evaporatorEnergyEvaporator Specific EnergykWh/m³
energyCostEnergy Cost/kWh
freshWaterCostFresh Water Cost/m³
brineFlowBrine Reject Flowm³/h
permeateFlowPermeate Recoveredm³/h
permeateTdsPermeate TDSmg/L
brineTdsBrine TDSmg/L
concentrationFactorConcentration Factor×
evaporatorLoadEvaporator LoadkW
netCostPerHourNet Utility Cost/h

How the result is derived

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

  1. The 7 inputs are read from the form on every keystroke: Feed Flow, Recovery Rate, Feed TDS, Salt Rejection, Evaporator Specific Energy, Energy Cost and Fresh Water 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 Brine Reject Flow together with every supporting figure in one pass — no value is carried over from a previous entry.
  4. The supporting outputs — Permeate Recovered, Permeate TDS, Brine TDS, Concentration Factor, Evaporator Load and Net Utility 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
Feed Flowm³/h0.5 to 2000 m³/h100
Recovery Rate%10 to 95 %75
Feed TDSmg/L100 to 50000 mg/L4500
Salt Rejection%80 to 99.9 %98
Evaporator Specific EnergykWh/m³1 to 200 kWh/m³25
Energy Cost/kWh0 to 5 /kWh0.09
Fresh Water Cost/m³0 to 20 /m³0.6

What the tool returns

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

OutputUnitWhat it tells you
Brine Reject Flow (headline result)m³/hConcentrate the ZLD stage has to deal with
Permeate Recoveredm³/h
Permeate TDSmg/L
Brine TDSmg/L
Concentration Factor×
Evaporator LoadkW
Net Utility Cost/h

Worked example

Given

Feed Flow
100 m³/h
Recovery Rate
75 %
Feed TDS
4500 mg/L
Salt Rejection
98 %
Evaporator Specific Energy
25 kWh/m³
Energy Cost
0.09 /kWh
Fresh Water Cost
0.6 /m³

The tool loads with this case already solved — the Brine Reject Flow 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 — RO Stage and ZLD & Costs. 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 Brine Reject Flow in the dark results panel — that is the headline figure, expressed in m³/h.
  4. Check the supporting rows underneath (Permeate Recovered, Permeate TDS, Brine TDS, Concentration Factor, Evaporator Load and Net Utility 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 Brine Reject Flow 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 — Brine Reject Flow 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 Feed Flow) shows how much of the gap in Brine Reject Flow 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

  • A negative net cost means the evaporator is spending more on energy than the recovered water is worth — which is often true, and is why ZLD is usually a discharge-compliance decision rather than a savings one. Watch the concentration factor against the saturation limits of the actual salts present; sulphate and silica scale long before sodium chloride does.
  • Every input is bounded to the range normal practice occupies (Feed Flow 0.5 to 2000 m³/h, Recovery Rate 10 to 95 % and Feed TDS 100 to 50000 mg/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 Dyehouse RO Recovery & Brine Reject Modeler (ZLD)?

Have these to hand: Feed Flow, Recovery Rate, Feed TDS, Salt Rejection, Evaporator Specific Energy, Energy Cost and Fresh Water Cost. With those entered, the tool returns Brine Reject Flow immediately.

What exactly is Brine Reject Flow?

Concentrate the ZLD stage has to deal with. It is reported in m³/h. It is derived from Feed Flow, Recovery Rate, Feed TDS, Salt Rejection, Evaporator Specific Energy, Energy Cost and Fresh Water Cost, and is the figure the rest of the Sustainability, ETP & Utilities calculation is built around.

Which units does this calculator expect?

Enter Feed Flow in m³/h, Recovery Rate in %, Feed TDS in mg/L, Salt Rejection in %, Evaporator Specific Energy in kWh/m³, Energy Cost in /kWh and Fresh Water Cost in /m³. 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: Permeate Recovered, Permeate TDS, Brine TDS, Concentration Factor, Evaporator Load and Net Utility 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?

A negative net cost means the evaporator is spending more on energy than the recovered water is worth — which is often true, and is why ZLD is usually a discharge-compliance decision rather than a savings one. Watch the concentration factor against the saturation limits of the actual salts present; sulphate and silica scale long before sodium chloride does. Treat the output as an engineering estimate that narrows the trial window, not as a substitute for the trial.

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