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Engineering Tool · Membrane & Filtration

NF System Designer

Model nanofiltration mass balance with independent monovalent (salt) and divalent (hardness) rejection tracking across up to 3-stage arrays, plus a solver for the bypass blend needed to hit a target finished hardness.

Status
Live Engineering Tool
Conditions
Day 1 / aged
Array
Single / multistage
Units
Metric / Imperial
ATLAS WTS · Process Engineering

NF System Designer

Nanofiltration mass-balance with selective monovalent/divalent (hardness) rejection tracking, up to 3-stage arrays, membrane-aging projection, and product-water blending — including a solver for the bypass flow needed to hit a target finished hardness.

Cloud Engine
Project Information
Feed Water & Application

Pressure & Membrane Configuration

2- and 3-stage arrays feed each stage from the prior stage's concentrate, raising overall system recovery beyond what a single stage can reach — standard for hitting the 80-90% system recoveries common in NF softening.

Stage 1

ΔP guidance: ~0.2–0.3 bar (~3–4 psi) friction loss per element in series, ≈1.2–2.4 bar for a standard 6–8-element vessel — independent of how many vessels feed this stage in parallel.
Stage 2 Optional

ΔP guidance: ~0.2–0.3 bar/element in series, ≈1.2–2.4 bar for a standard 6–8-element vessel.

Re-pressurizes Stage 1's concentrate before it enters Stage 2, independent of the main feed pump — useful when this stage would otherwise run short on net driving pressure, especially at high recovery or aged-membrane conditions.

Stage 3 Optional

ΔP guidance: ~0.2–0.3 bar/element in series, ≈1.2–2.4 bar for a standard 6–8-element vessel.

Re-pressurizes Stage 2's concentrate before it enters Stage 3, independent of the main feed pump.

Membrane Aging Projection

Defaults follow the selected application type; edit for a specific project. The "Aged" condition (toggle top-right) projects permeate TDS/hardness and required feed pressure at end of the stated membrane age — both monovalent and divalent passage increase by the same compounding rate.

Product Water Blending (Bypass)

Raw/pretreated water blended directly into the final product stream — the standard NF softening lever for hitting a target finished hardness economically without over-designing rejection. Leave flow at 0 to disable.

Solve for Target Finished Hardness

Back-solves the bypass flow (at current membrane-train performance, using the on-screen Day-1/Aged condition) needed to blend the membrane permeate up to a target finished hardness. Only valid for a target strictly between the membrane's own permeate hardness and the raw feed hardness.

Overall System (Membrane Train + Blend)
Final Product Flow
—m³/h
Final Product TDS
—ppm
Final Product Hardness
—mg/L
Overall Hardness Removal
—%
Overall System Recovery
—%
of total raw intake incl. bypass
Waste (To Drain)
—m³/h
Membrane Train Performance
Train Recovery
—%
Total Permeate Flow
—m³/h
Final Concentrate Flow
—m³/h
Permeate TDS
—ppm
Permeate Hardness
—mg/L
Concentrate TDS
—ppm
Concentrate Hardness
—mg/L
Monovalent (TDS) Rejection
—%
Divalent (Hardness) Rejection
—%
Total Membrane Area
—m²
System Average Flux
—LMH
Stage-by-Stage Breakdown
Stage Elements Recovery NDP Osmotic P. Flux Mono. Rej. Div. Rej. Perm. Flow Perm. TDS Perm. Hardness Conc. TDS Conc. Hardness
Membrane Chemistry Reference (Informational)
Technical Warnings
No warnings — all parameters within the modeled envelope.

Powered by ATLAS WTS

01

Engineering Basis

Methodology

Mass-balance and flux calculations follow the standard recovery-based form (Qp = Qf·Y), with net driving pressure derived from feed pressure less concentrate-side losses and the log-mean average shell-side osmotic pressure across the stage.

Monovalent and divalent salt passage are each independently temperature- and flux-normalized against the membrane's bench test-condition baseline, reflecting nanofiltration's defining selective-rejection behavior rather than reverse osmosis's uniform total-salt rejection.

Standards / Reference Basis

NF 15–25 LMHVendor-neutral

Assumptions

  • Single- or multi-stage arrays use the existing 4-, 8-, and 16-inch element sizing options.
  • Day-1 / aged conditions and bypass blending remain part of the existing calculator model.

Scope / Limitations

  • Vendor-neutral loose/tight NF chemistry classes only; selective-rejection modeling, membrane aging, and bypass blending calibrated for well water, surface water, and scale-control softening duty.
02

Engineering Path

Application

Scenario

Workflow

  • High-purity water Quality-critical water planning for advanced manufacturing and related uses. Define the end-use basis first: semiconductor UPW, pharmaceutical PW/WFI, power or boiler makeup, and laboratory water are distinct duties.
    Stage 01 — PretreatmentReturn to Stage 01