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Engineering Tool · Membrane & Filtration

RO Membrane Performance Calculator

Model permeate flow, recovery ratio, and concentrate TDS across multi-stage RO arrays, with membrane fouling and osmotic pressure checks.

Seawater desalinationStage 05 Stage 08
Status
Live Engineering Tool
Conditions
Day 1 / aged
Array
Single / multistage
ATLAS WTS · Process Engineering

RO Membrane Performance Calculator

Reverse osmosis mass-balance, temperature correction, and salt-passage performance for single- or two-pass, up-to-3-stage concentrate-staged array configurations, with membrane-aging projection and product-water blending.

Local Engine
Project Information
Pass 1 — Feed Water & Process Conditions

Pass 1 — 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.

Pass 1 — 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.
Pass 1 — Stage 2

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.

Pass 1 — 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.

Pass 1 — Membrane Aging Projection

Defaults follow the selected feed water type; edit for a specific project. The "Aged" condition (toggle top-right) projects permeate TDS and required feed pressure at end of the stated membrane age — the design should stay within spec at BOTH Day-1 and Aged conditions.

Second Pass

Pass 2's feed is Pass 1's blended permeate, re-pressurized by an interstage pump (modeled as Pass 2's own feed pressure). Common for high-purity applications (boiler feed, semiconductor, pharma) and RO+EDI trains.

Product Water Blending

Optional raw/pretreated water blended directly into the final product stream to hit a target finished TDS without over-designing rejection. Leave flow at 0 to disable.

Overall System
Final Product Flow
—m³/h
Final Product TDS
—ppm
Overall System Recovery
—%
of raw feed, net of recycle boost
Waste (To Drain)
—m³/h
Pass 1 Performance
System Recovery
—%
Total Permeate Flow
—m³/h
Final Concentrate Flow
—m³/h
Blended Permeate TDS
—ppm
Final Concentrate TDS
—ppm
Overall Rejection
—%
Total Membrane Area
—m²
System Average Flux
—LMH
Pass 1 — Stage-by-Stage Breakdown
Stage Elements Recovery NDP Osmotic P. Flux Rejection Perm. Flow Conc. Flow Conc. TDS
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 feed osmotic pressure.

Salt passage is temperature- and flux-normalized against the element's bench test-condition baseline, with a concentration-polarization factor applied to estimate real membrane-wall salt passage.

Standards / Reference Basis

NSF/ANSI 58ASTM D4516

Scope / Limitations

  • For preliminary process evaluation only. It does not replace validated design software or review by a licensed process engineer.
02

Engineering Path

Application

Scenario

Workflow

  • Seawater desalination A membrane-led desalination train from intake and pretreatment through chemical conditioning, UF/MF where applicable, RO, conditioning, disinfection, and product water.
    Stage 05 — Reverse OsmosisReturn to Stage 05
    Stage 08 — Product & Concentrate BoundaryReturn to Stage 08
  • 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 02 — Reverse OsmosisReturn to Stage 02
  • Cooling water A systems route from makeup-water characterization through conditioning, cooling-system balance, blowdown, and reuse or discharge context.
    Stage 04 — BlowdownReturn to Stage 04