Water Engineering Verified Calculator

RO Permeate TDS Calculator

Project RO permeate product water TDS and salinity from feed water concentration and membrane salt rejection specifications.

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Water Quality Computation Engine • Verified

Stream Concentration & Rejection

Note: 1 mg/L ≈ 1 ppm for dilute aqueous solution density (ρ ≈ 1.0 kg/L).
mg/L
%
Example Presets:

Illustrative values only. Actual permeate salinity varies with feed composition, membrane age, recovery, and operating temperature.

Permeate Water Quality Output

Projected Permeate TDS (Cp) Product Salinity
10.00 mg/L
Feed TDS (Cf): 1000.00 mg/L
Specified Rejection (R): 99.00 %
Resulting Salt Passage (SP = 100 - R): 1.00 %

What is Permeate TDS Projection?

This calculator estimates expected Permeate Total Dissolved Solids (Cp) based on incoming raw feed salinity and manufacturer-specified or field-measured membrane rejection efficiency.

Governing Formula

Governing Formula
Cp = Cf × (1 - R / 100)

Where:

  • Cp = Projected Permeate product TDS / concentration [mg/L or ppm]
  • Cf = Feed water Total Dissolved Solids (TDS) [mg/L or ppm]
  • R = Specified membrane Salt Rejection percentage [%]

Derived Equations:

Permeate TDS: Cp = Cf × (1 - R / 100)
Corresponding Salt Passage: SP (%) = 100 - R (%)

Worked Engineering Example

Design Scenario: Feed TDS = 1000 mg/L & Rejection = 99%

  1. Cp = 1000 mg/L × (1 - 99 / 100) = 1000 × 0.01 = 10.00 mg/L

The estimated permeate stream salinity is 10.00 mg/L.

Engineering Notes & Limitation Warning

Engineering Note: This is a simplified estimate based on feed concentration and assumed salt rejection. Actual RO permeate quality depends on membrane characteristics, feed composition, pressure, temperature, recovery, concentration polarization, pretreatment, and operating conditions.

Real membrane permeate quality depends on raw feed ionic composition, operating temperature (salt passage increases roughly 3% per °C rise), system recovery, and concentration polarization (β).

Assumptions & Limitations

  • Calculates bulk TDS projection assuming average element rejection across the vessel.
  • For precise ion-by-ion projection, use full membrane projection software (DuPont WAVE, IMSDesign, Toray DS2).

Continue in the RO Engineering Workbench

Carry your feed TDS and membrane rejection into the RO Engineering Workbench, where they combine with feed flow, recovery, and temperature to resolve the full train balance — permeate quality, concentrate salinity, osmotic pressure, and scaling-risk screening in one saved project.

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Frequently Asked Questions

Why does permeate TDS increase as recovery increases?

As recovery increases, feed water salinity concentrates inside the pressure vessel, raising average membrane surface TDS (Cf,avg) and driving higher salt diffusion into permeate.

Engineering Disclaimer

Engineering Note: This calculator provides simplified engineering estimates for preliminary analysis and educational use. Actual RO system performance depends on membrane type, feedwater chemistry, temperature, pressure, recovery, concentration polarization, pretreatment, and operating conditions. Final system design should be verified using manufacturer data, validated design software, applicable standards, and qualified engineering review.

Technical References

  • DuPont FilmTec™ Reverse Osmosis and Nanofiltration Technical Manual (Form No. 45-D01504-en).
  • AWWA Manual M46: Reverse Osmosis and Nanofiltration, American Water Works Association.
Engineering Disclaimer & Verification Notice

This calculator provides preliminary engineering estimates for informational and planning purposes. Actual reverse osmosis / engineering system performance depends on site conditions, feed-water chemistry, membrane characteristics, operating pressure, temperature, recovery limits, fouling/scaling potential, and system design. Verify results using project-specific data, manufacturer projections, and applicable engineering standards before final design or operation.