Introduction & Context

The concentration ratio (CR) quantifies how much a solute is enriched in the concentrate (reject) stream of a reverse-osmosis (RO) stage when the membrane is assumed to exhibit perfect rejection. In process engineering, this idealised metric is used to:

  • Size downstream ion-exchange or thermal brine concentrators.
  • Estimate osmotic pressure rise and scaling potential.
  • Set recovery limits before CaSO4, BaSO4, or silica precipitation occurs.

Because no real membrane rejects 100% of every species, the value obtained here is an upper-bound used for conservative design. The calculation is routinely embedded in HAZOP studies, process simulators, and membrane manufacturers’ projection software.

Methodology & Formulas

  1. Overall mass balance on water
    \[ Q_{\text{feed}} = Q_{\text{permeate}} + Q_{\text{concentrate}} \]
  2. Recovery fraction
    \[ R = \frac{Q_{\text{permeate}}}{Q_{\text{feed}}} \quad \text{(dimensionless)} \]
  3. Solute mass balance (ideal total rejection)
    Because the membrane passes no solute, every kilogram of salt entering in the feed exits in the concentrate: \[ Q_{\text{feed}}\,C_{\text{feed}} = Q_{\text{concentrate}}\,C_{\text{concentrate}} \] Re-arranging gives the concentrate concentration: \[ C_{\text{concentrate}} = C_{\text{feed}}\,\frac{Q_{\text{feed}}}{Q_{\text{concentrate}}} = C_{\text{feed}}\,\frac{1}{1 - R} \]
  4. Concentration ratio
    \[ \text{CR} = \frac{C_{\text{concentrate}}}{C_{\text{feed}}} = \frac{1}{1 - R} \]
Empirical operating limits for spiral-wound brackish-water elements
Parameter Threshold Consequence if exceeded
Recovery, \( R \) ≤ 0.45 High axial salinity gradient, increased scaling risk
Concentration factor, \( \text{CF} = 1/(1-R) \) ≤ 1.8 Excessive osmotic back-pressure, rapid fouling

The above limits are independent of feed salinity and are used as first-pass design rules before detailed geochemical modelling.