Reverse osmosis and reuse

Boron removal in seawater RO: pH and passes

Design boron control separately from conductivity in desalination. Review membrane choice, temperature, pH and full or partial second-pass treatment.

Published Updated

Define the boron duty at enquiry stage

State the seawater boron concentration and the maximum required concentration at the delivery point. Identify the use: industrial process, irrigation and drinking-water applications may need different assessments. Do not adopt a limit from another project or jurisdiction as an automatic specification for yours.

Request laboratory boron analysis with units and method, alongside salinity, alkalinity and temperature. Include the limiting operating temperature. Product quality must be checked for that condition rather than only for the cold feedwater present during a commissioning test or a favourable short pilot run.

Understand why pH matters

Boron can occur as uncharged boric acid or as borate. Raising pH increases the ionised fraction, which suitable membranes generally reject more effectively. This does not mean that any feedwater can safely be taken to a higher pH: precipitation risks and the operating limits of the complete assembly also change.

FilmTec documentation recognises improved rejection of weak-acid species at higher pH. Selection needs the actual element datasheet and a projection. Do not substitute overall sodium-chloride rejection for boron rejection or transfer a test percentage to conditions different from those of the test.

VariableWhy review itEvidence
pHChanges boron speciationProjection for each pass
TemperatureAffects output and rejectionDesign scenarios
BlendingSets final boron concentrationFlow and concentration balance

Compare full and partial second-pass arrangements

A second pass treats first-pass permeate; a second stage treats concentrate and is a different arrangement. It may be appropriate to treat all permeate or only a fraction, then blend streams if the final target is met. The balance must close both boron mass and water flow.

For an arithmetic example, equal volumes at 0.8 and 0.1 mg/L mix to 0.45 mg/L, assuming no reaction or other input. Those assumed concentrations are not equipment performance claims. The calculation helps determine the treatment fraction after the actual quality of each stream has been established.

Include final conditioning and system acceptance

Inter-pass pH adjustment may require subsequent correction and checks of alkalinity, corrosivity and distribution compatibility. Count chemicals, additional pumping, second-pass concentrate and recycle effects. The configuration should be evaluated against cost and usable water delivered at the agreed boundary.

Request boron acceptance criteria at specified temperature and salinity. Provide sampling points before and after blending, and define the response to deviations. A useful guarantee identifies the target constituent, feedwater envelope and exact supply boundary, rather than simply referring to a low-conductivity permeate stream.

Common questions

Are two stages equivalent to two passes for boron?

No. A further stage treats concentrate, while another pass treats permeate again. Their effects must be projected using the actual configuration.

Can conductivity alone control boron?

No. Conductivity is an overall ionic signal. Boron requires constituent-specific analysis at the defined acceptance points.

Sources and documentation

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