Reverse osmosis and reuse

RO dechlorination: activated carbon or bisulfite

Compare activated carbon and bisulfite ahead of reverse osmosis, including chlorine species, mixing, monitoring and protective actions.

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Identify the oxidant entering the plant

A water report labelled simply “chlorine” leaves an important gap. Free chlorine and combined chlorine, including chloramines, need separate consideration. Request both measurements, the analytical method and any changes made by the water supplier or upstream process. A low free-chlorine reading does not demonstrate the absence of combined chlorine.

The FilmTec manual distinguishes these species and recommends dechlorination before incompatible agents reach its membranes. Do not treat a published ppm-hour tolerance as permission to run with a residual: temperature, pH, metals and the particular element also matter. An upstream disinfection cycle or restart can create a very different exposure from normal operation.

Activated carbon: provide contact and maintain the bed

Carbon provides a barrier without continuous reducing-agent dosing and may remove some specific organic compounds. Selection needs the media type, maximum flow, contact time, pressure loss and treatment target for each oxidant. A design established for free chlorine should not automatically be carried over to chloramines.

Include backwashing, replacement, sampling and microbiological management. A bed that removes disinfectant can also encourage biological growth downstream. New media require a verified rinse because carbon fines can foul RO. A downstream cartridge is not a substitute for confirming that fines have been removed.

Ask the supplier to define the end-of-service condition and how oxidant breakthrough will be detected. A large vessel without a design basis and monitoring plan does not demonstrate protection throughout its operating cycle.

Bisulfite: verify delivery, mixing and treatment

Chemical reduction can fit a compact treatment line. Pump and tank selection need flow, maximum demand, commercial solution strength, residual variability and storage conditions. Metabisulfite forms bisulfite when dissolved; check product identity and concentration before using either name in a dosing calculation.

A running dosing pump does not prove that effective reagent reaches the water. An empty tank, blocked valve, suction air or deteriorated solution can allow oxidant through. Confirm mixing, measurement location and response to changing flow. Permanent overdosing is a poor substitute for effective mixing and reliable delivery.

Excess reducer adds chemical load and may affect process conditions. Establish the setting with representative feed and the membrane supplier rather than adopting a universal recipe from another plant.

IssueActivated carbonChemical reducer
Key design basisMedia and contact at design flowDemand, effective delivery and mixing
MaintenanceBackwashing, renewal and bed managementPreparation, storage and calibration
Failure to detectBreakthrough or channelingDosing loss or ineffective solution
Shared verificationResidual before ROResidual before RO

Specify protective actions as well as an analyser

Locate monitoring where it represents the actual RO feed, downstream of treatment and adequate mixing. Specify the method, detection limit, maintenance and response time. Oxidation-reduction potential, ORP, is an indirect signal affected by water chemistry; a setpoint from another plant is not a universal chlorine concentration.

Engineering must define the response to a high residual, instrument failure, depleted reagent or lost sample flow: alarm, inhibition, diversion and restart conditions. Check whether detection and action fit within the available hydraulic travel time. An alarm that arrives after the oxidant provides little protection. Include sampling lines when assessing this delay.

Compare protection over the full operating cycle

Compare capital, footprint, backwash water, chemicals, labour, instruments and failure consequences at the same availability target. For intermittent duty, include the first water after shutdown and upstream sanitisation, rather than assessing only steady operation. Record who maintains the protection system and how the result reaches the plant operator.

Commissioning should verify low, normal and peak flow, together with reasonably foreseeable residual changes. This gives both alternatives a measurable purchase criterion: compatible feed reaching the membrane, with a demonstrated response when that condition is lost. Preserve the commissioning results as the reference for future maintenance and changes to the water supply.

Common questions

Will a cartridge filter remove chlorine?

A conventional particulate cartridge is not a dechlorination stage. That function requires a specifically selected and verified media or treatment process.

Can CIP repair an oxidised membrane?

Cleaning can remove deposits, but it cannot restore the chemical structure of an oxidation-damaged membrane. Investigate the cause before replacing elements.

Sources and documentation

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