Industry best practice manual for water quality management and sterilisation on-farm

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Pre-treatment issues: reverse osmosis

Table 33. Troubleshooting reverse osmosis (RO) issues

Probable causesPreventive measuresChecking preventive measuresCorrective action
What to checkSigns that action is needed
Observation: Low product water or accelerated differential pressure build-up due to turbidity

Possible hazards: Increases scale build-up
Excessive turbidity to the unit.Check filters are working optimally
Increase the efficacy of pre-treatment
Regular membrane cleaning (usually RO units have an automatic cleaning)
Turbidity and colour of effluent from filtration system (i.e. going into RO unit)High turbidity and colour inlet water
Membrane fouling
Pressure increase
Turbidity should be limited to below 1 NTU to RO unit.
Filter media breakthrough or cartridge filter failureMonitor water quality going to RO unit
Add additional pre-treatments
Increase the efficacy of pre-treatment
Turbidity and colour of effluent from the filtration system. (i.e. going into RO unit)High turbidity and colour inlet water
Membrane fouling
Pressure increase
Correct filtration problems
Inadequate cleaning of the membraneIncrease frequency of membrane cleaning to a rate that resolves the problemCleaning cycle (initiated when the flux is ± 15% of rated value)Membrane fouling
Pressure increase
Initiate more frequent cleaning of the membrane
Fine suspended solids on the face of membrane and feed concentrate mesh spacerAdd additional pre-treatments
Increase the efficacy of pre-treatment
Turbidity and colour of effluent from the filtration system. (i.e. going into RO unit)
Perform silt density index (SDI) and modified fouling index (MFI)—these should be between 0 and 2.
High turbidity and colour inlet water
Membrane fouling
Pressure increase
The system will require a higher level of turbidity removal
Observation: Low product water or accelerated differential pressure build-up due to minerals.

Possible hazards: Increases scale build-up
Mineral scaling from carbonates, sulphates, silica, ferric (Fe+++), or H2S.Additional pre-treatmentsHardness, iron or manganese and hydrogen sulphideMembrane fouling
Increased pressure
Convert carbonate hardness to CO2 by adding acid.
Remove hardness by ion exchange.
Elemental sulphur and iron oxide deposits on the membrane.Increase frequency of membrane cleaning to a rate that resolves the problem
Additional pre-treatments
Perform water quality tests for: hardness (temporary and permanent), iron or manganese and hydrogen sulphide.Membrane fouling
Increased pressure

Add polyphosphates or silicates to prevent scaling.
Remove iron or manganese by greensand, chlorination or dichlorination (note, it is very important to remove residual) (no aeration.)
H2S can be removed by degasification.
Initiate more frequent cleaning of the membrane using citric acid.
Observation: Low product water flow rate, higher salt rejection, high operating pressure

Possible hazards: Low flow
Membrane compactionMonitor pressure
Ensure membrane installation is done correctly
Operating pressure should be less than 500psiLow flow rateReplace membrane.
Observation: High product flow rate with lower salt rejection

Possible hazards: High salt
Membrane hydrolysisIdentify the cause of membrane hydrolysis and optimise system
Add additional monitoring points for pH and temperature
Check pH and temperature to determine if they are within operating limitsHigh flow and high saltInjection of colloid 189 will sometimes extend membrane life
Replace membrane
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