Table 33. Troubleshooting reverse osmosis (RO) issues
Probable causes | Preventive measures | Checking preventive measures | Corrective action | |
---|---|---|---|---|
What to check | Signs that action is needed | |||
Observation: Low product water or accelerated differential pressure build-up due to turbidity Possible hazards: Increases scale build-up |
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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 failure | Monitor 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 membrane | Increase frequency of membrane cleaning to a rate that resolves the problem | Cleaning 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 spacer | 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) 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-treatments | Hardness, iron or manganese and hydrogen sulphide | Membrane 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 compaction | Monitor pressure Ensure membrane installation is done correctly | Operating pressure should be less than 500psi | Low flow rate | Replace membrane. |
Observation: High product flow rate with lower salt rejection Possible hazards: High salt | ||||
Membrane hydrolysis | Identify 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 limits | High flow and high salt | Injection of colloid 189 will sometimes extend membrane life Replace membrane |