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October 14, 2026Understanding LSI and Scaling Indices: Why Your RO Reject Water Matters
October 15, 2026Low permeate flow is one of the most common complaints from RO plant operators. Production falls short, storage tanks do not fill, and pressure mounts to find a quick fix. The temptation is to raise the pressure or immediately clean the membranes. Sometimes that works, but often the real cause lies elsewhere. A systematic approach saves time, chemicals and membranes.

Step 1: Confirm the Problem Is Real
Before investigating membranes, check the measurement itself. Is the flow meter accurate? Rotameters can become dirty, and floats can stick. Cross-check by timing how long it takes to fill a known volume, or compare with tank level changes.
Step 2: Check the Temperature
Membrane productivity depends strongly on water temperature. Colder water is more viscous and passes through the membrane more slowly. A drop of several degrees in winter can reduce permeate flow noticeably even with perfectly clean membranes. Normalising flow to a reference temperature shows whether the decline is real or seasonal.
Step 3: Review Feed Pressure
If feed pressure has dropped, permeate flow will drop with it. Possible causes:
- Blocked cartridge filters: a high pressure drop across cartridges starves the high-pressure pump
- Worn high-pressure pump: internal wear reduces output pressure
- Low suction pressure: inadequate feed pump performance or low tank level
- Incorrect valve positions: reject or recycle valves adjusted improperly
Check the pressure readings at each point and compare them with commissioning data.
Step 4: Check Feed Water Quality
Changes in feed water can affect performance. Higher TDS increases osmotic pressure, reducing net driving pressure and permeate flow. Compare current feed conductivity with design values. If the source has changed, the plant may need adjustment.
Step 5: Look at Differential Pressure
If feed pressure is normal but permeate flow is low, examine the pressure drop across each stage.
- Rising pressure drop in the first stage: suggests particulate, colloidal or biological fouling
- Rising pressure drop in the last stage: suggests scaling
- Normal pressure drop with low flow: may indicate fouling on the membrane surface that does not restrict feed channels, or membrane compaction
Step 6: Check Recovery and Valve Settings
If the reject valve has been opened wider, more water leaves as reject and pressure falls, reducing permeate flow. Ensure recovery settings match design.
Step 7: Examine Pre-Treatment Performance
Many membrane problems originate upstream. Check:
- SDI after the cartridge filter
- Chlorine or ORP before the membranes
- Antiscalant dosing pump operation and tank level
- Filter backwash frequency and effectiveness
- Iron and manganese levels
Step 8: Inspect Membranes
If evidence points to the membranes, inspect the lead element of the first stage and the tail element of the last stage. Deposits, slime or scale provide strong clues. A membrane autopsy by a specialist laboratory can identify foulants precisely when the problem is persistent.
Step 9: Clean Appropriately
Choose cleaning chemicals based on the identified foulant: low-pH cleaning for scale and metal oxides, high-pH cleaning for organics, biofilm and colloids. Measure performance before and after to judge effectiveness.
Step 10: Fix the Root Cause
Cleaning restores performance temporarily. Lasting improvement comes from fixing the cause: improving pre-treatment, adjusting antiscalant dose, reducing recovery or improving sanitisation.
When Membranes Need Replacement
If cleaning no longer restores acceptable performance and membranes are several years old, replacement may be the most economical option. Replace with membranes suited to your water and consider a design review to prevent repeating the same problems.
Conclusion
Low permeate flow is a symptom, not a diagnosis. Working through temperature, pressure, feed quality, pre-treatment and membrane condition in a logical order reveals the true cause and points to the right solution.
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