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G.  TROUBLESHOOTING 

 

RO MEMBRANE TROUBLE SHOOTING GUIDE 

SYMPTOMS

 

 

Salt Passage 

Permeate Flow 

Pressure Drop 

Location 

Possible Causes 

Verification 

Corrective Action 

Normal to 
increased 

Decreased 

Normal to 
increased 

Predominantly 
first stage 

Metal oxide 

Analysis of metal 
ions in cleaning 
solution. 

Improved pretreatment 
to remove metals. 
Cleaning with acid 
cleaners. 

Normal to 
increased 

Decreased 

Normal to 
increased 

Predominantly 
first stage 

Colloidal fouling 

SDI measurement 
of feed/ X-ray 
diffraction 
analysis of 
cleaning sol. 
residue. 

Optimize pretreatment 
system for colloid 
removal. Clean with 
high pH, anionic 
detergent formulation. 

Increased 
 
 

Decreased 

Increased 

Predominantly 
last stage 

Scaling  
(CaSO

4

, CaSO

3

BaSO

4

, SiO

2

Analysis of metal 
ions in cleaning 
sol. Check LSI of 
reject. Calculate 
maximum 
solubility for 
CaSO

4

, BaSO

4

SiO

2

 in reject 

analysis. 

Increase acid addition 
and scale inhibitor for 
CaSO

3

 and CaSO

4

Reduce recovery. 
Clean with an acid 
formulation for 
CaCO

3

, CaSO

4

 and 

BaSO

4

.  

Normal to 
moderate 
increase 

Decreased 

Normal to 
moderate 
increase 

Can occur in 
any stage 

Biological fouling 
 

Bacteria count in 
permeate and 
reject. Slime in 
pipes and vessels. 

Shock dosage of 
sodium bisulfite. 
Continuous feed of 
low conc. bisulfite at 
reduced pH. Peracetic 
acid sterilization. 
Clean with alkaline 
anionic surfactant. 
Chlorine dosage up-
stream with  
dechlorination. 
Replace cartridge 
filters. 

Decreased or 
moderately 
increased 

Decreased 

Normal 

All stages 

Organic fouling 

Destructive 
testing, e.g. IR 
reflection 
analysis. 

Optimization of 
pretreatment system 
(e.g. coagulation 
process.) 
Resin/activated carbon 
treatment. Clean with 
high pH detergent. 

Increased 

Increased 

Decreased 

Most severe in 
the first stage 

Chlorine oxidant 
attack 

Chlorine analysis 
of feed. 
Destructive 
element test. 

Check chlorine feed 
equipment and 
dechlorination 
equipment. 

Increased 

Increased 

Decreased 

Most severe in 
the first stage 

Abrasion of 
membrane by 
crystalline material 

Microscopic 
solids analysis of 
feed. Destructive 
element test. 

Improved 
pretreatment. Check 
all filters for media 
leakage. 

Increased 

Normal to 
increased 

Decreased 

At random 

O-ring leaks, End 
or side seal glue 
leaks. 

Probe test. 
Vacuum test. 
Colloidal 
material passage. 

Replace O-rings. 
Repair or replace 
elements. 

Increased 

Normal to low 

Decreased 

All stages 

Conversion too 
high. 

Check flows and 
pressures against 
design guidelines 

Reduce conversion 
rate. Calibrate sensors. 
Increase analysis and 
data collection. 

 

 

 

Summary of Contents for R4X40

Page 1: ...REVERSE OSMOSIS INSTALLATION AND OPERATION MANUAL Model R4X40...

Page 2: ......

Page 3: ...ty of the end user Successful long term performance of an RO system depends on proper operation and maintenance of the system This includes the initial system startup and operational startups and shut...

Page 4: ...nt II Controls Indicators and Components III Operation A Installation B Plumbing Connections C Electrical D Startup E Control Function F Operation and Maintenance Log G Troubleshooting IV Replacement...

Page 5: ...0 ppm TDS and pH 7 Individual membrane productivity may vary 15 May be operated on other feed waters with reduced capacity Percent Rejection is based on membrane manufactures specifications overall sy...

Page 6: ...suspended solids sediment from the feed water Backwashing the media removes the trapped particles Backwash can be initiated by time or differential pressure Water Softener Used to remove calcium and m...

Page 7: ...solubility Additionally the solubility is highly pH and temperature dependent Silica fouling can be prevented with chemical injection and or reduction in recovery II CONTROLS INDICATORS and COMPONENT...

Page 8: ...Figure 1...

Page 9: ...Figure 2 Controller Connections...

Page 10: ...he product water line should never be restricted Membrane and or system damage may occur if the product line is blocked 3 Connect the reject water outlet to a drain The reject outlet is located behind...

Page 11: ...rating data using the log sheet E CONTROL FUNCTION 1 When the on off switch is in the on position the inlet valve opens and the pump runs There is a five second delay between the opening of the inlet...

Page 12: ...ater TDS The meter will automatically turn it self off after a few seconds The quality meter is powered by two AAA batteries To replace the batteries lift the meter out of the bracket and remove the b...

Page 13: ...ED WATER TEMP FEED WATER HARDNESS FEED WATER CHLORINE LEVEL PRE FILTER INLET PRESSURE PRE FILTER OUTLET PRESSURE REMARKS Note Change the prefilter when the differential pressure increases by 5 10 psi...

Page 14: ...and reject Slime in pipes and vessels Shock dosage of sodium bisulfite Continuous feed of low conc bisulfite at reduced pH Peracetic acid sterilization Clean with alkaline anionic surfactant Chlorine...

Page 15: ...Low feed water temperature Adjust reject valve or replace pump Increase membrane feed pressure or heat the feed water IV REPLACEMENT PARTS LIST A list of common replacement parts is provided below Co...

Page 16: ...e the end caps The new membranes should be installed in the same orientation as the old membranes Note It is very important that the brine seal does not flip up or roll when installing the membrane br...

Page 17: ...perating at 50 recovery with a feed water SDI 1 R4X40 1 R4X40 2 R4X40 3 Product GPM 1 5 3 0 4 5 Reject GPM 1 5 3 0 4 5 Nominal flows for systems operating at 50 recovery with a feed water SDI 3 R4X40...

Page 18: ...0 68 0 86 19 66 2 0 84 18 64 4 0 81 17 62 6 0 79 16 60 8 0 77 15 59 0 74 14 57 2 0 72 13 55 4 0 70 12 53 6 0 68 11 51 8 0 66 10 50 0 64 9 48 2 0 62 8 46 4 0 61 7 44 6 0 59 6 42 8 0 57 5 41 0 55 Multip...

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