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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 R12-Wall Mount

Page 1: ...REVERSE OSMOSIS INSTALLATION AND OPERATION MANUAL R12 Wall Mount ...

Page 2: ......

Page 3: ...e 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 shutdowns Prevention of fouling or scaling of the membranes is not only a matter of system design but also a matter of proper operation Record keeping and data normalization are required in order to know the actu...

Page 4: ...ent 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 Parts List V Membrane Replacement VI Appendix Temperature Correction Factors ...

Page 5: ...sufficient to eliminate chemicals that would attack the membrane materials A SPECIFICATIONS R12 0150 R12 0250 R12 0600 R12 1200 Maximum Productivity Gallons per day 150 250 600 1200 Quality membrane rejection 98 98 98 98 Recovery user adjustable 15 75 15 75 15 75 30 75 Membrane Size 2 5 x 14 2 5 x 21 2 5 x 40 2 5 x 40 Number Of Membranes 1 1 1 2 Dimensions W x H x D approximate inches 22 x 32 x 12...

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 magnesium from the feed water in order to prevent hardness scaling The potential for hardness scaling is predicted by the Langelier Saturation Index LSI The LSI should be zero or negative throughout th...

Page 7: ...and temperature dependent Silica fouling can be prevented with chemical injection and or reduction in recovery I CONTROLS INDICATORS and COMPONENTS see figure 1 A On Off Switch Turns the unit on and off B Product Pressure Switch Automatically turns the unit on and off based on the product water pressure C Reject Control Valve Controls the amount of reject flow D Reject Recycle Control Valve Contro...

Page 8: ...Figure 1 ...

Page 9: ...ater 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 at the reject needle valve or on top of the product flow meter depending on how the unit is equipped The reject drain line should never be restricted Membrane and or system damage may occur if the reject drain line is ...

Page 10: ...ed 200 psi on the pump discharge gauge Figure 1 item F 10 Allow the product water to flow to drain for 30 minutes 11 Turn off the system and connect the product line to the point of use The product water line should never be restricted Membrane and or system damage may occur if the product line is blocked 12 Restart the system and record the initial operating data using the log sheet E CONTROL FUN...

Page 11: ...EED 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 over the clean differential pressure Clean the RO membrane s when the product flow drops by 15 or more See appendix ...

Page 12: ... 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 Optimizatio...

Page 13: ... of common replacement parts is provided below Contact your dealer for replacement parts assistance Part Number Description S9550 D T Pre filter housing 10 R9677 SV2514 1 RO membrane pressure vessel 2 5 x 14 SS R9677 SV2521 1 RO membrane pressure vessel 2 5 x 21 SS R9677 SV2540 1 RO membrane pressure vessel 2 5 x 40 SS R2451 Pressure gauge 2 0 100 psi dry bottom mount R2456 Pressure gauge 2 0 100 ...

Page 14: ... the new membranes 6 Lightly lubricate the brine seals on the new membranes with clean water 7 Install the new membranes in the direction of flow with the brine seal end going in last 8 Lightly lubricate the end cap internal and external o rings with glycerin 9 Install the end caps and secure them with the U pins 10 Reconnect the tubing to the pressure vessel 11 Verify that all retaining U pins ar...

Page 15: ...ature Correction Factors Deg C Deg F Correction Factor 30 86 1 16 29 84 2 1 13 28 82 4 1 09 27 80 6 1 06 26 78 8 1 03 25 77 1 00 24 75 2 0 97 23 73 4 0 94 22 71 6 0 92 21 69 8 0 89 20 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 Multiply the nominal pro...

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