| |
PERFORMANCE |
CONDITION |
DESCRIPTION |
RESPONSE |
ACTION |
| A1 |
REJECTION = |
FLUX = |
GOOD |
Element performing within specifications |
|
|
| A2 |
REJECTION = |
FLUX LOW |
FOULED |
Organic fouling more likely than inorganic |
CLEAN |
Chlorinate / UV, change carbon |
TEMPERATURE
VARIATION |
Cold feed water temperature greatly lowers flux. Standard = 77°F (25°C) |
|
Use higher productivity element |
PRESSURE
VARIATION |
Low pressure will give lower flux. Standard is 60
psi., residential-225 psi, commercial |
|
Increase pressure |
| A3 |
REJECTION = |
FLUX HIGH |
EMPERATURE
VARIATION |
Warm feed water temperature raises flux. Maximum is 110°F (43.3°C) |
|
Increase feed flow, cool feed water |
PRESSURE
VARIATIONS |
High pressure increases flux |
|
Check gauges |
| B1 |
REJECTION LOW |
FLUX = |
OXIDATION |
Chlorine or other oxidizers not adequately removed. Damage is accumulative and progressive |
REPLACE |
Change precarbon or chemical treatments |
RECOVERY TOO
HIGH |
Average feed concentration much higher than expected |
CLEAN |
Lower recovery |
| SEAL REVERSED |
Part of feed bypasses the element-fouling is very likely if not corrected quickly |
CLEAN |
Reverse element |
| B2 |
REJECTION LOW |
FLUX LOW |
FOULED |
#1 mode of element failure. Inorganic or organic material coats membrane surface |
CLEAN |
Lower recovery, add softener, use chemical feed additives |
| OVER PRESSURE |
Exceeding maximum pressure or allowing water hammer stretches membrane which opens up rejection layer and compresses support layer |
REPLACE |
Lower pressure and vent any air prior to start up |
| B3 |
REJECTION LOW |
FLUX HIGH |
OXIDATION |
2nd common mode of failure. Chemical burn of membrane destroys rejection layer |
REPLACE |
Increase precarbon size |
| BACTERIA |
Rarely happens, but membrane can be attacked |
REPLACE |
Use UV or chlorine
pretreatmen |