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Reverse Osmosis Membranes
Hydranautics Technical Articles
Reverse Osmosis Troubleshooting
Reverse Osmosis Troubleshooting
Reverse Osmosis Chemistry
Troubleshooting Your RO
Summary: There can be many reasons why a RO system suffers a loss in
performance, and is unable to produce the proper quantity and/or quality of
permeate water. Similar to a doctor attempting to make a diagnosis, you must
identify as many symptoms as possible before you can derive an educated guess
as to what the disease is.
The focus of this paper is how to troubleshoot a RO system on-site. Many of the
techniques assume the equipment has been designed with instrumentation and
sampling points to allow troubleshooting and for on-site cleanings, which is
common for ï¿½industrial qualityï¿½ systems, but not necessarily for ï¿½residential or
light commercialï¿½ equipment. The capital cost for small RO to include
troubleshooting instruments and sample valves is prohibitive for their market
niches, relative to the minimal cost of replacing RO elements on a more frequent
basis. As RO systems reach a certain size (say 15 gpm or larger), the cost of
replacing RO elements on a frequent basis becomes prohibitive versus the initial
capital cost of adding instruments, sample valves and on-site cleaning
HOW TO AVOID TROUBLE
The best way to stay out of trouble with a RO system is to avoid it initially.
A few RO design tips are:
ï¿½ Design the RO system with access to a complete water analysis. If there are
seasonal variations (which are common for surface sources) or varying
sources (which are common with municipal sources), get all the analyses you
can and be sure they are recent.
ï¿½ Perform 15 minute SDI (Silt Density Index) tests. This on-site testing helps to
determine the potential for colloidal silt fouling. Refer to TSB113.
ï¿½ Invest in the appropriate pretreatment. If you want to sleep well at night, make
sure the system design has adequate pretreatment to the RO.
ï¿½ Design the RO system flux rate conservatively, especially if the potential for
fouling exists. A RO with a clean well water source can be designed more
aggressively than one for a surface water source. A reduced rate of permeate
water flow for a given area of membrane reduces the convective deposition of
foulants at the membrane surface. Fluxes for surface waters should range
from 8 to 14 gfd (gallons per square foot of membrane area per day) and 14
to 18 gfd for well sources.
ï¿½ Design the RO recovery rate conservatively. A conservative per cent recovery
of the feed water minimizes the concentration of foulants.
ï¿½ Maximize the cross flow velocity in the elements. A conservative design
maximizes the cross-flow velocity of the feed and concentrate streams. A
higher cross-flow velocity reduces the concentration of salts and foulants at
the membrane surface by increasing their diffusion back into bulk feed stream
above the membrane surface.
ï¿½ Select the right membrane for the application. Sometimes a neutrally
charged CAB (cellulose acetate blend) or LFC (Low Fouling Composite) RO
element is a better choice than a negatively charged CPA (Composite
PolyAmide) RO element for difficult surface or waste water sources.
IDENTIFYING A PROBLEM
Verify that you really have RO system fouling. Changes in system operating
parameters do have an effect on performance. For instance, an increase in feed
TDS (total dissolved solids) will increase feed pressure requirements by
approximately 1 psig for every 100 ppm TDS increase due to increased osmotic
pressure and it will also increase permeate conductivity since the RO will always
reject a fixed percentage of the salts. A 10o F increase in feed water temperature
will decrease the feed pump pressure requirement by 15%. An increase in the
per cent recovery of the system will increase the reject TDS which in turn will
increase permeate conductivity. (Concentrate TDS due to concentration of the
feed water is 2 times higher at 50% recovery, 4 times higher at 75% recovery
and 10 times higher at 90% recovery). Finally, a reduction in the permeate flow will result in higher conductivity if the same recovery is maintained because the
passage of salts through the membrane is independent of the passage of water
through the membrane, which results in less permeate water to dilute the salts
that have passed through.
It is recommended that you ï¿½normalizeï¿½ your logged operating data to determine
if you have a problem with your system. ï¿½Normalizationï¿½ computer programs,
such as RODATA, graphically represent normalized permeate flow, per cent salt
rejection and feed-to-reject pressure drop. These normalized parameters are
calculated by comparing a particular dayï¿½s operations to the first day of operation.
Adjustments are made for changes in major operating variables such as
temperature, feed TDS, recovery, and pressures. In this way, performance
declines unrelated to operating parameters can be identified and treated.
Questions to ask yourselfï¿½
Loss in performance is generally divided into two categories: loss of flow, and
loss of rejection. The following lists of questions help to identify possible root
causes for either of these problems.
Loss of Flow
Attributable to fouling, these questions can help pinpoint the problem. Certain
foulants impact the front end of the system while others impact the back end of
the system. Use the RO Troubleshooting Matrix (at the end of this document) to
help determine the nature of the foulant.
ï¿½ Did you shut down the RO system properly? In some instances, the reject
water from the Service operation should be flushed out of the system upon
shutdown. If not, inorganic foulants can precipitate onto the surface of the
membrane. The best flush water source is RO permeate.
ï¿½ Did you store the RO system properly? Improperly stored systems
(especially under warm conditions) can produce a severe biofilm problem.
(Refer to TSBï¿½s 101, 103, 108, and 110 for more information).
ï¿½ If you acidify to lower feed pH or add scale inhibitor (SI) for the control of
calcium carbonate (lime) scale, are you meeting your target pH or SI
concentration? If not, you may need to do an acid clean. (TSBï¿½s 100, 102,
ï¿½ Has your pressure drop between the feed and reject lines increased greater
than 15%? Increasing pressure drop indicates that fouling of the feed path
and a restriction of flow over the membrane surface is occurring. Monitoring
pressure drops across stages gives you the advantage of determining if the
fouling is limited to a particular stage, which can help identify the potential
ï¿½ In seawater systems, are you flushing with permeate water at shut-down?
Flushing removes high concentrations of ions that could precipitate out of
solution. At a minimum, feedwater can be used, but it is recommended to use
permeate water for the flush.
ï¿½ Are the cartridge filters fouling? Inspect the RO feed cartridge filter for
foulants as this is relatively easy.
Loss of Rejection
Loss of rejection displays itself as a higher permeate conductivity. It may be due
either to fouling, degradation of the membrane surface, or an o-ring leak. The
following questions can help you pinpoint the source of this problem. Verify that
the permeate conductivity has not increased greater than 15%.
ï¿½ Do all the vessels in a stage have nearly the same conductivity permeate?
Measure permeate quality by stage and by pressure vessel if possible. One
vessel having a significantly higher permeate conductivity probably has a
faulty o-ring, a disconnect, or a damaged membrane. (See TSBï¿½s related to
vessel shimming (TSB 109) and vessel probing (TSB 114) to determine the
point of the leak).
ï¿½ Have your composite membranes been exposed to chlorine or any other
strong oxidant? The exposure may have damaged the membranes.
ï¿½ Have your cellulose acetate (CAB) membranes been exposed to pH
extremes? The exposure may have damaged the membranes.
of pH extremes are faulty metering pumps, acid tanks that have gone dry,
loss of prime to the metering pump, or flushing/storage in non-acidified water.
ï¿½ Is the instrumentation accurate? Verify that all of your instruments are
ï¿½ Do the elements look discolored or damaged? Inspect the RO elements for
foulants or physical damage.
ï¿½ How do the actual conductivity and temperature of the feedwater compare to
the design criteria? If the actual feedwater has higher TDS or is warmer than
the design, this may account for the discrepancy. Sample and obtain detailed
water analyses of the RO feed, concentrate and permeate. Compare the
results of the analyses to the RO design projections of the element
ï¿½ Can there be times when the permeate pressure exceeds the feed pressure?
If the permeate is pumped to an elevated position, and there are no check
valves on the permeate lines, at shut down, the permeate pressure can
exceed the feed pressure. This can cause the membrane envelopes to
expand and rupture.
ï¿½ Are your o-rings in good condition? O-rings can flatten or crack with age. The
result is that leaks can develop. Replacement of o-rings periodically is a good,
cost-effective preventive maintenance step. Alternatively, vessels may be
probed (TSB 114) to find faulty o-rings.
IF you still think there is a problemï¿½
ï¿½ Once you have ruled out any mechanical failures as the source of your RO
problem, then you need to determine what your suspected foulant or foulants
are and perform a cleaning or series of cleanings.
ï¿½ The cleaning solution can be collected and analyzed for the foulants
removed, color change or pH change. The effectiveness of the cleaning can
be verified by placing the RO back into Service.
ï¿½ If you donï¿½t know what your foulants are and donï¿½t want to experiment on site
as to what cleaning solution(s) are required and what the proper cleaning
procedures should be, their are companies who specialize in the supply of
proprietary cleaning chemicals and off-site evaluations of RO elements.
These services can be invaluable, especially the first time around in cleaning
ï¿½ If all else fails in determining what fouled the RO element, a destructive
autopsy can be performed. The RO element is cut open and unrolled with
analytical tests run on the membrane and the foulant to determine the
Hydranautics can perform analytical testing of foulants at our labs, as well as
perform Scanning Electron Microscopy (SEM) and Energy Dispersive X-Ray
analysis to help determine the cause of fouling. TSB 116, Returned Goods
Authorization (RGA) Procedure, provides a list of services and costs.
This list of questions should help in troubleshooting most RO problems. Attached
is a table to help determine some of the most common problems from the given
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