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Sodium
Calcium Magnesium Potassium
Iron 2 Manganese 2 Aluminum Copper
Nickel
Zinc
Strontium Cadmium
Silver
Mercury
Barium Chromium
Lead
Chloride Bicarbonate Nitrate3 Fluoride Phosphate Chromate Cyanide
Sulfate
Boron
Arsenic + 3
Arsenic + 5 Selenium Radioactivity
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Bacteria
Protozoa Ameobic- Cysts
Giardia Asbestos Sediment/ Turbidity
Organic
Contaminants Organic molecules with a molecular weight < 300
Organic
molecules with a molecular weight < 3005
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90-95%
93-98% 93-98% 90-95% 93 98% 93-98% 93-98% 93-98% 93-98% 93-98% 93-98%
93-98% 93-98% 93-98% 93-98% 93-98% 93-98% 90-95% 90-95% 85-90% 90-95%
93-98% 90-95% 90-95% 93-98% 55-60% 70-80% 93-98% 93-98% 93-98%
--------
>
99%
> 99%
> 99%
> 99%
> 99%
> 99%
> 99%
>
99%
0-99%
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1.
This table of nominal rejection performance is for reverse osmosis
membranes used in drinking water systems operating at a net pressure
(feed pressure less back pressure and osmotic pressure) of 60 psi
and 77° F water temperature.
The
actual performance of systems incorporating these membranes may
be different due to changes in feed pressure, temperature, water
chemistry. contaminant level, net pressure on membrane, and individual
membrane efficiency. Countertop RO drinking water systems produce
better overall rejection performance than undercounter systems due
to maximizing of net pressure on membrane.
2.
While iron and manganese are effectively removed by the membrane,
they also can easily foul its surface with deposits even at low
concentrations. Generally, iron and manganese should be removed
by other water treatment methods prior to RO treatment.
3.
Nitrate removal depends on factors such as pH, temperature, net
pressure across membrane. and other contaminants present.
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