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glasswatersystems@msn.com
glasswatersystems@yahoo.comGreensandPlus™ is a purple-gray fi lter media used for
removing soluble iron, manganese, hydrogen sulfi de, arsenic
and radium from well water supplies.
Like its sister product manganese greensand, the substrate
media has a manganese dioxide coated surface that acts
as a catalyst in the oxidation- reduction reaction of iron
and manganese. The difference between GreensandPlus™
and Manganese Greensand is in the substrate that forms
the core of the media and the method by which the
manganese dioxide coating is attached to that substrate.
GreensandPlus™ has a silica sand core and the coating is
fused to it while Manganese Greensand has a glauconite
core and the coating is ionically bound to it.
The silica sand core of GreensandPlus™ allows it to better
withstand operating conditions in waters that are low in
silica, TDS and hardness. Thus, if you currently are using
manganese greensand and are feeding sodium aluminate,
you will likely be able to eliminate the aluminate feed by
switching to GreensandPlus™. Also, GreensandPlus™
can withstand higher operating temperatures and higher
differential pressures than can manganese greensand. The
higher differential pressure may allow for a longer run length,
but, if nothing else, allows for more operational margin of
error.
Along with the added benefi ts comes the fact that
GreensandPlus™ is an exact replacement for manganese
greensand. It can be used in CR and IR applications and
requires no changes in backwash rate or times or chemical
feeds. GreensandPlus™ has received the WQA Gold Seal
Certifi cation for compliance with NSF/ANSI 61. It is available
in easy-to-handle 1/2 cubic foot bags.
GreensandPlus™ is NOT shipped in a regenerated form;
therefore it is necessary, prior to use, to regenerate it
contacting the bed for a minimum of 4 hours
Capacity/Cu. Ft.:
Iron Alone .................550 gr. (10,000 gal. of water con tain ing
1 ppm iron/cu. ft.)
Iron and Manganese ........................400 gr. (7,000 gal. of water
containing 1/2 ppm iron and
1/2 ppm manganese/ cu. ft.)
Hydrogen Sulfide .................................175 gr. (3,000 gal. of water
containing 1 ppm hydrogen sulfide. cu. ft.)
Advantages:
• Iron removal over wide pH range
• Effective removal of hydrogen sulfi de in addition
to iron and/or manganese
• No harmful effects from a chlorine feed
• Low attrition loss for long bed life
Physical Properties:
Color ....................Black nodular granules
Density ............................................85 lbs./cu. ft.
Effective Size .....................0.30 - 0.35 mm
Uniformity Coeffi cient ...............................1.6
Mesh Size .....................................18 X 60
Attrition Loss Per Year ..................................2%
Conditions for Operation:
Raw Water pH .......................................6.2 - 8.5
Bed Depth ........................30 in.
Freeboard ............................................35 - 50%
Service Flow Rate ............................2 – 5 gpm/sq. ft. (5-12 m/hr)
Backwash Flow Rate ......................... 12 gpm/sq. ft. at 55ºF
(30 m/hr at 13ºC)
Maximum Temperature ...............No Limit
Maximum Practical Limit of Iron (Fe++) or
Man ga nese (Mn++) In Raw Water ...............................15 ppm.
Maximum Practical Limit of
Hydrogen Sulfi de (H2S) ................5 ppm.