| APPLICATIONS: |
| ProSoft™ Fine Mesh is ideally suited for use in industrial softening
applications. It has a high level of DVB which gives it a longer service life when softening
aggressive waters. It is intended for use in all water softening, dealkalization, deionization,
and chemical processing applications. |
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| PRESSURE DROP — The graph above shows the expected pressure loss per foot of bed depth as a
function of flow rate at various temperatures. |
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| BACKWASH — After each cycle the resin bed should be backwashed at a rate that expands the
bed 25 to 50 percent. This will remove any foreign matter and reclassify the bed. The graph above shows the expansion
characteristics of ProSoft™ Heavy Duty in the sodium form. |
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SODIUM CHLORIDE (NaCl) REGENERATION |
POUNDS
NaCl
per cu.ft. |
CAPACITY
Kilograins
per cu.ft. |
| 5 |
21.0 |
| 7.5 |
27.0 |
| 10 |
30.9 |
| 15 |
35.4 |
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The sodium cycle operating capacity for hardness removal at various regeneration levels
with an influent calcium/magnesium ratio of 2/1 and a hardness level of 500 ppm, as CaCO3. |
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HYDROGEN SULFATE (H2SO4) REGENERATION |
POUNDS
H2SO4
per cu.ft. |
CAPACITY
Kilograins
per cu.ft. |
| 5 |
20.0 |
| 7.5 |
24.5 |
| 10 |
27.0 |
| 15 |
30.1 |
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The hydrogen cycle operating capacity for hardness removal at various regeneration levels
with an influent calcium/magnesium ratio of 2/1 and a hardness level of 500 ppm, as CaCO3. |
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| ProSoft™ is a trademark of Safe Water Technologies, Inc. |
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Features: |
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Conforms to paragraph 21 CFR173.25 of the Food Additives Regulations of the FDA |
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10% divinylbenzene |
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Uniform particle size, low pressure drop |
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Superior physical stability |
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Low color throw |
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| PHYSICAL PROPERTIES |
| Part Number |
ER10006 |
| Polymer Structure |
Styrene crosslinked with DVB |
| Functional Group |
R-(SO3)-M+ |
| Ionic Form (as shipped) |
Sodium or Hydrogen |
| Physical Form |
Tough spherical beads |
Screen Size Distribution
+ 16 mesh (US Std.)
– 50 mesh (US Std.) |
5% maximum
1% maximum |
| pH Range |
0 to 14 |
| Sphericity |
93% minimum |
| Uniformity Coefficient |
Approx. 1.6 |
Water Retention
Sodium Form
Hydrogen Form |
39 to 45%
46 to 52% |
| Solubility |
Insoluble |
Approx. Ship. Wt.
Sodium Form
Hydrogen Form |
54 lb/cu.ft.
52 lb/cu.ft. |
| Swelling Ca+2 or Na+ to H+ |
Approx 5% |
Total Capacity
Sodium Form
Hydrogen Form |
2.2 meq/mL min.
2.1 meq/mL min. |
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| SUGGESTED OPERATING CONDITIONS |
Maximum Temperature
Sodium Form
Hydrogen Form |
280°F (138°C)
265°F (130°C) |
| Minimum Bed Depth |
24 inches |
Backwash Rate
50% Bed Exp. @60°F |
(See graph left)
7.0 gpm/sq.ft. |
Regenerant Concentration *
Sodium Cycle
Hydrogen Cycle (Option 1)
Hydrogen Cycle (Option 2) |
10 to 15% NaCl
10% HCl
1 to 8% H2SO4 |
| Regenerant Flow Rate |
0.5 to 1.5 gpm/cu.ft. |
| Regenerant Contact Time |
20 minutes minimum |
| Regenerant Level |
4 to 15 lb/cu.ft. |
| Displacement Rinse Rate |
0.5 to 1.5 gpm/cu.ft. |
| Displacement Rinse Volume |
10 to 15 gal/cu.ft. |
| Fast Rinse Rate |
2 to 10 gpm/cu.ft. |
| Fast Rinse Volume |
35 to 60 gal/cu.ft. |
| Service Flow Rate |
2 to 10 gpm/cu.ft. |
| Pressure Drop |
(See graph left) |
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*CAUTION: DO NOT MIX ION EXCHANGE RESINS
WITH STRONG OXIDIZING AGENTS. Nitric acid and other strong oxidizing agents can cause explosive
reactions when mixed with organic materials such as ion exchange resins.
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ADDITIONAL INFORMATION:
SWT Ion Exchange Resin Guide |
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This information has been gathered from standard materials and or test data that is believed
to be accurate and reliable. Nothing herein shall be determined to be a warranty or representation expressed or
implied with respect to the use of such information or the use of the goods described for any particular purpose
alone or in combination with other goods or processes, or that their use does not conflict with existing patent
rights. No license is granted to practice any patented invention. It is solely for your consideration, investigation
and verification.
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