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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 — The graph above shows the expansion characteristics as a function of flow rate at various temperatures. |
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APPLICATIONS: |
Boron Removal From Potable Water
ProSelect Boron/Borate can be used to remove boron from potable waters of any type. Its selectivity for boron is so high that the concentration of common bulk ions — such as chloride, sulfate, and bicarbonate — are unimportant. ProSelect Boron/Borate is kinetically limited and cannot be operated at a high flow rate without experiencing increased leakage and decreased throughput capacity.
Regeneration is accomplished with acid to strip the boron, followed by caustic to remove the acidity. The regenerated resin should be buffered into the potable water range to prevent possible pH excursions when it is first returned to service, and also to prevent possible calcium carbonate scaling. |
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Boron Removal From Brine
ProSelect Boron/Borate can be used to remove boron from almost any brine stream, even when the brine is fully saturated. The brine pH must not be lower than approximately 4 or the chelating exchange groups will be destabilized and might not work properly. Ion exchange in any concentrated salt solution is kinetically hindered by high TDS, therefore flow rates are necessarily low. |
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ProSelect™ is a trademark of Safe Water Technologies, Inc. |
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Features: |
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Highly selective for boron — able to remove boron from almost any liquid solution, provided that the pH is greater than 4 |
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Superior physical stability — 90% plus sphericity, high crush strengths, and carefully controlled particle distribution provide long life and low pressure drop |
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Suitable for regenerable applications — two stage acid/caustic regeneration process restores the capacity for hundreds of operating cycles |
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PART NUMBER |
Free Base Form |
ER20013 |
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PHYSICAL PROPERTIES |
Polymer Matrix |
Styrenic Macroporous |
Ionic Form |
Free Base |
Functional Group |
Methylglucamine |
Physical Form |
Spherical beads |
Color |
White to tan |
Particle Size |
16 to 50 US Mesh
(297 to 1190 μm) |
% < 50 mesh (300 μm) |
< 1% |
Minimum Sphericity |
95% |
Uniformity Coefficient |
1.6 |
Reversible Swelling |
Free Base to Cl
15% to 20% |
Temperature Limit |
170°F (77°C) |
Capacity |
0.8 meq/ml |
Moisture Retention |
46 to 60% |
Regenerability |
Yes |
Approx. Ship. Wt. |
38 to 40 lb/cu.ft.
(609 to 641 g/L) |
Packaging |
500 ml samples
1 cu.ft. bags
1 cu.ft. boxes
1 cu.ft. drums
7 cu.ft. drums
42 cu.ft. supersacks |
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SUGGESTED OPERATING CONDITIONS |
Maximum Temperature
Free Base Form |
170°F (77°C) |
Minimum Bed Depth |
24 inches |
Backwash Expansion |
25 to 50% |
Maximum Pressure Loss |
20 psi |
Operating pH Range |
4 to 10 SU |
Regenerant Concentration
Acid Strip
Caustic Neutralization |
0.5 to 6% HCl
1 to 4% NaOH |
Regenerant Level |
3 to 10 lb/cu.ft. |
Regenerant Flow Rate |
0.25 to 1.0 gpm/cu.ft. |
Regenerant Contact Time |
> 30 minutes |
Displacement Flow Rate |
Same as dilution water |
Displacement Volume |
10 to 15 gal/cu.ft. |
Rinse Flow Rate |
Same as service flow |
Rinse Volume |
35 to 60 gal/cu.ft. |
Service Flow Rate |
0.5 to 2 gpm/cu.ft. |
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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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