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ResinTechModel SIR-900 -Granular Aluminum Oxide Based Adsorbent

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ResinTech SIR-900 is a granular aluminum oxide based adsorbent. SIR-900 is supplied as an active oxide media based on porous aluminum oxide. ResinTech SIR-900 is intended for removal of fluoride from water. It can also be used for the removal of arsenate, selenate, and lead from potable water. SIR-900 is supplied in the activated adsorbent form.

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  • Physical Structure : Crystalline Aluminum Oxide
  • Physical Form: Granules
  • Water Retention: 0 to 10 percent
  • Approximate Shipping Weight     : 38 lbs/cu.ft.
  • Screen Size Distribution : 16 to 50 (U.S. Mesh)
  • Maximum Fines Content: 1 percent (less than 50 Mesh)
  • Uniformity Coefficient: 2.2 (Approximate)
  • Resin Color: White

High Affinity for Fluoride

Adsorbs fluoride ions efficiently, especially when pH is slightly acidic

Multiple Contaminant Removal

Removes a variety of contaminants such as arsenic and lead through a combination of adsorption and chemical reactions

Superior Physical Stability

Good physical integrity helps minimize breakage and fines formation

Controlled Granule Size

Large granules provide good physical strength and minimal fines provide low pressure loss.

Fluoride Removal

Fluoride is removed by ResisinTech SIR-900 by a chemical reaction which is flow and pH sensitive. The best results are obtained when the flow is limited to about 1 gpm/cu.ft. and the pH is held at 5.5. Higher flows and higher or lower pH results in loss of capacity. Leakage of fluoride is generally less than 0.1 mg/L to breakthrough. SIR-900 can be regenerated with sodium hydroxide, followed by neutralization with acid at a pH of 5-6.

Arsenic Removal

Inorganic arsenic (arsenate) can be removed by ResisinTech SIR-900. The process is pH sensitive and capacity decreases when the pH is below 5.5 or above 6.O. Arsenite is not removed nearly as well as arsenate, therefore pre-oxidation may be required.

Lead Removal

Dissolved lead is adsorbed by ResisinTech SIR-900. This process is not dramatically affected by flow rate, temperature or TDS. However, pH should be maintained above 6.0 as lead removal drops under acidic conditions, and below 10 as lead precipitates under basic conditions.