Summary
Strong Acid Cation Exchangers
Gel Resins
| Purolite Type | Ionic Form | Total Volume (eq/l) | Moisture Retention (%) | Specific Gravity | Reversible Swelling (%) | Remarks & Applications |
|---|
| C100 | Na⁺ | 2.0 | 44 - 48 | 1.29 | Na → H: 8 | Primary softening and demineralization resin. |
| C100E | Na⁺ | 1.9 | 46 - 50 | 1.27 | Ca → Na: 8<br>Na → H: 10 | Softening and demineralization resin, widely used in industrial and domestic applications. Potable water grade. |
| C120E | Na⁺ | 1.5 | 56 - 60 | 1.22 | Ca → Na: 12 | Designed specially for small scale domestic softening. Potable water grade. |
| C100X10 | Na⁺ | 2.2 | 40 - 43 | 1.30 | Na → H: 6 | Excellent resistance to oxidation. Higher density cation resin offering good separation from anion resins in mixed bed applications and weak acid cation resins in layered beds. |
| SGC650 | Na⁺ | 2.2 | 40 - 43 | 1.30 | Na → H: 8 | Uniform particle size used for condensate polishing and make up MB’s. Offers excellent physical strength and high resistance to OSA. |
| C150 | Na⁺ | 1.8 | 48 - 53 | 1.25 | Na → H: 4 | Macroporous structure offers high resistance to OSA. Employed in areas of very difficult operating conditions such as condensate treatment and process applications. |
| C160 | Na⁺ | 2.4 | 35 - 40 | 1.30 | Na → H: 4 | Higher cross linked macroporous resin with higher exchange capacity offering excellent resistance to oxidation. For process applications, such as non-ferrous hydrometallurgy and in the treatment of industrial waste streams. |
Note: Above products also available in the H⁺ form.
Shallow Shell Technology Resins
| Purolite Type | Ionic Form | Dry Weight Capacity (eq/kg) | Moisture Retention (%) | Specific Gravity | Reversible Swelling (%) | Remarks & Applications |
|---|
| SST60 | Na⁺ | *3.8 | 38 - 46 | 1.20 | Ca → Na: 8 | Shallow Shell Technology resin primarily for high performance softening for reducing operating costs through savings in rinse and regenerant consumption. Use SST60H for demineralization. |
| SST65 | Na⁺ | *3.9 | 40 - 47 | 1.20 | Ca → Na: 8 | For use in the CIX-RO™ Process using RO reject brine as a regenerant. |
| SST80 | Na⁺ | *4.2 | 42 - 48 | 1.27 | Ca → Na: 8 | Shallow Shell Technology resin primarily for softening of high TDS water at elevated temperature. Reduces operating cost through savings in rinsing and regenerant consumption. |
| SST104 | H⁺ | *6.6 | 34 - 44 | 1.17 | H → Ca: 10 | Unique product with high efficiency and less susceptible to heavy metal fouling. Particularly suited to high TDS softening. Reduces operating cost through savings in rinsing and regenerant consumption. |
*SST products typically have equal or higher operating capacities than standard grade ion exchange resins based on multiple cycles.
Particle Size Distribution - Cation Exchangers
| Purolite Grade | Nominal Particle Size (µm) | Max % Below Lower Limit | Uniformity Coefficient | Remarks & Applications |
|---|
| STD | 300 - 1200 | 1% < 300 | ≤ 1.7 | Standard grade. |
| MB | 425 - 1200 | 2% < 425 | ≤ 1.6 | Mixed Bed grade. |
| TL Gel | 550 - 1000 | 1% < 550 | ≤ 1.3 | Higher purity Mixed Bed grade which can be used with intermediate inert spacer in 3-component Mixed Bed systems (Trilite). |
| TL Macroporous | 710 - 1200 | 1% < 710 | ≤ 1.3 | |
| DL Strong | 630 - 1200 | 5% < 630 | ≤ 1.4 | Layered Beds, Lower Layer. |
| DL Weak | 300 - 850 | 2% < 300 | ≤ 1.4 | Layered Beds, Upper Layer. |
| S/C | 425 - 1200 | 2% < 425 | ≤ 1.6 | High flow rate IWT and special process applications. (treatment of sugar solutions, etc.) |
| G | 500 - 1200 | 2% < 500 | ≤ 1.5 | Very high flowrate softening applications, such as dishwashers. |
| Purolite Grade | Mean Diameter (µm) | Uniformity Coefficient | Remarks & Applications |
|---|
| PUROFINE® | 570 ± 50 | 1.1 - 1.2 | High efficiency softening and demineralization. Excellent kinetics and rinse properties. |
| PUROPACK® Gel | 650 ± 50 | 1.1 - 1.2 | High efficiency softening and demineralization. Counter flow packed bed system. Mixed bed cation component employed with PUROFINE anion grade. |
| PUROPACK® Macroporous and Acrylics | 750 ± 100 | 1.2 - 1.4 | High efficiency softening and demineralization. Counter flow packed bed system. |
Note: Most resins presented in this catalog can be supplied as Purofine® and Puropack® grades (specific literature available).
Weak Acid Cation Exchangers
| Purolite Type | Type | Ionic Form | Total Volume (eq/l) | Moisture Retention (%) | Specific Gravity | Reversible Swelling (%) | Remarks & Applications |
|---|
| C104Plus | Porous | H⁺ | 4.5 | 45 - 52 | 1.19 | H → Ca: 20<br>H → Na: 70 | High capacity regenerable dealkalization resin with good exchange kinetics. Also available in food grade as C104EPlus. |
| C106 | Macroporous | H⁺ | 2.7 | 54 - 64 | 1.15 | H → Ca: 15<br>H → Na: 50 | Higher resistance to OSA. For process applications, such as antibiotics extraction from fermentation broths and treatment of ammoniacal condensates. |
| C107E | Macroporous | H⁺ | 3.6 | 53 - 58 | 1.18 | H → Ca: 25<br>H → Na: 90 | Food Grade, specifically designed dealkalization resin for use in small cartridges for domestic applications. Not usually regenerated. |
| C115E | Porous | H⁺ | 3.5 | 46 - 53 | 1.10 | H → Ca: 40<br>H → Na: 100 | Very weakly acidic for process applications especially in the pharmaceutical industry. Recommended for the CARIX™ process. |
Strong Base Anion Exchangers
| Purolite Type | Type | Ionic Form | Total Volume (eq/l) | Moisture Retention (%) | Specific Gravity | Maximum Swelling (%) | Remarks & Applications |
|---|
| A400 | Type I | Cl⁻ | 1.3 | 48 - 54 | 1.08 | Cl → OH: 20 | Used primarily in industrial water treatment in warmer climates due to its higher temperature stability. Offers the best silica removal even in co-flow regenerated plants. Also widely used in mixed beds as A400MB, PFA400MB or A400TL. |
| A444 | Type I | Cl⁻ | 1.0 | 50 - 60 | 1.07 | Cl → OH: 20 | Alternative high moisture gel anion resin for demineralization and as organic scavenger on high TOC waters. |
| A600 | Type I | Cl⁻ | 1.4 | 43 - 48 | 1.09 | Cl → OH: 20 | Premium grade resin with high total capacity and high breaking weight. Very low silica leakage. |
| A200 | Type II | Cl⁻ | 1.3 | 45 - 51 | 1.08 | Cl → OH: 15 | High capacity resin offering good silica removal, primarily used in the production of demineralized and dealkalized water. |
| A300 | Type II | Cl⁻ | 1.4 | 40 - 45 | 1.10 | Cl → OH: 10 | Premium grade high capacity resin offering good silica removal. Primarily used in the production of demineralized and dealkalized water. |
| SGA550 | Type I | Cl⁻ | 1.4 | 43 - 48 | 1.09 | Cl → OH: 24 | Uniform particle size Supergel resin with higher resistance to mechanical and osmotic shock. Recommended for condensate polishing and make-up mixed beds, operating in conjunction with SGC650. |
| A500 | Type I | Cl⁻ | 1.15 | 53 - 58 | 1.08 | Cl → OH: 15 | Macroporous version of A400 offering greater resistance to OSA. Mainly used in condensate polishing or make-up mixed beds, where its polymer structure helps in resisting organic fouling. |
| A500P | Type I | Cl⁻ | 0.8 | 63 - 70 | 1.04 | Cl → OH: 20 | Polystyrenic based organic scavenger resin used to reduce NOM (Natural Organic Matter) and color levels and fouling of downstream anion resins. Also supplied as A500PS for potable water and food applications. |
| A501P | Type I | Cl⁻ | 0.6 | 70 - 75 | 1.04 | Cl → OH: 20 | Specifically designed for the adsorption of colloidal particulate (silica, organic matter, metals, clays, etc.). |
| A510 | Type II | Cl⁻ | 1.15 | 44 - 51 | 1.08 | Cl → OH: 10 | Macroporous version of A200 offering better resistance to OSA and organic fouling due to its polymer structure. |
| A850 | Gel | Cl⁻ | 1.25 | 57 - 62 | 1.09 | Cl → OH: 15 | Most widely used resin for the demineralization of high organic bearing waters, offering the best resistance to organic fouling. Higher operating capacity than type I polystyrenic resins, while still offering very good silica leakage in co-flow and counter-flow regeneration. |
| A860S | Macroporous | Cl⁻ | 0.8 | 66 - 72 | 1.08 | Cl → OH: 20 | Acrylic based organic scavenger resin used to reduce NOM (Natural Organic Matter) color levels and fouling of downstream anion resins. Also supplied as A860S for potable water and food applications. Better suited to brine-only regeneration than A500P. |
| A870 | Dual Functionality | Cl⁻/FB | 1.25 | 56 - 62 | 1.08 | Cl → OH: 10 | Bifunctional resin combining weak and strong base sites on the same beads, offering the highest operating capacity and good resistance to organic fouling. Should not be used where the feed water contains a high weak acid anionic loading (CO₂ + SiO₂). Recommended weak acid loading less than 20%. |
Note: Most of the above products are also available in the OH⁻ form.
SBA resins are temperature sensitive. This must be taken into consideration in selecting the correct product.
Particle Size Distribution - Anion Exchangers
| Purolite Grade | Nominal Particle Size (µm) | Max % Below Lower Limit | Uniformity Coefficient | Remarks & Applications |
|---|
| STD | 300 - 1200 | 1% < 300 | ≤ 1.7 | Standard grade. |
| MB | 300 - 1200 | 1% < 300 | ≤ 1.7 | Mixed Bed grade. |
| TL Gel | 425 - 850 | 1% < 425 | ≤ 1.35 | Higher purity Mixed Bed grade which can be used with intermediate inert spacer in 3-component Mixed Bed systems (Trilite™). |
| TL Macroporous | 425 - 850 | 1% < 425 | ≤ 1.35 | |
| DL Strong | 630 - 1200 | 5% < 630 | ≤ 1.4 | Layered Beds, Lower Layer. |
| DL Weak | 300 - 630 | 3% < 300 | ≤ 1.4 | Layered Beds, Upper Layer. |
| S/C | 425 - 1200 | 2% < 425 | ≤ 1.6 | High flow rate IWT and special process applications. (treatment of sugar solutions, etc.) |
| Purolite Grade | Mean Diameter (µm) | Uniformity Coefficient | Remarks & Applications |
|---|
| PUROFINE® | 570 ± 50 | 1.1 - 1.2 | High efficiency grade with excellent kinetics and rinse properties. Also employed as mixed bed anion component with PFC and PPC grade cation resins. |
| PUROPACK® Gel | 650 ± 50 | 1.1 - 1.2 | High efficiency grade particularly suited to counter flow regenerated packed bed systems. |
| PUROPACK® Macroporous and Acrylics | 750 ± 100 | 1.2 - 1.4 | High efficiency grade particularly suited to counter flow regenerated packed bed systems. |
Note: Most resins presented in this catalog can be supplied as Purofine® and Puropack® grades (specific literature available).
Ready to Use Mixed Beds
| Purolite | Ionic Form | Component Description | Typical Working Capacity (eq/l) | Remarks & Applications |
|---|
| MB400 | H⁺ / OH⁻ | 40% Strong Acid Cation Gel<br>60% Strong Base Anion Gel Type I | 0.60 | For the production of high-purity, silica-free demineralized water. Principal use in polishing units after small IEX or RO plants. Also used in direct treatment of raw waters. High operating capacity, achieving conductivities less than 0.1 µS/cm in many polishing applications. MB400 is the most popular ready to use industrial grade mixed bed. |
| MB3720 | H⁺ / OH⁻ | 40% Strong Acid Cation Gel<br>60% Strong Base Anion Gel Type I | 0.60 | This product is the highest quality industrial grade mixed bed offering enhanced performance between that associated with industrial and UPW grades. |
| MB46LT | H⁺ / OH⁻ | 50% Strong Acid Cation Gel<br>50% Strong Base Anion Gel Type I | 0.70 | High capacity mixed bed, specific for the EDM market (spark erosion machining). Also used for direct treatment of raw waters with high alkalinity. |
| MB478LT | H⁺ / OH⁻ | 50% Strong Acid Cation Gel<br>50% Strong Base Anion Gel Type I | 0.60 | Primarily used for EDM applications. |
Note: Working capacities to full exhaustion, typical for the first column in a lead-lag layout and dependent on influent water quality and end point. Many other special customized Mixed Beds are produced with and without indicators – consult your local Purolite sales office.
Ready to Use Mixed Beds with Indicator
| Purolite | Ionic Form | Color Change On Exhaustion | Component Description | Typical Working Capacity (eq/l) | Remarks & Applications |
|---|
| MB400IND | H⁺ / OH⁻ | Blue (regenerated) / Amber (exhausted) | Indicator on anion component<br>40% Strong Acid Cation Gel<br>60% Strong Base Anion Gel Type I | 0.60 | For the production of high-purity, silica-free demineralized water. Principal use in polishing units after small IEX or RO plants. Also used in direct treatment of raw waters. High operating capacity, achieving conductivities less than 0.1 µS/cm in many polishing applications. |
| MB600AE | H⁺ / OH⁻ | Greenish Blue (regenerated)<br>Reddish Amber (exhausted) | Indicator on anion component<br>40% Strong Acid Cation Gel<br>60% Strong Base Anion Gel Type I | 0.66 | High performance mixed bed with special particle size and bright color change thanks to the unique indicator used. Product successfully used in the production of cartridges for steam irons. |
| MB500VC | H⁺ / OH⁻ | Green (regenerated)<br>Blue (exhausted) | Indicator on cation component<br>40% Strong Acid Cation Gel<br>60% Strong Base Anion Macroporous Type I | 0.54 | High contrast color change mixed bed with a UV stable indicator for the production of high quality demineralized water. Can be used in polishing units as well as for the direct treatment of raw waters. Product successfully used in the production of cartridges for steam irons. |
| MB59VC | H⁺ / FB | Green (regenerated)<br>Blue (exhausted) | Indicator on cation component<br>60% Strong Acid Cation Gel<br>40% Weak Base Anion Macroporous | 1.1 | Very high capacity mixed bed employing a WBA component for the production of partially demineralized water, where removal of CO₂ and SiO₂ is not required. Typical run end point of 30 - 50 µS/cm. |
Note: Working capacities to full exhaustion, typical for the first column in a lead-lag layout and dependent on influent water quality and end point. Many other special customized Mixed Beds are produced with and without indicators – consult your local Purolite sales office.
Nuclear Grade Products
| Purolite Type | Type | Ionic Form | Total Capacity (eq/l) | Moisture Retention (%) | Remarks & Applications |
|---|
| NRW1000 | Gel | H⁺ | 1.8 | 51 - 55 | Make up demineralization and radwaste systems. This cation resin is not normally used in Li or ⁷Li forms as a stand-alone resin. |
| NRW1100 | Gel | H⁺ | 2.0 | 46 - 50 | Used in separate bed cation vessels for polishing or layered on mixed bed resins for added cation capacity. Also available in ⁷Li, Li and NH₄ forms. Higher capacity version of NRW1000. |
| NRW1160 | Gel | H⁺ | 2.5 | 36 - 41 | Primary purification cation beds for delithiation and outage clean up. Polishing steam generator blow down and layering on polishing mixed beds. Also available in ⁷Li form. |
| NRW160 | Macroporous | H⁺ | 2.1 | 43 - 48 | Polishing steam generator blow down and layering on polishing mixed beds. Primary purification cation beds for delithiation and outage clean up. Selective for ¹³⁷Cs. Also available in ⁷Li form. |
| NRW4000 | Gel | OH⁻ | 1.0 | 48 - 54 | Separate bed demineralizer anion radwaste systems. Type 1, nuclear grade version of A400, offering good silica removal and removal of weak and strong acids. |
| NRW6000 | Gel | OH⁻ | 1.1 | 43 - 48 | Primary and secondary separate bed demineralizer anion. Also used as underlay in condensate polishing. Higher total capacity version of NRW4000. |
| NRW7000 | Gel | OH⁻ | 1.15 | 42 - 47 | Primary and secondary separate bed demineralizer anion. Also used as underlay in condensate polishing. |
| NRW5010 | Macroporous | OH⁻ | 0.4 | 70 - 75 | Special nuclear grade colloid removal resin for single beds or surface layer on mixed beds to achieve ultra polishing of primary coolant and radwaste. |
| NRW5050 | Macroporous | OH⁻ | 0.9 | 53 - 58 | Porous structure designed to give greater resistance to surface fouling in a wide range of nuclear applications. |
Nuclear Grade Mixed Beds
| Purolite | Ionic Form | Components | Total Volume Capacity (min eq/l) | Remarks & Applications |
|---|
| NRW3240 | H⁺/OH⁻ | Gel Cation<br>Gel Anion | 1.8/1.0 | Primary polishing, clean up systems, and radwaste. |
| NRW3460 | H⁺/OH⁻ | Gel Cation<br>Gel Anion | 2.0/1.1 | Higher total capacity version of NRW3240 for primary polishing, clean up systems and radwaste. |
| NRW3560 | H⁺/OH⁻ | Macroporous Cation<br>Gel Anion | 2.1/1.1 | Mixed Bed with very high capacity and porous cation for primary purification, steam generator blow down and spent fuel pool demineralization. |
| NRW3670 | H⁺/OH⁻ | Gel Cation<br>Gel Anion | 2.5/1.15 | Primary polishing, condensate polishing, spent fuel pool demineralizer, steam generator blow down demineralizer and reactor water cleanup. |
(1) Cation component available in ⁷Li form
(2) Cation component available in Li form
Notes:
A. Nuclear grade mixed beds are normally supplied with near stoichiometric equivalents of anion and cation resin sites. Other ratios can be supplied on request.
B. Purolite Nuclear Grade Products are in operation within the defense industry or nuclear power stations in the Americas, Europe and Asia and carry formal approvals from leading operators of nuclear installations. They meet internationally recognized specifications from the leading suppliers of nuclear power station designs.
Purity of Nuclear Grade Ion Exchangers
Cation Resins
| Ionic Form | Conversion | Impurities (mg/kg dry) |
|---|
| H⁺ | 99.9% min. | Sodium: 40 max.<br>Iron: 50 max.<br>Heavy Metals as Lead: 40 max. |
| Li⁺ or ⁷Li⁺ | 99.9% min. | Sodium: 40 max.<br>Iron: 50 max.<br>Heavy Metals as Lead: 40 max. |
Anion Gel Resins
| Ionic Form | Conversion | Impurities (mg/kg dry) |
|---|
| OH⁻ | 95% min. | Sodium: 20 max.<br>Iron: 50 max.<br>Heavy Metals as Lead: 30 max. |
| CO₃²⁻ | 5% max. | |
| Cl⁻ | 0.1% max. | |
| *SO₄²⁻ | 0.1% max. | |
*0.3% max. for NRW5010.
Ultrapure Water Products
Ultraclean™
| Type | Ionic Form | Total Volume Capacity (min eq/l) | Moisture Retention (%) | Specific Gravity | Remarks & Applications |
|---|
| UCW9126 | H⁺ | 1.9 | 49 - 54 | 1.21 | Ultrapure Water Cation Resin with very low TOC release operating in single beds or mixed beds with anion component UCW5072. |
| UCW5072 | OH⁻ | 1.0 | 55 - 60 | 1.07 | Ultrapure Water Anion Resin with very low TOC release operating in single beds or mixed beds with cation component UCW9126. |
| UCW1080 | Free Base | 0.6 | 61 - 67 | 1.10 | Semiconductor Industry - Ultrapure Water for Selective Boron Removal. |
Note: The ratio of Cation to Anion is chemically equivalent at 1:1.
Ultraclean™ Ultrapure Water Mixed Beds
| Purolite | Ionic Form | Total Volume Capacity (min eq/l) | Moisture Retention (%) | Remarks & Applications |
|---|
| UCW9964 | H⁺ / OH⁻ | Cation: 1.9<br>Anion: 1.0 | Cation: 49 - 54%<br>Anion: 55 - 60% (Cl⁻ form) | Highest purity separable MB for final polishing and point of use treatment for UPW systems. Highest resistivity and very low TOC release. |
| UCW9966 | H⁺ / OH⁻ | Cation: 1.9<br>Anion: 1.0 | Cation: 49 - 54%<br>Anion: 55 - 60% (Cl⁻ form) | Highest purity non separable MB for final polishing and point of use treatment for UPW systems. Highest resistivity and very low TOC release. |
| UCW3600 | H⁺ / OH⁻ | Cation: 1.9<br>Anion: 1.1 | Cation: 49 - 54%<br>Anion: 55 - 62% | High operating capacity separable Mixed Bed for UPW systems. |
| UCW3700 | H⁺ / OH⁻ | Cation: 1.9<br>Anion: 1.0 | Cation: 46 - 50%<br>Anion: 60 - 70% | Separable Mixed Bed for UPW systems. |
| UCW3900 | H⁺ / OH⁻ | Cation: 2.0<br>Anion: 1.0 | Cation: 49 - 54%<br>Anion: 60 - 70% | Separable Mixed Bed with higher capacity cation for UPW systems. |
Pharmaceutical Products
Active Pharmaceutical Ingredients
| Purolite Type | USP/EP Type | Remarks & Applications |
|---|
| C100NaMR | Sodium Polystyrene Sulfonate | Strong acid cation resin with sulfonic acid groups in sodium form; purified, ground and dried for the treatment of hyperkalemia. Can also be used as a drug carrier for controlled release. |
| C100CaMR | Calcium Polystyrene Sulfonate | Strong acid cation resin with sulfonic acid groups in the calcium form; purified, ground and dried for the treatment of hyperkalemia. |
| A430MR | Cholestyramine | Special strong base anion resin; purified chloride form, ground and dried for treatment of high cholesterol. |
| A830EMR | Polyamine | Weak base anion resin in free base form; purified, ground, dried and used as antacid to control gastric acidity. |
Note: The manufacturing site is approved by the FDA and is cGMP certified.
Excipients and Tablet Disintegrants
| Purolite Type | Type | Remarks & Applications |
|---|
| C100HMR | Polystyrene Sulfonic Acid | Strong acid cation resin with sulfonic acid groups in hydrogen form; purified, ground, dried and used as a drug carrier for controlled release. |
| C108DR | Polyacrylic Acid | Special weak acid cation resin in hydrogen form; provided as very fine, dry beads and used as a drug carrier for controlled release or as taste masking. |
| C115HMR | Polacrilex | Weak acid cation resin in hydrogen form; purified, ground, dried and used as a drug carrier or as pH adjuster in the formulation of tablets. |
| C115KMR | Polacrilin Potassium | Weak acid cation resin in potassium form; purified, ground, dried and used as a tablet disintegrant. |
Note: Consult your local Purolite office for confirmation of regional, country or state regulatory compliance.
Hydrometallurgical Resins
| Purolite Type | Functional Group | *Ionic Form | Capacity | Moisture Retention (%) | Remarks & Applications |
|---|
| A100/2412 | Mixed Base Anion | Mixed Tertiary & Quaternary Amines | Cl⁻: 3.8 eq/kg | 46 - 56 | For effective recovery of aurocyanide complexes obtained from the alkaline cyanide processing of gold ores. Suitable for RIP process. 800-1300 µm grading. |
| S992 | Weak Base / Chelating | Mixed Amines | FB: 4.4 eq/kg | 47 - 55 | For effective recovery of aurocyanide complexes obtained from the alkaline cyanide processing of gold ores. Suitable for RIP process. 800-1300 µm grading. |
| A500C | Strong Base Anion | Quaternary Ammonium | Cl⁻: 1.15 eq/l | 53 - 58 | For effective recovery of gold complexes obtained from the thiosulfate processing of gold ores. |
| PFA600/4740 | Strong Base Anion | Quaternary Ammonium | Cl⁻: 1.6 eq/l | 40 - 45 | For the extraction of uranyl sulfate and carbonate complexes from the leachates originated from ISL, batch or heap leaching processes. |
| A660/4759 | Strong Base Anion | Quaternary Ammonium | Cl⁻: 1.3 eq/l | 44 - 52 | For the extraction of uranyl sulfate complexes from the sulfuric leachates. Suitable for RIP process. 800-1300 µm grading. |
| PFA460/4783 | Strong Base Anion | Quaternary Ammonium | Cl⁻: 1.3 eq/l | 47 - 54 | For the extraction of uranyl sulfate complexes from the clean sulfuric solutions. |
| A500U/2788 | Strong Base Anion | Quaternary Ammonium | Cl⁻: 1.15 eq/l | 53 - 58 | For uranium recovery. Suitable for RIP process. 800-1300 µm grading. |
| A500U/4994 | Strong Base Anion | Quaternary Ammonium | Cl⁻: 1.15 eq/l | 53 - 58 | For uranium recovery. Suitable for RIP process. 710-1300 µm grading. |
| A560/4790 | Strong Base Anion | Quaternary Ammonium | Cl⁻: 1.15 eq/l | 49 - 56 | For uranium recovery from the sulfuric solutions. Suitable for RIP process. 800-1300 µm grading. |
| A100Mo | Mixed Base Anion | Mixed Tertiary & Quaternary Amines | Cl⁻: 1.2 eq/l | 48 - 56 | For molybdenum recovery from acid solutions. |
| S930Plus | Chelating | Iminodiacetic | Na⁺: 50 g/l Cu | 52 - 60 | For base metals recovery from weak acid solutions. |
| S930/4888 | Chelating | Iminodiacetic | Na⁺: 50 g/l Cu | 52 - 60 | For base metals recovery from weak acid solutions. Suitable for RIP process. 800-1300 µm grading. |
| S950 | Chelating | Amino-phosphonic | Na⁺: 26 g/l Ca | 60 - 68 | For recovery of uranium from phosphoric acid. |
| S960 | Chelating | Bis-picolylamine | SO₄²⁻: 25 g/l Ni | 50 - 60 | For sorption of base metals from more concentrated sulfuric solutions and separation of base metals. |
| A170/4675 | Weak Base Anion | Complex Amine | FB: 1.3 eq/l | 42 - 47 | For selective sorption of rhenium from acid streams. Suitable for RIP process. 600-1200 µm grading. |
| A172/4635 | Weak Base Anion | Complex Amine | FB: 1.2 eq/l | 25 - 45 | For separation of rhenium from molybdate. |
| S984 | Weak Base / Chelating | Mixed primary, secondary and tertiary amines | FB: 2.7 eq/l | 50 - 56 | For tungsten impurity removal from molybdate solutions. |
| S957 | Strong Acid Cation / Chelating | Mixed Sulfonic and Phosphonic | Na⁺: 18 g/l Fe | 55 - 70 | For removal of ferric iron from copper, nickel or cobalt electrolytes as well as molybdenum sorption from strong acid solutions. |
*Some products can be supplied in customized ionic form.
Adsorbents
PUROSORB™ Polymeric Adsorbents
| Polymer Matrix | Pore Diameter (Å) | Pore Volume (ml/g) | Surface Area (m²/dry g) | Moisture Retention (%) | Remarks & Applications |
|---|
| Polystyrenic | 350 | 0.7 | 700 | 58 - 64 | These two polystyrene based polymeric adsorbents offer consistent enhanced performance over carbon and other adsorbents and are specifically designed for selective adsorption of molecules with a relatively low molecular weight. Polystyrenic adsorbents are more selective to non-polar products and their pore size has been tightly controlled to enhance this selectivity. The variations in surface area and pore volume give each product unique advantages in certain applications. This includes the removal of hydrocarbons and chlorinated solvents from ground waters and industrial waste streams. |
| Polystyrenic | 400 | 0.7 | 720 | 55 - 61 | |
| Polystyrenic | 620 | 1.0 | 700 | 63 - 69 | This unique product, characterized by medium size pores and a narrow particle size distribution, offers definitive advantages over standard grade adsorbents. Its uniform beads ensure lower pressure drop in service duty and enhanced elution profiles of the adsorbed species on desorption. Typical applications include the extraction and separation of antocyans and polyphenols from grape must and other fruit juices. |
| Polystyrenic | 600 | 1.1 | 950 | 58 - 64 | These three products differ in offering a range of surface areas, pore volumes and pore sizes specifically tailored for applications where medium to large molecular weight species are targeted within the application. Typical applications include the isolation and purification of Active Pharmaceutical Ingredients. |
| Polystyrenic | 630 | 1.1 | 830 | 58 - 64 | |
| Polystyrenic | 700 | 1.2 | 550 | 56 - 62 | |
| Polystyrenic | 1000 | 1.5 | 800 | 67 - 73 | Special manufacturing techniques are employed to manufacture this range of polystyrene based adsorbents offering the largest pore sizes. They are designed to capture the largest molecular weight species in a wide range of applications such as the extraction of antibiotics from fermentation broths or bitterness removal from citrus juices. |
| Polystyrenic | 1100 | 1.6 | 540 | 62 - 68 | |
| Polyacrylic | 280 | 0.5 | 90 | 59 - 65 | These products are all based on an acrylic matrix which gives them different chemical properties. Their less hydrophobic structure enables them to outperform polystyrene based synthetic adsorbents in non-polar media but does not mean they cannot be used in aqueous solutions. They have widely differing surface areas, pore volumes and pore sizes to cover a wide range of applications. The changes in these parameters alter the selectivity of each product. |
| Polyacrylic | 700 | 1.1 | 490 | 60 - 66 | |
| Polyacrylic | 960 | 1.3 | 535 | 65 - 71 | |
HYPERSOL-MACRONET®
| Type | Volume Capacity (eq/l) | Pore Diameter (Å) | Surface Area (m²/dry g) | Moisture Retention (%) | Remarks & Applications |
|---|
| MN100 | 0.1 - 0.3 (FB form) | 900 | 900 | 57 - 61 | For the efficient sorption of high molecular weight color bodies such as those found in sugar solutions and many complex organics such as dyestuffs or certain pesticides. |
| MN102 | 0.1 - 0.3 (FB form) | 750 | 700 | 50 - 60 | For the efficient sorption of high molecular weight organic molecules such as limonin and narangin from fruit juices. Regenerated more easily than other materials due to its weak base functionality. |
| MN200 | - | 900 | 900 | 57 - 61 | For the efficient sorption of high molecular weight organic molecules with lipophilic properties (dyestuffs, pesticides) in industrial process waste water treatment. |
| MN202 | - | 750 | 700 | 50 - 60 | For the efficient sorption of high molecular weight organic molecules with lipophilic properties as are typically found in waste waters from industrial processes. These include complex organics such as dyestuffs or pesticides. |
| MN270 | - | 25 | 1200 | 35 - 50 | Sorption / Separation of hydrophobic organic species - Microporous matrix. Pore Volume 0.2 – 0.4 ml/g. |
| MN500 | 0.8 - 1.0 (Na⁺ form) | 900 | 900 | 52 - 57 | Sorption / Separation of hydrophobic organic species |
| MN502 | 0.8 - 1.0 (Na⁺ form) | 750 | 700 | 52 - 57 | Sorption / Separation of hydrophobic organic species |
Chromatographic Resins
Cation Chromatographic Resins
| Purolite Type | Total Volume Capacity (eq/I) (Na form) | Mean Size Typical (µm) | Moisture Retention % (Na form) | Moisture Retention % (H form) | Remarks & Applications |
|---|
| PCR145 | 1.5 | 270 - 310 | 55 - 60 | 60 - 66 | Cation chromatographic separation resins can be supplied in Ca²⁺, Na⁺, K⁺ or H⁺ forms. Ca²⁺ form separations: Glucose-Fructose, Maltose. Na⁺ form separations: Beet Molasses, Dextrose enrichment, Erythritol. K⁺ form separations: Beet Molasses, Fructo-oligosaccharides, Soluble fiber. H⁺ form separations: Acid-Sugar (cellulose hydrolyzate). |
| PCR450 | 1.35 | 360 - 400 | 60 - 65 | 65 - 71 | |
| PCR631 | 1.6 | 210 - 240 | 50 - 56 | 55 - 62 | |
| PCR632 | 1.7 | 210 - 250 | 52 - 55 | 55 - 61 | |
| PCR633 | 1.6 | 210 - 240 | 50 - 56 | 55 - 62 | |
| PCR642 | 1.6 | 295 - 335 | 52 - 56 | 57 - 61 | |
| PCR651 | 1.6 | 330 - 360 | 52 - 56 | 57 - 61 | |
| PCR652 | 1.6 | 350 - 370 | 52 - 56 | 57 - 61 | |
| PCR732 | 1.8 | 210 - 250 | 50 - 52 | 53 - 57 | |
| PCR833 | 2.0 | 225 - 275 | 44 - 48 | 51 - 55 | |
Anion Chromatographic Resins
| Purolite Type | Total Volume Capacity (eq/l) (Cl⁻ form) | Mean Size Typical (µm) | Moisture Retention % (Cl⁻ form) | Remarks & Applications |
|---|
| PCA433 | 1.3 | 230 - 280 | 48 - 57 | Anion chromatographic separation resin can be supplied in Cl⁻, SO₄²⁻, OH⁻ forms |
Catalyst Resins
| Purolite Type | Functional Group | Ionic Form | Total Capacity (eq/dry kg) | Moisture Retention (%) | Remarks & Applications |
|---|
| CT122 | Sulfonic | H⁺ | 4.8 | 78 - 82 | Recommended for esterification reactions and for the synthesis of Bisphenol A. |
| CT124 | Sulfonic | H⁺ | 5.0 | 65 - 70 | Recommended for esterification reactions and for the synthesis of Bisphenol A. |
| CT151 | Sulfonic | H⁺ | 5.1 | 54 - 59 | Specifically designed for catalysis of organic reactions, in particular for the purification of phenol. |
| CT169 | Sulfonic | H⁺ | 4.7 | 51 - 57 | MTBE, ETBE, TAME, TAEE, Esterification, C4 dimerization. |
| CT175 | Sulfonic | H⁺ | 4.9 | 53 - 58 | Excellent accessibility of active sites. Studied and developed for the synthesis of MTBE, ETBE and TAME. |
| CT251 | Sulfonic | H⁺ | 5.2 | 54 - 59 | Primarily used for phenol purification, esterification, C4 dimerization. |
| CT252 | Sulfonic | H⁺ | 5.4 | 54 - 58 | Primarily used for esterification, aromatic alkylation, phenol purification, and C4 dimerization. Highest dry weight capacity. |
| CT269 | Sulfonic | H⁺ | 5.2 | 51 - 57 | High activity with very good mechanical resistance. Ideal for esterification reactions and phenol alkylation. |
| CT275 | Sulfonic | H⁺ | 5.2 | 54 - 59 | High activity catalyst with excellent accessibility of active sites. Recommended for the synthesis of MTBE, ETBE, TAME and TAEE. |
| CT276 | Sulfonic | H⁺ | 5.3 | 51 - 59 | For MTBE, ETBE, TAME, and C4 dimerization. High dry weight capacity. |
| CT482 | Sulfonic | H⁺ | 4.0 | 61 - 68 | High temperature catalysis. Hydration of olefins in MEK process, hydrogenation of MIBK. |
Note: Most products are also available in DR (Dry) grade.
Chelating Resins
| Purolite | Functional Group | Ionic Form | Capacity | Moisture Retention (%) | Remarks & Applications |
|---|
| S110 | N-methylglucamine | Free Base | 0.8 eq/l | 40 - 50 (Cl⁻) | Removal of boron from brines, concentrated aqueous solutions and waste waters. For potable water applications see S108. |
| S910 | Amidoxime | Free Base | 40 g/l Cu | 52 - 60 | Selective removal of heavy metals from wastewater and hydrometallurgical processes. |
| S920 | Isothiouronium | H⁺ | 200 g/l Hg | 48 - 54 | High selectivity and high capacity for mercury removal in wastewaters. Widely used for final polishing to meet mercury discharge limits. Selective removal of precious metals (gold, platinum, palladium, etc) from acidic solutions. Non-regenerable use. |
| S924 | Thiol | H⁺ | 200 g/l Hg | 45 - 51 | Regenerable resin designed for the selective removal of mercury from wastewaters and special applications (i.e. chlor-alkali plants). |
| S930Plus | Iminodiacetic | Na⁺ | 50 g/l Cu | 52 - 60 | Improved version of S930 widely used as a general metals polisher from a wide variety of wastes. Purification of brine in chlor-alkali plants offering highly efficient removal of strontium. Extremely high copper capacity. Countless applications in non-ferrous hydro‐metallurgy. |
| S940 | Amino-phosphonic | Na⁺ | 20 g/l Ca | 55 - 65 | Highly selective for low atomic weight metals. Also used in purification of brine where lower strontium levels are encountered in chlor-alkali plants. |
| S950 | Amino-phosphonic | Na⁺ | 26 g/l Ca | 60 - 68 | Selective removal of heavy metals from wastewaters. Purification of selected plating baths in the surface finishing industry. (i.e. Bright Nickel bath rejuvenation) |
| S957 | Phosphonic/ Sulfonic | H⁺ | 18 g/l Fe | 55 - 70 | Resin for removing trace iron from drinking water. Applications in the purification of galvanic baths including removal of iron in low pH applications. Purification of selected plating baths in the surface finishing industry. |
| S960 | Bis-picolylamine | SO₄²⁻ | 25 g/l Ni | 50 - 60 | For sorption of base metals from more concentrated sulfuric solutions and separation of base metals. |
| S985 | Polyamine | Free Base | 2.3 eq/l | 52 - 57 | Removal of heavy metals present in complexed form (e.g. EDTA complexes) from wastewaters. |
Powdered Resins for Condensate Polishing
MICROLITE® Powdered Resins
| Type | Functional Group | Ionic Form | Total Capacity (eq/kg) | Moisture Retention (%) | Standard Packaging Dry Weight (kg) | Remarks & Applications |
|---|
| PrCH | Sulfonic (Cation) | H⁺ | 4.8 | 45 - 62 | 8.8 | 100% Powdered Cation Hydrogen Form. |
| PrCN | Sulfonic (Cation) | NH₄⁺ | 4.8 | 40 - 60 | 10.2 | 100% Powdered Cation Ammonia Form. |
| PrAOH | Quaternary Ammonium (Anion) | OH⁻ | 4.0 | 50 - 60 | 5.7 | 100% Powdered Anion Hydroxide Form. |
| FC+ | Inert (Cellulose Fiber) | Neutral | - | 55 - 75 | 5.5 | 100% Specialty Cellulose Fiber. |
MICROLITE® Powdered Resin Premixes
| Type | Functional Group | Ionic Form | Total Capacity (eq/kg) | Ratio Cation to Anion (dry wt.) | Ratio Fiber to Resin | Standard Packaging Dry Weight (kg) | Remarks & Applications |
|---|
| CG12H | Sulfonic/Quaternary Ammonium (Cation/Anion) | H⁺ / OH⁻ | 4.8 / 4.0 | 4 : 5 | 1 : 2 | 5.5 | Resin/Fiber blend. Also available in ammonium / hydroxide form. |
| CG19H | Sulfonic/Quaternary Ammonium (Cation/Anion) | H⁺ / OH⁻ | 4.8 / 4.0 | 4 : 5 | 1 : 9 | 5.5 | Resin/Fiber blend. Also available in ammonium / hydroxide form. |
| CG4H | Sulfonic/Quaternary Ammonium (Cation/Anion) | H⁺ / OH⁻ | 4.8 / 4.0 | 1 : 1 | 1 : 1 | 5.5 | Resin/Fiber blend. Also available in ammonium / hydroxide form. |
| MB1/1H | Sulfonic/Quaternary Ammonium (Cation/Anion) | H⁺ / OH⁻ | 4.8 / 4.0 | 1 : 1 | - | 5.5 | Resin only. Also available in ammonium / hydroxide form. |
Note: Other custom made resin/fiber premixed combinations available upon request.
Selective Resins for Potable Water
| Purolite Type | Type | Functional Group | Ionic Form | Total Capacity (eq/l) | Moisture Retention (%) | Remarks & Applications |
|---|
| A520E | Macroporous | Quaternary Ammonium | Cl⁻ | 0.9 | 50 - 56 | Selective nitrate removal resin for municipal water, food / drink production and domestic applications. |
| A530E | Macroporous | Quaternary Ammonium | Cl⁻ | 0.6 | 49 - 55 | Selective removal of perchlorate, pertechnetate and other oxyanions from water for potable use. |
| A532E | Gel | Quaternary Ammonium | Cl⁻ | 0.8 | 36 - 45 | Ultra high selectivity and capacity for perchlorate, pertechnetate and other oxyanions from water for potable use. |
| S108 | Macroporous | N-methylglucamine | Free Base | 0.6 | 61 - 67 (Cl⁻) | Selective removal of boron from potable water and water used in agriculture/horticulture irrigation. For industrial applications see S110. |
Special Ion Exchangers
| Purolite Type | Functional Group | Ionic Form | Total Capacity (eq/l) | Moisture Retention (%) | Remarks & Applications |
|---|
| MPR1000 | Strong Base Anions | Quaternary Ammonium | Cl⁻: 0.6 | 68 - 74 | Proprietary resin blend for reducing membrane fouling by removing colloidal materials and dissolved organic matter from RO feedwater. Significant SDI reduction. |
| C100EAg | Sulfonic (Strong Acid Cation) | Na⁺ | 1.9 | 46 - 50 | Softening resin with bacteriostatic properties containing a small proportion of special silver loaded resin. |
| C150Ag | Sulfonic (Strong Acid Cation) | Na⁺/Ag⁺ | 1.8 | 48 - 53 | Silver loaded resin used as bacteriostatic additive for softening resins. |
| A605 | Quaternary Ammonium (Iodinated Strong Base Anion) | Cl⁻/I⁻ | - | - | Iodine release anion resin for disinfecting potable water at point of use. For remote locations and treatment of contaminated water. |
| HM6 / HM10 | Sulfonic / Tertiary Amine | H⁺/FB/ Nutrients | - | - | Two products for nutrient release for healthy growth and development of ornamental plants in hydroculture. |
| NRW100QR | Sulfonic (Strong Acid Cation) | H⁺ | 1.9 (Na) | 53 - 57 (H) | Cation resin with indicator. On exhaustion, color changes from neutral (regenerated form) to red (exhausted form). Widely used for after-cation conductivity measurement for monitoring condensate quality on power stations. |
| C100EVCH | Sulfonic (Strong Acid Cation) | H⁺ | 1.9 (Na) | 53 - 57 (H) | Cation resin with indicator. On exhaustion color changes from green (regenerated form) to blue (exhausted form). |
| A200MBOH IND | Quaternary Ammonium (Strong Base Anion Type II) | OH⁻ | 1.3 (Cl⁻) | 45 - 51 (Cl⁻) | High capacity Type 2 anion resin with indicator. Upon exhaustion color changes from blue (regenerated form) to neutral form (exhausted form). Used in HCl vent scrubbers and demineralization tank vents to stop CO₂ ingress. |
| A400MBOH IND | Quaternary Ammonium (Strong Base Anion Type I) | OH⁻ | 1.3 (Cl⁻) | 48 - 54 (Cl⁻) | Type 1 version of A200MBOHIND. Also available as macroporous product as A500MBOHIND. Anion resin with indicator. Upon exhaustion color changes from blue (regenerated form) to neutral form (exhausted form). |
| CT275Ag | Sulfonic (Strong Acid Cation) | H⁺/Ag⁺ | 5.2 | 51 - 59 | Silver loaded resin for the removal of alkyl iodides (C1 to C12 or higher) in organic solvents such as acetic acid, under low temperature conditions (<50°C) and /or high flow rate. |
| PD206 | Sulfonic (Strong Acid Cation) | H⁺ | 4.9 eq/kg | - | Premium dry resin with optimized residual moisture for biodiesel purification for removal of glycerine, water and residual cations. Helps to produce biodiesel to international recognized standards. |
| OL100 | Sulfonic (Strong Acid Cation) | Na⁺ | 1.9 | 44 - 48 | Specially activated resin designed for oil separation from water by coalescence. Primary application in deoiling of condensates. |
Special Products
| Purolite Type | Shipping Weight (g/l) | Particle Size or Dimension (mm) | Remarks & Applications |
|---|
| AC20 Granular Activated Carbon | 470 - 490 | 0.4 - 1.4 | For the removal of free chlorine & organic contaminants from potable water. |
| AC20G Granular Activated Carbon | 470 - 490 | 0.6 - 2.4 | Coarse version of AC20 for the removal of free chlorine & organic contaminants from potable water. |
| IP1 Polyethylene | 540 - 560 | 2.5 - 4.0 | Floating inert polymer for Puropack® systems with downflow service. |
| IP3 Polyacrylate | 680 - 710 | Mean 0.67 - 0.73 | Inert spacer for use in gel Trilite™ 3-component mixed beds. |
| IP4 Polypropylene | 520 - 550 | 1.1 - 1.5 | Floating inert polymer in the form of small cylinders for Puropack® systems with upflow service. |
| IP7 Polyacrylate | 680 - 710 | Mean 0.67 - 0.73 | Blue colored inert spacer for use in macroporous high performance Trilite™ 3-component mixed beds. |
| IP9 HDPVC | 800 - 900 | 3 - 5 | Heavy inert polymer for use as an underbed - cylindrical form. |
| MZ10 Manganese Zeolite | 1300 - 1400 | 0.25 - 1.0 | Activated greensand for removal of iron, manganese and hydrogen sulfide from ground water. Potable water treatment and pre-treatment for ion exchange resins plants. |
| CPM 7040 Cation Permselective Membrane | 380 - 420 g/m² | 1000 x 3000 | Heterogeneous membrane, permeable to cations; for electrodialysis and anaphoresis. |
| APM 7540 Anion Permselective Membrane | 380 - 420 g/m² | 1000 x 3000 | Heterogeneous membrane, permeable to anions; for electrodialysis and cataphoresis. |
Disclaimer: This extraction may miss figures, footnotes, or revisions. Contractual data must match the OEM PDF revision used on the project.
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