AQUChem
How-to Guides

How to Use Strong Acid Cation Resin 001×7 in Water Treatment

5 min read·
strong acid cation resinwater softeningdemineralizationion exchange

Overview

Strong Acid Cation (SAC) resin 001×7 is a gel-type sulfonated polystyrene divinylbenzene (DVB) cation exchange resin — the workhorse of industrial water treatment. Its sulfonic acid functional group (–SO₃H) is fully ionized across the entire pH range (0–14), making it effective at exchanging both hardness cations (Ca²⁺, Mg²⁺) and all other cations (Na⁺, K⁺, Fe²⁺, Mn²⁺) regardless of feed pH.

SAC resin operates in two fundamentally different service forms depending on the application:

  • Na⁺ form (softening): The resin exchanges Ca²⁺ and Mg²⁺ for Na⁺. The effluent conductivity remains nearly unchanged because Na⁺ replaces the equivalent meq of Ca²⁺/Mg²⁺. Regeneration uses sodium chloride (NaCl) brine. This is the standard configuration for boiler makeup softeners, cooling tower makeup, and domestic water softeners.

  • H⁺ form (demineralization): The resin exchanges all cations for H⁺. The H⁺ released then combines with anions present in the water to form free acids, which are subsequently removed by an anion exchange column. Regeneration uses hydrochloric acid (HCl) or sulfuric acid (H₂SO₄). This is the configuration for two-bed demineralization (cation → degasser → anion) and mixed-bed polisher systems.

Total exchange capacity is ≥1.9 meq/mL wet volume, with a typical working capacity of 0.8–1.2 meq/mL in softening service (Na form) and 0.6–1.0 meq/mL in H form demineralization, depending on regenerant dose and flow rate.

Preparation & Loading

New resin pre-treatment: Fresh resin ships in Na⁺ form preserved in brine. Before commissioning, rinse with 2–3 bed volumes (BV) of demineralized or softened water to remove fines and transport solution. For H⁺ form service, perform a chemical conversion: pass 4–5% HCl at 2 BV/h for 30 minutes, then rinse to neutral effluent pH (≥6.0).

Column sizing: Design service flow rate at 8–15 BV/h (equivalent to 8–15 m³/h per m³ of resin). Bed depth should be at least 800 mm to ensure adequate contact time. The recommended height-to-diameter ratio is 2:1 to 3:1 for most softening applications. For demineralization in H form, a minimum 1000 mm bed depth is preferred to prevent premature Na leakage.

Loading procedure:

  1. Fill the column 50% with demineralized water.
  2. Slowly pour resin slurry in from the top while water overflows through the distributor.
  3. Allow resin to settle. Do not compact — the bed must expand freely during backwash.
  4. Fill with water to 100–150 mm above the resin bed surface.
  5. Perform an upflow backwash at 8–12 m/h for 10–15 minutes to classify the bed and remove fines.
  6. Drain to the top of the resin bed and commence pre-treatment or first regeneration.

Operating Guide

ApplicationService Flow (BV/h)Exhaustion PointRegenerant
Water softening (Na form)10–25Effluent hardness ≥0.5 mg/L as CaCO₃10% NaCl, 80–120 g NaCl/L resin
Demineralization (H form)8–15Effluent Na⁺ ≥0.1 mg/L or conductivity rise4–5% HCl, 60–80 g HCl/L resin
Iron removal (Fe²⁺, H form)5–10Effluent Fe²⁺ ≥0.05 mg/L4% HCl with 30-min soak step
High-flow industrial softening20–30 (cocurrent)Effluent hardness ≥1.0 mg/L as CaCO₃10% NaCl, 150 g NaCl/L resin

Important operating notes:

  • Free chlorine in feed must be <0.1 mg/L. Chlorine oxidizes the DVB matrix causing irreversible capacity loss (1–3% per 1000 hours of exposure at 0.5 ppm Cl₂). Install a carbon filter or sodium bisulfite dosing upstream if the feed is chlorinated.
  • Maximum operating temperature: 120°C (Na form), 60°C (H form). However, for long-term capacity retention, keep feed below 50°C.
  • Suspended solids in feed should be <5 NTU. High TSS causes fouling between beads and elevated pressure drop. Install a 25–50 µm cartridge filter upstream.
  • For H₂SO₄ regeneration in H form, use stepwise concentration: 0.8% first pass (30 min), then 2–4% second pass (45 min). Avoid direct dosing of concentrated H₂SO₄ — this causes calcium sulfate (CaSO₄) precipitation inside the bead matrix.

Regeneration Procedure

The following procedure applies to Na form softening with NaCl regeneration:

  1. Backwash (upflow): 8–12 m/h for 10–15 minutes. This lifts and reclassifies the bed, removes suspended solids accumulated during service, and loosens compaction. The bed should expand 50–75% above its settled height.
  2. Slow rinse / draw: Reduce upflow to 2–4 m/h for 5 minutes to re-settle the resin before regenerant introduction.
  3. Brine injection (downflow cocurrent): Pass 10% NaCl solution at 3–5 BV/h for 30–45 minutes. Typical dose: 80–120 g NaCl per liter of resin (2–3 kg NaCl per 25 L bag). Brine must be free of iron and suspended solids to avoid fouling.
  4. Displacement rinse (slow rinse): Pass treated water at 3–5 BV/h for 15–20 minutes (2–3 BV) to push residual brine through the bed.
  5. Fast rinse: Pass treated water at 8–10 BV/h until effluent hardness is <0.1 mg/L CaCO₃ and Cl⁻ is at feed level. Typically 3–5 BV required.
  6. Return to service: Open service valve and resume normal flow.

For H form demineralization with HCl regeneration, replace steps 3–5 with: 4–5% HCl at 3–5 BV/h for 30–45 minutes, followed by displacement and fast rinse until effluent pH is ≥5.5.

Regeneration efficiency: Countercurrent (upflow) regeneration with downflow service typically achieves 10–15% higher efficiency than cocurrent, reducing chemical consumption by 20–30%.

Monitoring & Control

ParameterFrequencyTarget
Effluent hardness (Na form)Continuous / end of run<0.5 mg/L as CaCO₃
Effluent Na⁺ leakage (H form)Continuous conductivity<0.05 mg/L Na⁺
Differential pressure across bedDaily<70 kPa; investigate if >100 kPa
Volume per cycle (BV to exhaustion)Each runLog vs. baseline; >10% drop signals fouling
Rinse water Cl⁻ at end of regenEach regen≤ feed Cl⁻ level
Free chlorine in feedWeekly<0.1 mg/L
Total iron in feedMonthly<0.1 mg/L (Fe)
Resin visual inspection6 monthlyNo broken beads >5% by volume

Common Mistakes

  • Using concentrated H₂SO₄ for H-form regeneration: Direct application of concentrated sulfuric acid causes CaSO₄ to precipitate inside pores before it can be rinsed away. Always dilute to <4% and apply in two concentration steps (0.8% then 3–4%) to dissolve calcium progressively.

  • Insufficient backwash before brine injection: Skipping or shortening the backwash step leaves compacted mud balls and channeling paths in the bed. The brine then bypasses sections of resin, causing incomplete regeneration and short run lengths.

  • Chlorinated water in feed without dechlorination: Even 0.2–0.5 ppm free chlorine will oxidize the polystyrene-DVB matrix over months, leading to resin cracking, capacity loss, and TOC leaching into the product. Always dechlorinate before the cation unit.

  • Running the resin in H form with iron in the feed: Fe²⁺ is captured by the resin but upon regeneration can form ferric hydroxide (Fe(OH)₃) precipitates inside the beads if the regen pH momentarily rises. This causes permanent fouling. Feed iron should be <0.05 mg/L; otherwise oxidize and filter iron upstream.

  • Confusing Na form and H form cycle lengths: In H form, the working capacity is lower (0.6–1.0 meq/mL vs. 0.8–1.2 meq/mL) because H⁺ affinity is weaker than Na⁺ selectivity for most cations. Engineers who design H form systems using Na form capacity data will run columns to exhaustion prematurely.

Storage & Handling

  • Shelf life: 2 years in sealed, original packaging under recommended conditions.
  • Temperature: Store at 5–40°C. Protect from freezing — freeze-thaw cycles crack gel beads, causing irreversible capacity loss. If the resin freezes, do not thaw rapidly; warm slowly and inspect bead integrity before use.
  • Container: Keep in original sealed 25 L bags or plastic drums. Do not store in metal containers — iron contamination will load onto the resin.
  • Safety: Non-hazardous as shipped (Na form). H form resin is acidic; wear nitrile gloves and safety glasses when handling. Spent resin from industrial applications may contain heavy metals — dispose per local environmental regulations.
  • Hydration: Never allow the resin to fully dry out. Dehydration causes irreversible shrinkage and bead cracking. If resin has partially dried, re-wet slowly by immersing in demineralized water for 24 hours before loading.

Need a Sample or Quote?

AQUChem supplies all the chemicals mentioned in this article from qualified Chinese manufacturers. Reply within 24 hours.

Send Inquiry

Stay ahead of the market

Get the latest water treatment chemical insights delivered to your inbox.

TelegramWhatsApp