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Mixed Bed Polisher Silica Breakthrough & Sizing Calculator environmental
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Mixed Bed Polisher Silica Breakthrough & Sizing Calculator

Calculate mixed-bed demineralizer polisher service run time to reactive silica breakthrough (<10 ppb), Strong Base Anion (SBA) resin capacity, and chemical regenerant demand.

RO Permeate Feed Water Quality

From RO permeate (typical: 20-100 ppb)
RO permeate ~ 2 to 10 µS/cm
ASME High-Pressure Boiler limit = 10 ppb

Mixed Bed Vessel & Resin Volumes

Type 1 SBA Gel Resin
SAC:SBA ratio ~ 1:1.5
Useful capacity for weak acid anions in polishing service

Service Life & Ultra-Pure Throughput

Run Time to Silica Breakthrough
-- Hours
-- continuous operating days
Treated Throughput Volume
-- m³
-- Million Gallons
Caustic (NaOH) Regenerant
-- kg
100% NaOH basis
Total Mixed Bed Volume: -- Liters
Bed Volumes Treated (BV): -- BV
Effluent Water Quality Quality: 18.2 MΩ·cm (< 5 ppb SiO2)
Acid (HCl 100%) Regenerant: -- kg
--

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Frequently Asked Questions

Why is reactive silica always the first ion to break through a mixed-bed demineralizer?

Strong Base Anion (SBA) resin binds anions in order of chemical selectivity: Sulfate (SO4 2-) > Nitrate (NO3-) > Chloride (Cl-) > Bicarbonate (HCO3-) > Silicate (H3SiO4-). Because silicate is the most weakly ionized species, stronger mineral acid anions displace adsorbed silica, causing a sudden spike in effluent silica concentration while overall electrical conductivity remains ultra-low.

Why is silica strictly limited to < 10 ppb in high-pressure power boilers?

At boiler operating pressures above 1000 psig (70 bar) and temperatures above 500°F (260°C), silica exhibits volatile vapor solubility in high-pressure steam. As steam expands and cools across low-pressure turbine blades, gaseous silica precipitates out as hard, glassy quartz crystals that erode blading, distort aerodynamic profiles, and cause disastrous turbine imbalance trips.

How are the cation and anion resins separated before regeneration?

Because Strong Acid Cation (SAC) resin requires acid (HCl/H2SO4) while Strong Base Anion (SBA) resin requires heated caustic (NaOH), they cannot be regenerated together. During backwash, hydraulic density separation occurs: dense brown SAC resin (SG ~ 1.25) sinks to the bottom, while light amber SBA resin (SG ~ 1.08) floats to the top, allowing split chemical injection through a middle collector lateral.