Double Pass RO System For EDI Pretreatment

Double Pass RO System For EDI Pretreatment

This double pass reverse osmosis unit is engineered to reduce total dissolved solids, silica, and conductivity to ultra-low thresholds required for stable electrodeionization operation. By routing single-pass permeate through an intermediate tank into a second high-pressure pump and membrane array, the configuration eliminates residual ions to protect downstream electrodeionization modules from scaling and voltage spikes.

System Overview

 

This double pass reverse osmosis unit is engineered to reduce total dissolved solids, silica, and conductivity to ultra-low thresholds required for stable electrodeionization operation. By routing single-pass permeate through an intermediate tank into a second high-pressure pump and membrane array, the configuration eliminates residual ions to protect downstream electrodeionization modules from scaling and voltage spikes.

 

Technical Specifications

 

Parameter

Design Specification

Permeate Conductivity

Less than 2.0 uS/cm at 25 deg C

TDS Rejection Rate

Greater than 99.5 percent overall

Silica Rejection

Greater than 99.9 percent reduction

Recovery Rate

75 to 85 percent

Design Pressure

300 psi first pass / 150 psi second pass

 

Fluid Dynamics and Treatment Process

 

First-Pass Pressurization: Raw pretreated water enters the primary high-pressure pump to overcome osmotic pressure across spiral-wound polyamide elements.

 

Permeate Isolation: Initial permeate collects in an intermediate stainless steel tank while concentrated reject discharges to drain.

 

Second-Pass Polishing: An interstage booster pump feeds collected permeate into the secondary membrane array without anti-scalant replenishment.

 

Quality Monitoring: Polished permeate flows through inline resistivity sensors before reaching downstream electrodeionization systems.

 

Advanced System Configuration

 

Interstage pH Adjustment: Optional caustic soda injection converts carbon dioxide into bicarbonate ions for enhanced silica and boron rejection.

 

Interstage Degasification: Membrane contactor integration strips dissolved carbon dioxide gas prior to final membrane polishing.

 

Instrumentation Interlocks: Automated conductivity diversion valves reject off-spec permeate before reaching sensitive modules.

 

Recirculation Loops: Integrated flush circuits and automated clean-in-place connections support periodic membrane sanitation.

 

Feedwater Quality Parameters

 

Silt Density Index: Less than 3.0 measured over 15 minutes to protect membrane channels from particulate blockage.

 

Free Chlorine: Less than 0.1 mg/L maintained via activated carbon or sodium bisulfite dosing to prevent polymer oxidation.

 

Suspended Solids: Less than 1.0 mg/L verified through upstream multimedia or ultrafiltration pretreatment steps.

 

Temperature Range: Operational capability between 10 and 35 degrees Celsius, optimized at 20 degrees Celsius.

 

Permeate Quality Standards

 

Silica Concentration: Maintained below 20 ug/L to prevent fouling of ion-exchange resins inside chambers.

 

Sodium Levels: Reduced below 50 ug/L to minimize ionic load on direct current regeneration fields.

 

Total Organic Carbon: Kept below 500 ppb to prevent biological film accumulation on resin beds.

 

Hardness Levels: Calcium and magnesium reduced to undetectable limits, eliminating cathode scaling.

 

Engineering Value for Integration

 

Voltage Stabilization: Lower feed conductivity prevents excessive electrical resistance, reducing power consumption during continuous regeneration.

 

Extended Lifespan: Eliminating trace hardness and silica spikes prevents irreversible scaling, extending stack lifespans beyond five years.

 

Resin Protection: Minimizes chemical cleaning frequency of mixed-bed ion exchange resins, reducing maintenance downtime.

 

Effluent Consistency: Provides stable, low-conductivity water regardless of seasonal raw water mineral fluctuations.

 

Primary Industrial Applications

 

Power Generation Boilers: Produces demineralized water for high-pressure utility boilers to prevent turbine blade scaling.


Pharmaceutical Production: Generates feedwater meeting pharmacopeia standards for distillation without hazardous acid regeneration.


Microelectronics Manufacturing: Supplies ultra-low conductivity rinse water for semiconductor wafer fabrication lines.


Chemical Processing: Delivers high-purity water utilized as a solvent or reaction medium in specialty synthesis.

 

Selection Guide

 

Capacity Sizing: Calculate total daily volume requirements including peak hourly demand and continuous feed flow rates.


Feedwater Mapping: Match membrane polymer chemistry against specific ion concentrations and organic loading in water analysis reports.


Energy Evaluation: Balance high-flux membrane selection against pump horsepower requirements to minimize long-term electrical expenses.


Footprint Assessment: Measure mechanical room dimensions to select between vertical multi-stage pumps and compact horizontal skids.

 

Customization Parameters

 

Frame Materials: Available in 304 stainless steel, 316L stainless steel, or epoxy-coated carbon structural steel skids.

 

Membrane Selection: Configurable with fouling-resistant elements for wastewater reuse or high-rejection elements for well water.

 

Pumping Variations: Integration of variable frequency drives on high-pressure pumps to match variable flow demands.

 

Automation Platform: Programmable logic controllers paired with touch screen interfaces compatible with standard communication protocols.

 

Quality Assurance and Testing

 

Pressure Testing: All pressure vessels, high-pressure tubing, and welded manifolds undergo testing at 1.5 times design pressure.

 

Traceability: Membrane elements, pressure vessels, and instrumentation sensors are sourced from verified manufacturers with test reports.

 

Factory Acceptance Testing: Complete skids undergo wet testing using simulated feedwater to verify pump performance and sequence logic.

 

Electrical Inspection: Control panels are built according to industrial standards, verifying proper grounding and circuit protection.

 

Frequently Asked Questions

Q: Why is an interstage break tank required?

A: An intermediate tank or direct boosting configuration separates the hydraulic pressure zones of both passes, ensuring stable suction for the second-stage pump.

Q: Can the system operate without anti-scalant?

A: Because the first pass removes scale-forming minerals, the second pass often operates without anti-scalant injection if first-pass permeate hardness is negligible.

Q: What is the typical electrical power requirement?

A: Power scales with permeate capacity, ranging from 7.5 kW for small units up to 45 kW for large industrial installations.

Q: How often is chemical cleaning required?

A: With proper upstream pretreatment and stable SDI levels, second-pass membranes typically require cleaning every 12 to 18 months.

Q: What maintenance keeps feedwater within specification?

A: Routine tasks include monitoring normalized permeate conductivity, verifying dosing rates, replacing cartridge filters before differential pressure exceeds 1.5 bar, and calibrating resistivity meters.

 

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