A meaningful, cost-effective solution for polishing reverse osmosis permeate
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1 A meaningful, cost-effective solution for polishing reverse osmosis permeate
2 Electrodeionization or EDI, is a continuous and chemicalfree process of removing ionized and ionizable species from the feed water using DC power. EDI is typically used to polish reverse osmosis (RO) permeate and to replace conventional mixed bed ion exchange, which eliminates the need to store and handle hazardous chemicals used for resin regeneration and associated waste neutralization requirements. The patented DOW EDI module utilizes a unique, leak free, low maintenance spiral wound design containing membrane (see figure 1, below) and ion exchange resins, sealed in a high-strength fiberglass reinforced plastic (FRP) pressure vessel. DOW EDI modules optimize performance, maintain continuous product quality and can produce up to 18 M -cm high-purity water with high silica and boron rejection. Figure 1 1
3 DOW EDI Advantages No Leakage: The DOW EDI module is reliably sealed with high pressure top and bottom end caps, eliminating leakage problems commonly associated with plate and frame designs. Quality Control: Each DOW EDI module is performance and pressure tested prior to leaving our factory to ensure trouble free start-up and operation. Low Maintenance: Unlike plate and frame EDI systems DOW EDI modules do not require tightening of nuts and bolts at installation or the retorquing of bolts on an ongoing basis to prevent leaks. Light Weight Modules, Modular, Easy Access Designs: The DOW EDI modules result in very modular systems that allow easy access and the light weight modules are easy to work with; no special lifting devices are required. Each module comes complete with an individual dilute product water sample port. Cost Effective: The spiral wound DOW EDI modules allow system integrators to build systems that have both lower capital and operating costs when compared to plate and frame EDI devices and are truly a cost-effective replacement for conventional mixed bed ion-exchange. How Does Spiral EDI Work? The DOW EDI modules use electrical current to force a continuous migration of contaminant ions out of the feed water and into the reject stream while continuously regenerating the resin bed with H + (hydrogen) and OH - (hydroxyl) ions that are derived from water splitting. The patented flow process of the dilute and concentrate streams make the DOW EDI module completely unique. Feed water (dilute stream) enters from the bottom of the DOW EDI module and is diverted into vertically spiraled cells known as the D (dilute) chambers. The dilute stream flows vertically through ion-exchange resins located between two membranes (an anion membrane specifically designed to allow migration of only anions, and a cation membrane specifically designed to allow migration of only cations). 2
4 Concentrate enters the bottom of the module through the center pipe and is diverted into spirally flowing cells known as the C (concentrate) chambers. Figure 2 DC current is applied across the cells. The DC electrical field splits a small percentage of water molecules (H 2 O) into hydrogen (H + ) and hydroxyl (OH - ) ions. The H + and OH - ions attach themselves to the cation and anion resin sites, continuously regenerating the resin. Hydrogen ions have a positive charge and hydroxyl ions have a negative charge. Each will migrate through its respective resin, then through its respective permeable membrane and into the concentrate chamber due to its respective attraction to the cathode or anode. Cation membranes are permeable only to cations and will not allow anions or water to pass, and anion membranes are permeable only to anions and will not allow cations or water to pass. Contaminate ions, dissolved in the feed water, attach to their respective ionexchange resin, displacing H + and OH - ions. Once within the resin bed, the ions join in the migration of other ions and permeate the membrane into the C chambers. The contaminant ions are trapped in the C chamber and are recirculated and bled out of the system. The feed water continues to pass through the dilute chamber and is purified and is collected on the outlet of the D chambers and exits the DOW EDI module. All DOW EDI modules product flows are collected and exit the system (see figure 3). 3
5 DOW EDI-210 Performance Specifications Product Water Resistivity Total Exchangeable Anions (TEA) 5 M -cm 25 ppm (CaCO 3 ) 15 M -cm 8 ppm (CaCO 3 ) Based on standard test solution, actual module performance is based on specific feed water conditions. DOW EDI-210 Feed Water Requirements Parameter ph Hardness Dissolved Silica TOC Free Cl 2 Fe, Mn Turbidity, NTU Oxidizer, mg/l Specifications ppm (CaCO 3 ) 0.5 ppm 0.5 ppm 0.05 ppm 0.01 ppm 0.1 None Based on RO permeate feed water. Figure 3: Flow Loop 4
6 Module Operating Conditions Parameter Dilute Product Flow Rate Recovery Rate Inlet Temperature Inlet Pressure (continuous operation) Dilute Pressure Drop Concentrate Inlet Flow Concentrate Pressure Electrolyte Flush Concentrate Conductivity Maximum Electrical Current Maximum Working Voltage Specifications 6.6 to 10 gpm (1.5 to 2.2 m3/h) up to 95% 50 to 100 F (10 to 38 C) 36 to 80 psi (2.5 to 5.5 Bar) 22 to 36 psi (1.5 to 2.5 Bar) 2.2 to 4.5 gpm (0.5 to 1.0 m3/h) 7 to 10 psi (0.5 to 0.7 Bar) less than dilute pressure 0.22 to 0.30 gpm (0.8 to 1.1 lpm) 250 to 600 μs/cm 9A 160V DC Figure 4 5
7 Figure 5 MODULAR DESIGN: Original equipment manufacturers (OEMs) and system integrators can build small or large systems by combining multiple DOW EDI modules. Here are a few examples: EDI 20 EDI 30 EDI 100 EDI 140 EDI 320 6
8 For more information, contact us: North America Latin America Europe Pacific Japan (813) China (86) NOTICE: No freedom from any patent owned by Seller or others is to be inferred. Because use conditions and applicable laws may differ from one location to another and may change with time, Customer is responsible by determining whether products and information this document are appropriate for Customer s use and for ensuring that Customer s workplace and disposal practices are in compliance with applicable laws and other government enac ents. Seller assumes no obligation or liability for the information in this document. NO WARRANTIES ARE GIVEN; ALL IMPLIED WARRANTIES OF MERCHANTABILITY OR FITNESS FOR A PARTICULAR PURPOSE ARE EXPRESSLY EXCLUDED. June 2008 Published in U.S.A. Trademark of The Dow Chemical Company ( Dow ) or an affiliated company of Dow Form No XBBI
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