Reverse Osmosis Presented by Dick Youmans, CWT David H. Paul, Inc. 2 Outline for this Presentation 1) Define Osmosis and Reverse Osmosis 2) Types of Membranes and Their Characteristics 3) Manufacturing Process for the “Membrane” 4) Demonstration: Rolling One Of Our Own 5) Understand Water Flow Through an Element 6) Understand Water Flow Through Pressure Vessels 3 Definition of Osmosis Osmosis is the process where a solvent (usually water) passes from a dilute solution into a more concentrated one by moving through a semipermeable membrane which selectively allows the passage of the solvent, but restricts the passage of the solute (dissolved solids). 4 Osmosis Time = Zero Equilibrium Time Less Concentrated Pure Concentrated Solution Water Solution Pure Water 5 Osmosis 6 Osmosis Time = Zero Equilibrium Time Less Concentrated Pure Concentrated Solution Water Solution Pure Water 7 Types of Pressures Involved 1) Osmotic Pressure 2) Applied Pressures A) Hydrostatic or Head Pressure B) Pump or External Pressure 3) Net Driving Pressure 8 Osmotic Pressure Time = Zero Equilibrium Time <1000 ppm 1000 ppm TDS Pure Water TDS Pure Water Osmotic Pressure 10 psi 9 Approximate Osmotic Pressures • TDS in ppm • Osmotic Pressure in psi (bar) 100 ppm 1 psi (.069Bar) 1,000 ppm 10 psi (.69 Bar) 5,000 ppm 50 psi (3.45 Bar) 10,000 ppm 100 psi 6.9 Bar) 15,000 ppm 150 psi (10.35 Bar) 10 Net Osmotic Pressure Time = Zero 1000 ppm 1000 ppm TDS TDS Equilibrium Time 1000 1000 ppm ppm TDS TDS Osmotic Pressure 10 psi 10 psi Net Osmotic Pressure is 0 psi 11 Applied Pressure Time = Zero Equilibrium Time 2.3 feet 2.3 feet 2.3 feet 2.3 feet Pure Water Pure Water Pure Water Pure Water Hydrostatic Pressure 1 psi No Change 1 psi Net Pressure is 0 psi 12 Applied Pressure Time = Zero Equilibrium Time 4.6 feet Pure Water 2.3 feet Pure Water 3.45 feet 3.45 feet Pure Water Pure Water Hydrostatic Pressure Hydrostatic Pressure 1 psi 1.5 psi 2 psi Net Pressure is 1 psi 1.5 psi Net Pressure is 0 psi 13 Osmosis Stopped Time = Zero Equilibrium Time 7 psi 1000 ppm 7 psi 300 ppm TDS 1000 ppm 2.3 feet 300 ppm TDS TDS Osmotic Pressure 3 psi 10 psi Applied Pressure 8 psi 1 psi 11 psi 11 psi TDS Totals Net Driving Pressure 0 psi 14 Reverse Osmosis Equilibrium Time Time = Zero 100 psi 1000 ppm TDS 300 ppm 2.3 feet TDS Osmotic Pressure 3 psi 10 psi Applied Pressure 101 psi 1 psi Totals 104 psi 11 psi Net Driving Pressure 93 psi 15 Definition of Reverse Osmosis Reverse Osmosis occurs when sufficient external pump pressure is applied to the more concentrated solution to overcome osmotic and hydrostatic pressures to reverse the osmotic reaction causing water to flow from the concentrated solution to the dilute solution. 16 Definition of Net Driving Pressure Reverse Osmosis Unit 3 Feed Water 4 Permeate Flow 80 GPM Flow 100 GPM 1 2 Concentrate Flow NDP = Feed Water Pressure (1) + Osmotic Pressure of Permeate (3) - Permeate Back Pressure (4) - Osmotic Pressure of Feed Water (2) 20 GPM 17 Major Types of Membranes Configurations 1) Tubular (inside out) 2) Hollow Fiber (outside in) a) Shell & Tube Heat Exchanger 3) Spiral Wound a) Cellulose Acetate b) Thin Film Polyamide Composite 18 Spiral Wound RO Membrane Element 19 Cellulose Acetate Membranes 1) More Expensive than Thin Film Membranes 2) Typical salt rejection of 96% 3) Typical operating pressures of 400 to 700 PSI 4) Optimum pH operating range of 4.8 to 6.5 5) Good Chlorine Tolerance 20 Thin Film Composite Membranes 1) Less expensive than cellulose acetate membranes 2) Typical salt rejection of 97 to 98% 3) Typical operating pressures of 200 - 300 PSI 4) Wide pH operating range of 2 - 10 5) Very Low Chlorine Tolerance 6) Less susceptible to compaction due to lower PSI 21 Reverse Osmosis Membrane Sheet Components Cellulose Acetate Membrane (Asymmetric) Dense Skin Porous Support Backing Material Thin Film Composite Membrane Semipermeable Membrane Porous Support Backing Material 22 How Do RO Membranes Reject Three Modes of Rejection 1) Ionic Charge 2) Molecular Weight 3) Physical Size 23 Rolling Your Own Reverse Osmosis Membrane Element 24 Materials Needed 25 Fold Membrane in Two With 1/2 Inch Difference. Insert the Permeate Carrier 26 To Simulate Glue Lines, Tape the Edges of the Folded Sheet to Form the Envelope or “ Leaf ”. 27 Tape Permeate Tube to “ Leaf “, Lay Feed Water Spacer on Top and Roll Your Element 28 Continue Rolling Until Finished 29 Pick a Colored Tape and Wrap a Shell Around Your Element 30 Install the Brine Seal & Your Done. 31 Reverse Osmosis Membrane Element 32 Reverse Osmosis Water Flow Definitions Permeate Flow Out Feed Water In Concentrate Flow Out 33 Reverse Osmosis Versus Traditional Filtration 1) Filtration Water Flow in Water Flow out 2) Reverse Osmosis (Cross Flow Filtration) Permeate Flow Out Water Flow In Concentrate Flow Out 34 Does Reverse Osmosis Require Pretreatment? 1) Settling Basins for Silt & Mud 2) Filtration for suspended solids 3) Ion Exchange for Hardness Salts 4) Demineralization for Anions & Cations 5) Activated Carbon Filters for Organics Permeate Quality Required Dictates Pretreatment 35 Reverse Osmosis Typical Residential Well Water Installation Well Water Cloth Filter Carbon Filter Reverse Osmosis Drinking Water Concentrate 36 Reverse Osmosis Putting Elements into a Pressure Vessel Pressure Vessel Element Feed Water In Inter-connectors Permeate Out Element Element Brine Seals Element Concentrate Out 37 Reverse Osmosis What is a Pressure Vessel? 38 Reverse Osmosis Putting Elements into a Pressure Vessel Pressure Vessel Element Feed Water In Inter-connectors Permeate Out Element Element Brine Seals Element Concentrate Out 39 Water Flow Through Pressure Vessels Feed Water *Concentrate to Drain* Permeate to Storage 40 Concentrate Waste Disposal in the United States Evaporation Ponds, 2% Spray Irrigation, 2% Zero Liquid Discharge, 0% Deep Well Injection, 9% Discharge to Sewer, 42% Source: Concentrate Disposal, by Irving Moch, Jr. AMTA’s Pretreatment Solutions, Winter 2006/2007 Surface Water Discharge, 45% 41 Single Stage Reverse Osmosis Unit (50% Recovery) Permeate 50 GPM Feed 100 GPM Concentrate 50 GPM 42 Two Stage Reverse Osmosis Unit (75% Recovery on a 4 -2 Array) 50 GPM 75 GPM 5 TDS 6.7 TDS 25 GPM 10 TDS 100 GPM 100 TDS 25 GPM 380 TDS 50 GPM 1st Stage 195 TDS 2nd Stage 43 Two Stage Reverse Osmosis Unit (75% Recovery on a 6 - 3 Array) 2nd Stage 1st Stage 44 Two Stage Reverse Osmosis Unit (75% Recovery on a 30 - 15 Array) 2nd Stage 1st Stage 45 Two Pass Reverse Osmosis Unit (25% Recovery ) 50 GPM 25 GPM 5 TDS 0.25 TDS 100 GPM 100 TDS 25 GPM 10 TDS 50 GPM 195 TDS 46 Two Pass Reverse Osmosis Unit 47 Two Pass Reverse Osmosis Units 1) Booster Pump Between Passes 2) Storage Tank Between Passes 3) Caustic Soda Feed Between Passes 48 Two Pass / Two Stage Reverse Osmosis Unit 4 -2 Array 1st Pass / 2 – 1 Array 2nd Pass 1st Pass 2nd Pass 2nd Stage 2nd Stage 1st Stage 1st Stage 49 Hopefully, Time for Questions Thank You, Dick Youmans, CWT 50
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