the theory of reverse osmosis (ro)
DESCRIPTION
This presentation talks about the first commercial membranes starting in the 1960's and then moves on to discuss how membranes work and the processes required to clean them.TRANSCRIPT
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Theory of Reverse Osmosis Theory of Reverse Osmosis MembranesMembranes
Dilute Solution
Concentrated Solution
Osmotic Pressure
Dilute Solution
Concentrated Solution
Pressure
RO Membrane
RO Membrane
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Types of Reverse Osmosis Types of Reverse Osmosis MembranesMembranes
First commercially available membrane was First commercially available membrane was an asymmetric Cellulose Acetate (CA) an asymmetric Cellulose Acetate (CA) membrane (early 60’s)membrane (early 60’s)
Thin film composite (TFC) polyamide Thin film composite (TFC) polyamide membranes were an improvement on the membranes were an improvement on the original CA membranesoriginal CA membranes
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TFC vs. CA MembranesTFC vs. CA Membranes
Wider pH range 2 to 12 vs. 4 to 6Wider pH range 2 to 12 vs. 4 to 6 Lower operating pressure (1/2)Lower operating pressure (1/2) Higher rejections 99% vs. 96%Higher rejections 99% vs. 96% CA more resistant to chlorineCA more resistant to chlorine
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Feed Water ConsiderationsFeed Water Considerations
Scaling PotentialScaling Potential- Sparingly soluble compounds (CaCO- Sparingly soluble compounds (CaCO33, , Fe(OH) Fe(OH)33))- Alkalinity- Alkalinity
Silt Density Index (SDI)Silt Density Index (SDI) TurbidityTurbidity Biological foulingBiological fouling pHpH
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Prevention of Scale FormationPrevention of Scale Formation
Acid additionAcid addition Reduction of recoveryReduction of recovery Scale inhibitor additionScale inhibitor addition SofteningSoftening Preventative cleaningPreventative cleaning
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SDI and Turbidity ReductionSDI and Turbidity Reduction
Media filtrationMedia filtration Cartridge filtrationCartridge filtration Coagulant addition prior to coarse filtrationCoagulant addition prior to coarse filtration UltrafiltrationUltrafiltration
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Biological FoulingBiological Fouling
Chlorine additionChlorine addition OzoneOzone DechlorinationDechlorination
– Activated carbonActivated carbon– Sodium MetabisulfiteSodium Metabisulfite
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System DesignSystem Design
Feed water analysisFeed water analysis Product water requirementsProduct water requirements Required flow Required flow Materials of constructionMaterials of construction Level of instrumentationLevel of instrumentation
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Typical Flow SchematicTypical Flow Schematic
RO Membrane
RO Membrane
From Pressurized Treated Water Storage
(if using a repressurization pump. Plug connection if
using a bladder tank for storage)
LPS 01
LPS - Low Pressure Switch P I - Pressure Indicator F I - Flow Indicator
To Treated Water Storage
Water to be Treated
P I 03
SP7500 - 1 Membrane installed SP15000 - 2 Membranes installed SP22500 - 3 Membranes installed
FI 01
FI 02
FI 03
P1
V3 V4
CV3
SV1PI 02
CV2
CV1
Set @ 50 psi
CV4
CV5
SP2
SP1
230 VAC, 20A, 1Ø 2 lines, Neutral & GND SP Series with NF membranes 1.5 Hp SP Series with RO membranes 2 Hp
Signal From Pressure or Level SwitchesControl Panel
V5 CV7
CV6
SV2
*
* Signal from feed tank can be substitued
SV3
V1
SP3P I 04
PI 01
5044 South Service Rd., Burlington, Ontario, Canada L7L 5Y7 Tel: (905) 632-4968 Fax: (905) 632-6730
Scale:
Project:
Drawing #
Drawn by:
Rev #
Date:
THIS DOCUMENT CONTAINS PROPRIETARY INFORMATION. DO NOT COPY WITHOUT PRIOR WRITTEN APPROVAL FROM ASLAN TECHNOLOGIES.
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Designed by:
Approved:
File Name:Rev Description By Date
None
970501
99289
MM CW
99289I02
3System P&ID
SP Series Reverse Osmosis System
990904MMGeneral revisions1
001203MMAs built2
010217MMProper indication of SP3 location3
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System Operation & MaintenanceSystem Operation & Maintenance
Verification of pretreatment functionalityVerification of pretreatment functionality Setup of proper system flow dynamicsSetup of proper system flow dynamics Log operational dataLog operational data Normalize dataNormalize data Perform cleanings and maintenance as Perform cleanings and maintenance as
requiredrequired