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    Reverse Osmosis and DeionizationSystems for Aquaria

    Thoram Charanda

    Sr. ChemistWalt Disney World Co.

    Life Support

    Lake Buena Vista, FL

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    1st AQUALITY Symposium, April 2 - 7, 2004, Oceanario de Lisboa, Portugal

    Reverse Osmosis and Desalination

    1. Theory of Osmosis

    2. Typical Industry Applications of ReverseOsmosis (RO), Desalination

    3. Practical Considerations for RO in Aquaria

    4. Designing an RO System for a Salt Water

    Exhibit

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    Theory of Osmosis

    Fresh

    Water

    Sea

    Water

    H2O

    Initial Condition

    Fresh

    Water

    Sea

    Water

    (diluted)

    H2O

    Equilibrium

    H2O

    Semipermeable

    Membrane

    Fresh

    Water

    Sea

    Water

    H2O

    Pressure

    Reverse Osmosis

    The Osmotic Pressure, , is defined as: = MRT

    For sea water at 35 ppt, is about 350 psi.

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    1st AQUALITY Symposium, April 2 - 7, 2004, Oceanario de Lisboa, Portugal

    Key Terms in RO Systems

    PermeateThe purified product water exiting the

    system.

    ConcentrateThe concentrated salt solution exiting the

    system. In some system designs this outflow is returnedto the aquarium for salt recovery.

    Feed FlowThe total flow rate of the source water

    pumped in the system.

    Recovery - The percentage of permeate achieved in a

    system, % Recovery = permeate flow/feed flow x 100.

    RejectionThe percentage of dissolved solids removed

    from the source water by the membrane.

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    RO Membrane Filter Detail

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    Industrial Applications of RO

    Systems

    Purification of potable or fresh water sources: Purified, very lowTotal Dissolved Solids (TDS) water is produced for various uses. Inthe aquarium industry it can be used for:

    - Make up water in fresh and salt water aquariums

    - As a pure water base for artificial salt water systems

    - As a non-scaling/spotting wash or rinse water for aquarium exhibitwindows.

    Desalination of Sea Water:

    - Production of potable drinking

    - Source water for combustible turbine power plants

    - Irrigation and non-potable utility water uses

    - It can also be used as a salt recovery system for closed-filtration seawater aquaria

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    RO System for Fresh Water

    300 to 1,000 gallon per day

    RO System

    Requires a reservoir tank, high

    level shut-off switch and

    delivery pump

    Pre-Filtration: Requires a 5-micron sediment filter and a

    GAC filter to remove any

    chlorine residual and organics

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    Desalination RO Systems

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    Design Considerations for a Salt

    Recovery RO System Consider your feed water source: Natural or Artificial Sea Water.

    Identify the typical range of the water chemistry parameters.

    pH

    Temperature Salinity

    Silt Density Index (SDI)

    Silica

    Level of Particulates

    Presence of Organics or Residual Oxidizers What is the desired rate of permeate (fresh water) removal from your

    system? This will dictate the required feed flow rate for the ROsystem.

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    Design Considerations for a Salt

    Recovery RO System Consider any future requirements for system upgrade in fresh water

    removal capacity, e.g. system can accept an additional membrane,

    high pressure pump is slightly oversized.

    Identify the best location in the aquarium filtration pathway to connect

    the feed source.

    Consider connecting the return filtration line post ozonation.

    Identify pre-filtration requirements:

    GAC filter to removal residual oxidants, e.g. bromine, ozone Additional particulate filters for highly loaded systems

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    ROSA 5.4 Reverse Osmosis Design

    Software

    Specialized software can be used to assist in the initial

    design and membrane performance parameters required for a

    successful salt recovery system.

    A freeware program is offered by DOW Chemical called

    ROSA 5.4, that offers the ability to calculate the required

    feed, permeate and concentrate rates based on the feed water

    chemistry and a given sea water RO membrane type.

    The URL for this program is www.filmtec.com.

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    5,000 gpd RO System at Shark Reef, Typhoon

    Lagoon

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    Shark Reef Salinity Recovery: RO System

    25

    26

    27

    28

    29

    30

    31

    32

    0 2 4 6 8 10 12 14 16 18 20

    Days

    Salinity

    400,000

    425,000

    450,000

    475,000

    500,000

    525,000

    System

    Volume(gal)

    Salinity Volume (gal)

    Initial Salinity = 30.4

    Recovered Salinity = 30.3

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    Deionization Water Filtration Systems

    1. Principles of Deionization (DI)

    2. Applications for DI Water

    3. Water Chemistry Parameters and Considerations

    for a DI System

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    Ion Exchange Beads

    Ion exchange beads are typically

    constructed of a polymeric resin or gel

    with an average diameter of 0.3 to 1.2

    millimeters. The beads can have either

    cationic or anionic functional groups

    attached to the surface.

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    Types of Ionic Exchange Resins

    Strong Acid Resins

    - contain functional groups of R-SO3H on the

    polymeric resin

    Weak Acid Resins

    - contain functional groups of R-COOH

    Strong Base Resins

    - contain functional groups of R-OH

    Weak Base Resins

    - contain functional groups of R-NH3

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    Strong Acid Cationic Resin

    Polymeric ResinR-SO3-H

    Na+

    K+

    Cu2+

    Mg2+

    Ca2+

    Typical Cations

    Metals

    Fe2+

    Zn2+

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    Applications for DI Water

    Analytical grade water for laboratory use

    Essentially salt and micro nutrient free water that can be

    used to make artificial sea water Replenish system water loss due to evaporation

    Makeup of specialized water quality environments, ie.

    natural waters with very low TDS and specific

    concentrations of cations

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    Design Engineering of DI Systems

    Identify the source water for the DI system

    Analyze for the key water chemistry parameters:

    pH

    Free and Total ChlorineTotal Dissolved Solids (TDS)

    Identify the intended volume of DI required per day

    A GAC prefilter is required to remove residual chlorine

    and dissolved organics-typically sized from 0.0283 to 0.057 m3 (or 1 to 2 ft3)

    Plan for a reputable company to provide an exchange

    service for the mixed resin beds and GAC filter

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    Mixed bed ion exchange capacity = 353,357 grains per m3

    10,000 grains per ft3

    Design Engineering of DI Systems

    Example: Your source water is potable city water and you require up

    to 400 liters per day of DI water.

    Source water TDS: 200 ppm

    Equivalent grains per gallon = 11.7 gpg (divide TDS by 17.1)

    Planned DI resin exchange frequency = 30 days

    Minimum required amount of mixed bed resin = 0.105 m3

    3.71 ft3

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    Summary

    Reverse osmosis systems are a good design choice where:

    - Moderate (2,000 liters) to large (+18 m3) volumes of water arerequired per event and there is sufficient space for the purified waterreservoir

    - Desalinated water source for utilities and as a purified water sourcefor DI analytical laboratory grade water

    - Desalination system for salt recovery

    Deionization systems are a good design choice where:

    - A relatively fast flow rate (> 35 Lpm) of pure water is required

    - Only cost effective for relatively small exhibits, < 2,000 liters

    - Analytical laboratory grade water

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    Acknowledgements

    Dow Chemical Company

    GE Water Technologies

    Reverse Osmosis of South Florida

    US Filter Corporation

    David Cohrs, National Aquarium in Baltimore

    Kent Semmen, Brooksville Zoo

    Eric Kingsley, Monterey Bay Aquarium