Membrane Processes Introduction & Bascis August 2010

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    Membrane Separation Processes

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    GIA: Membrane Separation Market to Exceed $11.6 B

    Global Industry Analysts (GIA): June, 2010 Report

    GIA developed new report on"Membrane Separation Technologies: A Global StrategicBusiness Report"

    Reviews market trends

    Competitive scenario

    Product overview Product introduction/launches

    Recent industry activity across global

    Key regional markets

    The study also analyzes market data in terms of value sales

    for regions

    United States, Canada, Japan, Europe, Asia-Pacific,Middle East and Rest of World.

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    Air Liquide

    Celgard LLCCulligan InternationalCompanyCUNO Incorporated

    Degremont SADow Chemical CompanyFilmTec Corporation, E.I.DuPont De Nemours &Co.GE Water & ProcessTechnologiesIon Exchange India Ltd

    Major Global Companies dealing in Membrane Processes

    ITT Corporation

    Koch MembraneSystemsMillipore CorporationNitto Denko Corporation

    Pall CorporationParker HannifinCorporationPraxairSiemens Water Tech.Spectrum LaboratoriesThermaxPermionics

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    Production of Potable water

    Wastewater treatment and processing of water

    Food and Beverages industry

    Replacement of traditional filtration equipment

    Biological Applications

    Power Generation

    Chemicals Separation

    Medical Applications

    Production of pharmaceuticals

    Separation of a wide variety of emulsion, surfactant,

    and chelating mixtures

    Membrane filtration is emerging as a viable alternative toconventional granular media-based processes. There has been asignificant shift in preferences of key industries towards membranesf rom t rad i t iona l f i l t ra t ion & Adsorpt ion dev ices : G IA

    Diversified Applications of Membrane Processes

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    Municipalities in Europe are increasingly employing membraneseparation systems to ensure supply of pure drinking water.

    Moreover, in view of stringent environment regulations, there hasbeen significant increase in the deployment of membranes inw a s t e w a t e r t r e a t m e n t s y s t e m s .

    Rising demand for pure water is expected to boost market growth inAsia-Pacific. India is considered one of the more lucrative and bigger

    markets for membrane separation technologies in Asia-Pacific.With rap id advancements and deve lopment of nove l

    technologies, there has also been significant rise in application areasf o r m em b r a n e t e c h n o l o g y i n r e c e n t t i m e s i n C h i n a .

    Reverse osmosis is one of the fastest growing segments primarily onaccount of growing adoption of water desalination and its ability toachieve very high levels of purity cost-effectively and efficiently.The Middle East has emerged as the most promising market forseawater desalination thereby offering significant prospects forr e v e r s e o s m o s i s .

    Potential for Membrane based Applications

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    High Surface area

    Very much useful when Mixtures of similar Chemical compounds

    to be separated

    Separation of Mixtures of thermally unstable components (since

    no heating is needed). Also HT equipments are not required

    In conjunction with conventional separation methods (Separation

    of azeotropic mixtures before feeding them to a distillation column) When conventional method doesnt work, membranes are useful Huge & Complex machineries are not required

    Complex Instrumentation is not required

    The method does not require constant attention

    Energy savings No Phase change or Interphase MT

    No re-separation is required like Extraction, Leaching etc

    Whenever technology is new profit margin is higher

    Advantages of Membrane Processes

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    Membranes are expensive

    Low Flux

    Membranes are highly selective

    Narrow Operating conditions

    Membrane preparation is complex

    Upper Solid limit is lower (i.e. RO can be used for low solute conn)

    Certain solvents can quickly and permanently destroy the

    membrane

    Certain colloidal solids, especially graphite and residues can

    permanently foul the membrane surface

    The mechanical energy requirement is higher

    Difficult to Separate Highly ViscousLiquids

    Poor Cleaning

    Disadvantages of Membrane Processes

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    Example of Membrane

    Definition of Membrane: A membrane is a discrete, thin Interface that moderatesthe Permeation of Chemical Species in contact with it.

    Shrinking & Swelling of Grapes

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    Semi Permeable Membrane

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    Types of Membranes

    Solid Membranes Organic (Polymer)

    Membranes

    Inorganic Membranes

    Ceramic, Alumina, Zeolite& Silica

    Metallic Membranes

    Noble Metals (Pt, Pd, Au, Ag, Rh),

    Ti Liquid Membranes

    Glass Membranes

    According to Pore Size

    Porous Membranes

    (0.1-10 m)

    Microporous Membranes

    (1-100 nm)

    Non-Porous Membranes

    (0.5-5 nm)

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    Causes of Membrane Separation Processes

    Pore Size of Membrane

    Solubility & Selectivity of Components

    Mobility of Component in Membrane Phase (Depends

    upon membrane chemistry & phase)

    Driving force acting on Individual Component:

    P, T, C, Electric field

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    Membrane Separation

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    2-50 nm pore size

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    2 m10 m

    100 m

    MFUF

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    Types of Membranes

    Solid Membranes Organic (Polymer)

    Membranes

    Inorganic Membranes

    Ceramic, Alumina, Zeolite

    & Silica

    Metallic Membranes

    Noble Metals (Pt, Pd, Au, Ag, Rh),

    Ti Liquid Membranes

    Glass Membranes

    According to Pore Size

    Porous Membranes

    (0.1-10 m)

    Microporous Membranes

    (1-100 nm)

    Non-Porous Membranes

    (0.5-5 nm)

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    Spiral wound - Organic

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    Ceramic Membranes

    Metal Membranes

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    Hollow Fiber Membranes

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    Plate & Frame Membranes

    Tubular Membranes

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    Membrane Separation Processes to be Studied

    Micro FiltrationUltra Filtration

    Nano Filtration

    Reverse Osmosis

    Dialysis

    Electro Dialysis

    Donan Dialysis

    Pervaporation

    Gas Permeation

    Membrane Distillation

    Membrane Contactors

    Membrane Reactors

    Hemo Dialysis

    Blood Oxygenators

    Controlled Drug

    Delivery

    Liquid Membranes

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    Micro Filtration

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    Ultra Filtration

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    Nano Filtration

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    Reverse Osmosis

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    MF

    NFRO

    UF

    Examples of Applications and Alternative Separation Processes

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    Examples of Applications and Alternative Separation Processes

    Process ApplicationsAlternativeProcesses

    MicrofiltrationSeparation of bacteria and cells from

    solutions

    Sedimentation,Centrifugation

    UltrafiltrationSeparation of proteins and virus,

    Break up of oil-in-water emulsionsCentrifugation

    NanofiltrationSeparation of dye and sugar,

    water softening

    Distillation,Evaporation

    Reverse Osmosis Desalination of sea and brackish water,Process water purification

    Distillation,Evaporation,

    Dialysis

    Dialysis Purification of blood (artificial kidney) Reverse osmosis

    ElectrodialysisSeparation of electrolytes from

    non-electrolytes

    Crystallization,Precipitation

    PervaporationDehydration of ethanol and organic

    solventsDistillation

    Gas PermeationHydrogen recovery,

    NG purification, Dehydration andseparation of air

    Absorption,Adsorption,

    Condensation

    Membrane Water purification and desalination Distillation

    Si f M t i l R t i d D i i F d T f M b

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    Size of Materials Retained, Driving Force and Type of Membrane

    Process Separation Range Driving force Type of membrane

    Microfiltration0.1 - 10 m

    microparticlesPressure difference

    (0.5 - 2 bar)Porous

    Ultrafiltration 10 - 100 nmmacromolecules

    Pressure difference(1 - 10 bar)

    Microporous

    Nanofiltration0.5 - 10 nmmolecules

    Pressure difference(10 - 70 bar)

    Microporous

    Reverse

    Osmosis

    < 1 nm

    molecules

    Pressure difference

    (10 - 100 bar)

    Nonporous

    Dialysis< 1 nm

    moleculesConcentration

    differenceNonporous ormicroporous

    Electrodialysis< 1 nm

    moleculesElectrical potential

    differenceNonporous orMicroporous

    Pervaporation< 1 nm

    moleculesConcentration

    difference Nonporous

    Gas Permeation< 1 nm

    molecules

    Partial pressuredifference

    (1 - 100 bar)Nonporous

    Membrane

    Distillation

    < 1 nm

    molecules

    Partial pressure

    differenceMicroporous

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    Applications in Dairy Industry

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    Applications in Dairy Industry

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    Differences between Strainer Filter and Membrane

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    Differences between Strainer, Filter and Membrane

    Separation for more than 10-25

    m size

    Mechanical Operation Driving force: P

    Same size particles cannot be

    separated

    No phase change Solute cannot transfer

    Flux by Darcys Law

    Filter Thickness larger

    Equipments: Plate & Frame,Rotary etc

    Separation from 1 m to 1

    size

    Mass Transfer & MOP, T, C, Solubility, Mobility

    Same size particles can be

    separated

    Phase change May be Solute can transfer

    Flux by Ficks Law

    Membrane Thickness lower

    Equipments: Spiral Wound,Hollow Fiber etc

    Strainers: Solid visible to the Eye i.e. >25 m

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    Membrane: A membrane is a discrete, thin Interface that moderates

    the Permeation of Chemical Species in contact with it.Permeate: The species passes through the membrane and collected at downstream side.

    Flux: Permeate rate per unit cross sectional are of membrane.

    Retentate: The species do not pass through the membrane and retained at frontside.

    Concentrate: Another term for the reject stream.

    Cut : Ratio of Permeate flow rate to Feed Flow rate.Rejection: Ratio of difference between Feed and Permeate concentration to Feed

    concentration.

    Glossary of Membrane Processes

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    Glossary of Membrane Processes

    Selectivity: Ratio of permeability of high permeable species to permeability oflow permeable species.

    For UF: Ratio of Hydrodynamic diameter of Solute to Apparent pore diameter.

    Membrane Module: A unit package in which membrane separation is carriedout also called as Membrane Separator.

    Barrier Layer: This refers to the active layer of membrane material that actuallyseparates the impurities from the product stream or permeate. This barrierlayer is supported by a micro-porous support layer, usually made frompolysulfone, which is cast on a non-woven support material.

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    Concentration Polarization: Accumulation of less permeable component on the

    membrane surface during separation.

    Fouling: Accumulation of collodial, particulates and/or biological contaminants

    on the membrane surface which are coming along with feed.Blinding: If Membrane pore chocked with species of larger diameter

    (considered as impurities in feed) than pore diameter is called Blinding.

    Dope: In the preparation of membrane the solution of polymers from which

    membrane s to be formed called Dope.

    Casting: It is used to indicate either laying down of a polymer solution (dope)

    on support or the spinning of a dope in the form of a hollow fiber.

    Phase Inversion: Basic phenomenon underlying the formation of micro porous

    membrane structure. Exposing a homogeneous polymer solution to certain

    chemical or thermal environment cause phase separation in solution. The

    resultant polymer poor and polymer rich regimes developing pores and

    continuous solid polymer matrix.

    TDS (Total Dissolved Solids): This is a measure, usually given in PPM (Parts

    Per Million) or in milligrams per liter (mg/l) that is used to specify the

    concentration.

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    Osmosis The diffusion of a solvent through a semipermeable membrane from

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    a less concentrated solution to a more concentrated solution.

    Osmotic Pressure: This is the pressure differential that develops as a result of

    a solution containing water and a particular concentration of dissolved solids,

    including minerals and salts.

    Cartridge Filter: Cartridge filters are a widely used and have been utilized for

    water treatment for many decades. Cartridges are usually rated in microns. 40

    microns is considered the largest particle visible to the human eye. Typical

    prefiltration requirements for reverse osmosis systems are around 5 microns.

    Recovery Rate: This term refers to the percentage of water recovered as

    product water from a given quantity of feed water.Anion A negatively charged ion.Cation A positively charged ion.Ion An atom or group of atoms with an electrical charge that is positive(cation) or negative (anion) as a result of having lost or gained electrons.

    Auto flush An automatic temporary increase in the reject flow. This helpsprevent membrane fouling.

    Scale The mineral deposits that can coat the insides of boiler or the surfacesof RO membranes. It consists mainly of calcium carbonate, which precipitates

    out of solution under certain conditions of pH, alkalinity and hardness.

    MSP with Tubular modules

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    MSP with Tubular modules

    MSP with spiral-wound modules High Throughput

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    MSP with spiral-wound modules High Throughput

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    Overview of different Membrane Processes

    Micro & Ultra Filtration

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    Micro & Ultra Filtration

    Micro & Ultra Filtration

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    Micro & Ultra Filtration

    Reverse Osmosis

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    Osmosis

    Reverse Osmosis

    Gas Permeation

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    Gas Permeation

    Gas Permeation

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    Gas Permeation

    Dialysis

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    Dialysis

    Electrodialysis

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    Electrodialysis

    Feed

    Pervaporation

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    Pervaporation

    Pervaporation

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    p

    Pervaporation

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    p

    Membrane Contactor

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    Membrane Distillation

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    Membrane Distillation

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    Membrane Distillation

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    Hemodialysis

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    y

    Hemodialysis

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    Membrane Reactors

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    Pd Membrane reactor for Methane Reforming

    Membrane Reactors

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    CO + H2O CO2 + H2

    Membrane Reactors

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