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K. Thermal Desalination

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    1

    Thermal Desalination

    Antiscalant

    Indonesia Customer Seminar

    June 13 & 14 2012

    Jakarta Indonesia

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    Overview

    Scaling & Its Impact

    Type of Scale in Thermal Desalination

    Factors Influences Scale formation

    Scale Inhibitor Technology Overview

    PC-2040T Features

    Performance

    Comparison with other technology

    Advantages & Benefit

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    Why Scale Occur in Thermal Desalination?

    Condition in thermal desalination generate supersaturatedcondition for some minerals salt in sea water

    Factors:

    Increasing of temperature

    Evaporative concentration

    Release of CO2from the brine which induces further shift ofbicarbonate ion to the carbonate to the hydroxide ion through theincrease in pH

    4HCO3

    2-+ Ca2+ + Mg2+CaCO3(s)

    + Mg(OH)2(s)

    + 3CO2 (g)

    + H2O

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    Scale Formation in MSF

    LP steam

    MP steam

    Seawater

    Seawater

    Distilled water

    Brine discharge

    1-deaerator2-brine heater3-heat recovery4-heat rejection5-vacuum6-brine recirculation pump

    Condensate

    1

    2

    3

    4

    5

    6

    ~30C

    Hard scale (CaSO4) and alkaline scale (CaCO3 and MgOH2) in brine

    heater which has highest temperature

    Calcium carbonate scale and sludge in flash chamber and demister

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    Mainly alkaline scale (CaCO3) on tube surfaces where saturation index is

    the highest .

    Scale Formation in MED

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    Effects of Scaling in the Brine Heater

    Decreased brine temperature at a constant steampressure

    Increased steam pressure to maintain top brinetemperature

    Reduced flow rates for constant top temperature

    Loss of production if no compensation has beenmade for 1 and 3

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    Effects of Scaling in the Heat Recovery Section

    Lower temperature rise through the section and henceincreased steam demand in the brine heater to maintainproduction levels

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    Effects of Scaling in the Demisters

    Physical blocking of the mesh resulting in an increasein vapour pressure drop across the demister. Thisdecreases the steam temperature in the recoverystage, reducing the heat transfer and so reducing theexit temperature of the brine and eventually reducing

    the inlet temperature to the brine heater.

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    Overall Effect of Scaling

    Increased operational costCost of cleaning

    Decreased distillate production

    Decreased system reliability

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    Effect of Scale on MSF Heat Consumption

    Source: Effect of Scaling on Design and Operation of Thermal Seawater Desalination Plant, Dr. Rainer Greggarath, SECRC COMO GmbH

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    Factors Influencing Scale

    Water temperatureAlkalinity

    Thermally dissolved solids Type of dissolved products

    Presence of nucleation particles Silt from intake water

    Flow and velocity

    TimeAlkaline scales (CaCO3, Mg(OH)2) will form more quickly than

    CaSO4(Anhydride). CaSO4x H2O (hemi-hydrate) will form veryquickly.

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    Effect of Temperature on Scaling

    80C 90C 120C

    CaCO3 Mg(OH)2

    CaCO3

    CaSO4

    Mg(OH)2CaCO3

    Increased hardness, more difficult to remove

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    Deposit composition in sea water evaporator

    010

    20

    30

    40

    50

    6070

    80

    90

    100

    60 66 71 77 82 88 93 99 104

    Evaporator water temperature, C

    Compositiono

    fscale

    CaSO4

    CaCO3

    Mg(OH)2

    Nominal temperaturedifference - 27 C

    Concentration factor = 2

    Scale Type vs Temperature

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    Concentrationfactor

    Temperature (C)

    0 50 100 150 200

    1

    2

    3

    4

    5

    CaSO4Scale Formation in MSF Operation

    Data from:Mulford, Scale control in seawater evaporators

    TDS 35

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    Scaling Tendency in MSF

    Source: Fouling Phenomena in MSF Distiller, M, Abdul0Kareem Al-Sofi

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    Effect of Velocity - MSF (CaSO4)

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    Effect of Flow - MED

    In the tubes, the hot vapors arecontinuously passing uniformly atthe same mass and heat flow

    But if the on the outside tubes, ifsea water flow has locallyreduced , supersaturation ofsalts does occur

    - evaporation of water

    - localized continued heating

    - removal of carbon dioxide)

    Source: Effect of Scaling on Design and Operation of Thermal Seawater Desalination Plant, Dr. Rainer Greggarath, SECRC COMO GmbH

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    Effect of FlowMED (No of Tubes Row)

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    Scaling Tendency MSF vs MED

    Parameter MSF MED

    Operating Temperature 90120 0C

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    Scale Control in Thermal Desalination

    CaCO3scale control

    Mg(OH)2 scale control

    CaSO4scale control

    Dispersion capabilities

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    Inhibition of crystal growth

    Crystal modification

    Crystal growth inhibition

    Scale dispersion

    Inhibit adherence

    Scale Inhibitor Activity

    Modesofdefense

    Need Inhibitor that Work in All Fronts

    22

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    Antiscalant Technology Development

    PolyphosphatePhosphonate/Polyacrylate

    PolymaleicAcid

    ModifiedPolymaleic

    Acid

    22

    23

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    Antiscalant Performance Comparison

    23

    Chemistry T

    ToleranceCaCO3

    (Deposition)

    CaCO3(Growth)

    Disper

    sancy

    Mg(OH)2 CaSO4

    Phosphonate Medium Good Mediocre Poor Poor Poor

    Polyacrylate Medium Good Poor Good Fair Poor

    PMA

    Homopolymer

    High Poor Good Mediocre Fair Good

    PMA

    Copolymer

    High Poor Good Good Poor Mediocre

    PMA

    Terpolymer

    High Poor Poor Good Good Poor

    24

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    Antiscalant: The Needs

    Effective scale & deposition control for both soft scale(CaCO3& Mg(OH)2) and hard scale (CaSO4)

    Good dispersancy

    High temperature and calcium tolerance

    Easy to measure/detect On line measurement & control capability

    Cost-effective

    Environmental friendly

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    25

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    PolyphosphatePhosphonate

    / PolyacrylatePolymaleic

    Acid

    ModifiedPolymaleic

    Acid

    NovelAntiscalant

    25

    Antiscalant Technology Development

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    PC-2040T: The Features

    PC-2040T is antiscalant program for the control of softscale (calcium carbonate and magnesium hydroxide) andhard scale (calcium sulfate) in all types of sea waterdistillation plants

    It is specifically formulated for use in high Top BrineTemperature plants where the predominant scale potentialis from calcium sulfate

    PC-2040T is utilizing TRASAR technology for easydetection, monitoring and control (future)

    NSF Approved

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    28

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    PC-2040T: The Chemistry

    Blend of Nalco Patented:Phosphino Carboxylic Acid

    - Stable, reverse proof chemistry

    - Excellent CaCO3and CaSO4and deposition control

    - Good Mg(OH)2scale control

    - Environmental friendly

    High Stress Polymer (HSP)

    - Terpolymer PAA

    - High stress tolerance dispersant for silt, iron, phosphate; etc

    TRASAR technology

    - Tracer material for easy detection & monitoring

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    29

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    PC-2040T: Performance

    Laboratory Testing

    SWCC Plant Trial

    29

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    PC-2040T : Lab Testing CaSO4Inhibition

    0

    70

    %inhibition

    PC-2040Competitor A

    0.5 ppm

    PC-2040 more effective than competitor A in CaSO4inhibition

    Especially at lower dose

    no effect

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    Effect PC-2040T on the Formation of CaSO4

    Dramatic decrease in crystal number(>100000 vs. 2 in treated sample)

    Decrease in crystal size and shape

    CaSO4crystal

    CaSO4crystal grownPC-2040T

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    SWCC

    The Saline Water Conversion Corporation (SWCC) ofSaudi Arabia is one of the most internationally recognizedauthority in the industry for evaluating thermal desalinationantiscalant

    The Research & Development Center (RDC) in Al-Jubailhas been intensively involved in the evaluation ofcommercial scale inhibitor of most of recognized watertreatment companies in the world

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    PC-2040T :SWCC Plant Evaluation

    Phase #1TBT : 110 0C

    Dosage: 2 ppm

    Phase #2

    TBT : 110 0C

    Dosage: 1 ppm

    Phase #3

    TBT : 119 0C

    Dosage: 0.8 ppm

    34

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    SWCC Plant Evaluation Certification

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    PC-2040T Dosage Guide Line (MSF)

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    PC-2040T Additional Dosage: Turbidity

    0

    0,2

    0,4

    0,6

    0,8

    1

    0 1 2 3 4 5 6 7 8 9 10

    Turbidity (NTU)

    Doseincrea

    se(ppm)

    0

    0,2

    0,4

    0,6

    0,8

    1

    0 1 2 3 4 5 6 7 8 9 10

    Turbidity (NTU)

    Doseincrea

    se(ppm)

    37

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    Antiscalant Dosage & Control

    It is necessary to follow very closely the injectionof the chemical by analysis or by feed flow ratecontrol

    Just few hours of under-dosage are enough to

    produce scale in the brine heater with resultantloss of production

    Technology to measure & control antiscalantresidual in real time basis is not available

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    PC-2040T: What is TRASAR?

    Patented Technology from Nalco

    Use widely in boiler and cooling water system

    A specifically chosen ingredient (a tracer) is blended intoNalco product at precise concentration

    Once the product is fed, the tracer is optically excited andeasily detected in system water

    The signal generated by this process is used to monitor

    and control chemical addition on a real time basis

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    PC-2040T: How Trasar Work?

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    PC-2040T: 3DT Automation (Future.)

    PC-2040T

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    Summary PC-2040T Performance

    Effective scale inhibitor & deposition control ofCaCO3, Mg(OH)2and CaSO4at vary operatingcondition

    Broad temperature range

    Broad range of concentration factors

    Outperform antiscalant technology available in themarket

    Capability for having on-line measurement, realtime & control (by Trasar)

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    PC-2040T: Advantages

    Effective scale & deposition control for all type ofscales up to maximum operating condition ofthermal desalination

    Easy to monitor & control

    NSF approved

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    PC-2040T: Benefits

    Cleaner heat transfer surfaceLower steam consumption

    Lower cleaning frequency

    Higher plant efficiency

    Higher plant reliability

    Comply with SHE

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    Thank You !


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