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„Dry Foam“ Prevention in Suspension Polymerisation Process

„Dry Foam“ Prevention in Suspension Polymerisation Process...Foam in the Production of PVC 4 Polymerization Reactor Blowdown Vessel Monomer Recovery (VCM, water, surfactants, etc.)

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  • „Dry Foam“ Prevention in

    Suspension Polymerisation

    Process

  • Polymerization processes

    Emulsion Polymerization

    Suspension Polymerization

    Emulsifier:

    • Sodium alkylsulfate

    • Sodium alkylsulfonate

    • Ammonium alkylcarboxy acid

    • Sodium sulfosuccinate

    •Dosage: ~ 1%

    Suspension Aid:

    • Polyvinylalcohol

    • Methylhydroxycellulose

    •Dosage: ~ 0,1%

  • Foam in the Production of PVC

    Polymerization

    Reactor

    Blowdown

    Vessel

    Monomer

    Recovery

    (VCM, water,

    surfactants, etc.)

    Storage

    Tank

    Str

    ipp

    ing

    Co

    lum

    n

    Points where foam may occure

  • Production Problems caused by Foam

    An increased foam build up

    • reduces the space time yield of the reactor

    • may increase fouling in the reactor which results

    in higher maintenance and cleaning costs

    • reduces the cooling capacity and may build up

    layers on the cooling surface of reflux condensers

    • may slow down the speed of demonomerisation

  • Evonik Antifoams for PVC

    Designed for E-PVC and Micro S-PVC:

    -TEGO Antifoam KS 53

    -TEGO Antifoam KS 95

    Designed for S-PVC:

    -TEGO Antifoam KE 600

    -TEGO Antifoam 2280

  • Sintered glass

    To start, the cycliner is filled

    with 1 l of surfactant solution

    + defoamer

    Time is noted when foam

    reaches 2 l mark

    The Sintered Glass Test

  • Test Results in Suspending Agent and

    Emulsifier Solution

    0.1% PVOH solution 1% DBS solution

    TEGO Antifoam KS 53

    TEGO Antifoam KS 95

    TEGO Antifoam KE 600

    TEGO Antifoam 2280

    120 s

    150 s

    600 s

    660 s

    960 s

    840 s

    300 s

    240 s

  • Wet and Dry Foam

    Wet foam Dry foam

  • Gas Bubbles in Pure Liquids

    When the bubble reaches the

    surface it bursts immedeately

    No stable foam can be build

  • Foam Formation

    Introduction and dispersion of

    gas or air - formation of bubbles

    Stabilisation by dissolved

    amphiphilic molecules

    Rising of stabilised bubbles

    Penetration of the surface

    formation of the double

    layer

    1

    2

    3

    4

  • Defoaming: Mechanism Theory

  • Defoaming: Entering-Spreading

    Entering - E

    Spreading - S

    Destabilisation

    + viscous drag on the

    underlying liquid

    E = g w/a + g w/o - g o/a > 0

    S = g w/a - g w/o - g o/a > 0

    wo

    a

  • Dry Foam in S-PVC

    Bubble

    PVC particles

    Dry foam

  • Standard Antifoams can not enter the

    Surface

  • TEGOPREN 5890

    TEGOPREN 5890

    • is based on organomodifies siloxane (OMS)

    • is a 100 % product

    • is selfdispersable. Dilutions are long term stable

    • can be used in food contact application

    (EU Regulation 10/2011)

  • TEGOPREN 5890

    TEGOPREN 5890 will be

    added

  • Tests with PVC Slurry

    Glass pipe

    To start, the cycliner is filled

    with 1000 ml of PVC Slurry

    Antifoam is added hwen the

    foam reaches 1500 ml mark

  • Test Results in Dry Foam

    0

    100

    200

    300

    400

    500

    600

    700

    800

    900

    1000

    0 5 10 15 20 25 30

    ml fo

    am

    time (min)

    TA KS 95

    TA KS 53

    TA KE 600

    TA 2280

    TP 5890