Separation Vs Filtration - PowerPoint PPT Presentation

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Separation Vs Filtration

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NORSOK. 20.155 to 30.233. Design. V94.3. 28 – PowerPoint PPT presentation

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Title: Separation Vs Filtration


1
Separation Vs Filtration
  • Removal by Inertial Impaction
  • Uses the energy from the fluid
  • Removal of larger particle size, 10 micron and
    above
  • Used for bulk removal
  • Removal by Direct Impaction
  • Uses Filter Media with close mesh size (and
    inertial device)
  • Removal of fine particle size, typically 1 micron
    and above
  • Used for both bulk aerosol removal

2
Factors Influencing Gas Filtration Selection
  • Removal Efficiency, location of the filter system
  • Properties of Gas, flow rate
  • Type and quantity of Particle to be removed and
    its properties
  • Operating pressure temperature
  • Type of controls required
  • Pressure drop allowed Turn-down Ratio
  • Material specification

3
Information Required
  • Location Removal Efficiency
  • Type Property of Contaminant Oil in
    particular
  • Gas Property or MW or Sp. Gravity
  • Flow Rate Min / Max
  • Operating Pressure Min / Max
  • Operating Temperature Min / Max
  • Allowed pressure drop
  • Liquid Holding time or capacity
  • Controls required
  • Configuration Horizontal, Vertical, In-line
  • Special material, if any, required

4
Flow Rate
  • Flow rates converted to ACFM or ACFS.
  • At low pressure ACFM will be higher than at High
    Pressure.
  • At high temperature ACFM is higher than at low
    temperature .
  • SCFM and LB/Hr are independent of pressure and
    temperature while ACFM is sensitive to these.

5
Operating Pressure
  • Low pressure increases the ACFM.
  • High pressure increases cost of separator.
  • High pressure increases density resulting in
    decrease in density difference between gas
    liquid and separation becomes more difficult.
  • Drop in allowable shear force and therefore
    reduced velocity. (rV2)
  • Mass flow rate is independent of pressure for a
    given SCFM.

6
Operating Temperature
  • High Temperature increases ACFM.
  • Influences filter element selection.
  • Influences material selection.
  • Influences control instrument selection.
  • Mass flow rate is independent of temperature for
    a given SCFM.

7
Gas Property
  • Composition influences MW.
  • MW decides specific gravity.
  • Specific gravity influences density based on
    operating pressure and temperature.
  • Density influences velocity through the device
    and the size of the Separator.
  • ACFM is independent of MW for a given SCFM.

8
Type of Contaminant
  • Solids, solids and liquids, liquids.
  • Nature of liquid and volume flow rate, Liquid/Gas
    ratio,
  • Density of liquid.
  • Viscosity of the liquid, if high drainage would
    be a problem, may require a mesh pad foe vane
    packs.
  • Surface tension, if shear stress drops,
    re-entrainment would occur.
  • Above factors dictate size, type of device and
    controls required.

9
Removal Efficiency
  • Inertial Separators typically can remove only 10
    micron and above.
  • Vane will not guarantee removal of solids.
  • If heavy oil is present may require mesh pad
    addition.
  • Re-entrainment occurs at high gas velocity,
    dictates size of filter vessel.
  • Influences filter element selection .
  • Influences configuration.

10
Liquid Holding
  • Location of the system.
  • Is slug involved.
  • Type of Draining Automatic or Manual.
  • Volume flow rate of liquid.
  • Above factors decide sump capacity type of
    control.
  • Sump capacity dictates separator size.

11
Compressibility Factor
  • Compressibility Factor, Z, corrects the gas
    density for deviations from the ideal gas law.
  • Use client specified value or use TEMA or
    Chemical Engineers Handbook.
  • Use 1 if details not known.

12
Design Considerations
  • Inlet velocity not to exceed rV2 4500, based on
    TEMA guidelines.
  • Inlet to have a baffle to break the momentum and
    to protect against slugs.
  • If oil or other liquid contaminants expected,
    vane pack with/without mesh pad or multi-cyclone
    type device required.
  • If vane is selected for first stage and if inlet
    is directly in front, to use agglomerator .
  • Holding capacity required.
  • Size of inlet/outlet to vessel size.

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