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59 Particulate Control Equipment

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The physical and chemical properties of the particles; ... settling chamber with n horizontal baffles (n flow channels), the settling velocity Vt, ... – PowerPoint PPT presentation

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Title: 59 Particulate Control Equipment


1
5-9 Particulate Control Equipment
  • A number of factors must be determined before a
    proper choice of collection equipment can be
    made
  • The physical and chemical properties of the
    particles
  • The range of the volumetric flow rate of the gas
    stream
  • The range of expected particulate concentrations
    (dust loadings)
  • The temperature and pressure of the flow stream
  • The humidity
  • The nature of the gas phase (such as corrosive
    and solubility characteristics)
  • The required condition of the treated effluent. ?
    this may be the most important piece of
    information for particulate control. Why?

2
  • The condition 7 indicates the collection
    efficiency that must be met, either by a single
    piece of equipment or several operating in
    series.
  • The five basic classes of particulate collection
    equipments
  • Gravity settling chambers
  • Cyclone (centrifugal) separators
  • Wet collectors
  • Fabric filters
  • Electrostatic precipitators

3
5-9-A Gravity Settling Chambers
  • Gravitational force may be employed to remove
    particles in settling chambers when settling
    velocity is greater than about __________.
  • In general, this applies to particles larger than
    _____ if particle density is low, down to _______
    if the material is reasonably dense.
  • What would be needed if we want to use this kind
    of device to remove smaller particles?
  • ?

4
One possible configuration of a gravity settling
chamber
5
  • For a gravity chamber to be effective in
    preventing reentering of the settled particles,
    the gas velocity must be uniform and relatively
    _________, certainly less than _______ and
    preferably less than _________.
  • Theoretically, the minimum particle size that can
    be removed with 100 percent efficiency can be
    derived in the following manner.

6
The fractional collection efficiency for a given
particle size dp
  • For particle sizes below that given by
  • Vt (VH/L) Q/(LW) f(dp)
  • Or dp,min (18uHV/gLtho_p)1/2,
  • The fractional collection efficiency for a given
    particle size dp can be estimated for uniform
    duct flow by the relation

7
  • For settling chamber with n horizontal baffles (n
    flow channels), the settling velocity Vt,
  • The collecting efficiency for this kind of
    settling chamber with n flow channels

8
Remarks on the use of above equation
  • Turbulent within any device,
  • including the settling chamber, causes
    deviations in the particles movement under an
    applied external force,
  • resulting in deviations in the particles
    movement toward the collection surface.
  • ? In the case of the settling chamber, it
    causes deviations in the particles
  • (1) speed and
  • (2) direction of flow
  • when compared to the uniform duct flow model with
    no macroscopic mixing.

9
Limitation of the Uniform Duct Flow Model
  • Therefore, it is important to assess whether the
    flow through a pipe or box (settling chamber) is
    ___________ or __________ (well mixed).
  • In general, if the Reynolds number of the flow
    through the device is less than approximately
    ________, the flow is considered in a laminar
    flow regime.
  • As Re increases from _______ to ________, the
    flow undergoes a transition from laminar to
    turbulent.
  • The flow is considered to be fully turbulent for
    Re ________.

10
For a fully turbulent flow
  • The density and viscosity of the fluid in this
    case are that of air.
  • The diameter to be used in the Re calculation is
    the characteristic or hydraulic diameter of the
    pipe or box.
  • The hydraulic diameter Dh is defined as
  • Dh
  • For the case of a box such as a settling chamber,
  • Dh

11
Example 5-6
  • A settling chamber is operating at ambient
    conditions and has a height and width of 3 m, and
    a horizontal gas velocity of 1 m/s. Determine
    whether the air flow through the device is
    laminar or turbulent.

12
Development of a more realistic modelTo model
flow as well-mixed and a laminar layer next
to the collection tray
13
Example 5-7
  • Determine the length of a simple gravity
    collector required to obtain an efficiency of 90
    percent when collecting particles 50 um in
    diameter and having a density of 2.0 g/cm3. The
    bulk gas velocity is 0.5 m/s and the chamber is 3
    m height.

14
Basic characteristics of gravity settling chambers
  • (1) very low energy cost
  • (2) low maintenance cost
  • (3) low installed cost
  • (4) excellent reliability
  • (5) very large physical size
  • (6) low to very low collection efficiency
  • The last item is particularly true when the dust
    loading contains substantial amounts of fine to
    medium-size particles.
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