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PROCESS DESIGN STRATEGIES FOR AIR POLLUTION CONTROL

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xAA MA xBB MB = xAC MC. Overall Energy Balance: ... Enthalpy : H = U PV where V = 1/ is the specific volume. H calculated from Cp dT. ... – PowerPoint PPT presentation

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Title: PROCESS DESIGN STRATEGIES FOR AIR POLLUTION CONTROL


1
PROCESS DESIGN STRATEGIES FOR AIR POLLUTION
CONTROL
2
Example Removal of NOx from a Process Stream
Cross flow
Problem identified Emission of NOx
Counter flow
Co-current flow
  • PRELIMINARY DATA
  • Stream composition
  • Flow rate
  • Temperature
  • Pressure
  • Operating parameter variations

Decision Point 3
Condensation
Decision Point 1
Decision Point 2
Continuous Packed column
Absorption
Stage-wise
Adsorption
3
Energy and Mass Balances Basis for Process
Design
Q, heat transferred
Ws shaft work on system
Stream A
SYSTEM
Stream C
Stream B
ZA
ZC
ZB
4
Overall mass balance MA MB MC xAA MA xBB
MB xAC MC
Overall Energy Balance
Note First subscript represents component and
second subscript represents Stream.
Enthalpy H U PV where V 1/? is the
specific volume. ?H calculated from ?Cp dT.
  • Uj internal energy, Pj pressure, ?j
    density, Vj average stream velocity,
  • - correction factor (1 for turbulent and 0.5 for
    laminar flow), g acceleration

due to gravity, gc gravitational constant.
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Mean Mixing Depth
(dt/dz)env
MMD
MMD
MMD
T0
T0
Denotes environmental profile
Denotes adiabatic profile
11
Holzworth, G.C. (1972) "Mixing heights, wind
speeds, and potential for urban air pollution
throughout the contiguous United States", Office
of Air Prog. pub. AP-101,USEPA, RTP, NC.
Mean summer afternoon mixing height (meters)
Mean summer morning mixing height (meters)
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Effect of Terrain Roughness on Wind Speed Profile
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Wind Rose
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