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NSEN 618 Class 12

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Metals -- Oxides -- Ashes. SiO2 -- SiO2 Dust to Dust. 9/9/09. NSEN 618. 6. Method ... Ash removal. Filtration (particularly Cl, NOx, dioxins, SOx. High ... – PowerPoint PPT presentation

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Title: NSEN 618 Class 12


1
NSEN 618 Class 12
  • Combustion -- all of Chapter 4 and some of
    Chapter 5
  • Learn how to calculate combustion events
  • Temperature
  • Ignition
  • Volume increase
  • Pressure
  • Explosions
  • Apply to Incinerator types
  • Starved air
  • Excess air
  • Pyrolysis
  • Reduction.

2
Terminology
  • Reactions All chemical transformations
  • Combustion Rapid oxidation generally of
    hydrocarbons
  • Incineration Controlled combustion to
    destruction
  • Deflagration Explosive burning but vr lt vs
  • Explosion Destructive pressure release
  • Detonation Special case Deflagration vr gt vs

3
Special Combustion Processes
  • Combustion
  • C O2 --gt CO2
  • C H2 O2 --gt CO2 2H2O
  • H2 O2 --gt 2H2O
  • Explosives - Anything that has a destructive
    pressure increase is an explosion)
  • NaNO2 C --gt CO2 N2
  • NH4NO3 --gt 2 H2O 1/2 N2 NO

4
Calculations
  • One needs to understand chemistry
  • Phase changes
  • Thermodynamics
  • Physics
  • Operations

5
Combustion
  • The Governing Adiabatic Equation
  • Disposition of various components
  • H2 --gt H2 O
  • C --gt CO2
  • N --gt N2
  • Cl, S, P, F --gt Acids, i.e., HCl, H2SO4, HF
  • Metals --gt Oxides --gtAshes
  • SiO2 --gt SiO2 Dust to Dust

6
Method
  • Set up Chemical Equation
  • Select the least amount that is of interest
  • Assign that to be 1 mole
  • Adjust molar volume of the remaining reactants
    and POCs
  • Calculate weight percent if necessary (it usually
    is, since we think of our real world in terms of
    weight percent although, in fact it is mass
    percent)

7
Method (continued)
  • Given the calculated T, is it above ignition
    temperature?
  • Where does ignition temperature come from?
  • Generally around 250 C for flammables
  • 400 C for nitrate
  • 800 C for almost everything
  • If T gt 1000 C, should reevaluate specific heats
    depending on the degree of accuracy you need

8
Method (continued)
  • Double check the heats of reaction and make sure
    they make sense
  • Negative heats of formation for reactants
    decrease the heat of reaction
  • Positive heats of formation for reactants
    increase the heat of reaction over and above that
    of the heat of formation of the POCs
  • Evaluate the gaseous products
  • Compute pressure increases or volume increases of
    the POCs against the Reactants as desired
  • Use PV nRT as necessary

9
Examples using Excel Combustion Files
  • H2 O2
  • C O2
  • C2H4
  • NaNO3 C
  • Ammonium Nitrate
  • TNT

10
Types of Combustion
  • Combustion (low velocity - constant pressure)
  • Stoichemetric, Starved air, Excess air
  • Deflagration (high velocity - pressure build-up)
  • Detonation (reaction velocity gt velocity of sound
    - pressure build-up)

11
Special Conditions
  • Ignition Temperature
  • Flame Temperature
  • Flash point
  • Flash over
  • LEL, UEL (Lower and upper explosion limit)

12
LEL, UEL
  • Concentration of a gaseous fuel (CH4, C2H2, H2 ,
    for example) at which the reaction will
    propagate unassisted. Generally this is equal
    the concentration at which the calculated
    adiabatic temperature equals the ignition
    temperature.
  • Note however that ignition temperature is
    pressure sensitive, sensitive to catalytic
    influences.
  • Note also that Temperature adiabatic delta T
    initial T
  • Nevertheless, the adiabatic calculation is very
    close to correct.

13
Why Incinerate??
  • Satisfies all 10 CFR 61 WAC except finely divided
    Particulates
  • Volume Reduction - Mostly a Cost Issue
  • Destroys organics not conducive to good
    cementation
  • Mostly imposed by 40 CFR 268 Hazardous Waste
    Treatment Standards
  • Required for 40 CFR 761 PCB

14
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15
Equipment Issues
  • Feeding
  • Ash removal
  • Filtration (particularly Cl, NOx, dioxins, SOx
  • High temperature materials
  • Contamination spread
  • Repair and maintenance
  • Uniform feed - trash vs. known input

16
Operational Conditions
  • 800 - 1100 C First Stage
  • 2000 C volatile destruction
  • Sub atmospheric conditions

17
Alternative Incinerator Variants
  • Fixed hearth
  • Moving hearth
  • Rotary kiln
  • Dual stage
  • Cyclone furnaces
  • Pyrolysis

18
More Alternative Incinerator Variants
  • Slagging pyrolysis
  • Gravity feed
  • Molten salt
  • Acid bath
  • Fluidized bed
  • Glass furnace based
  • Plasma driven
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