Combustion of Pulverised Coal in a Mixture of Oxygen and Recycled Flue Gas (eBook)
272 Seiten
Elsevier Science (Verlag)
978-0-08-100004-5 (ISBN)
Combustion of Pulverised Coal in a Mixture of Oxygen and Recycled Flue Gas focuses on a niche technology, combustion of coal in an oxygen rich environment, which is one approach to obtaining 'clean coal,' by making it easier to capture carbon that is released in the combustion process. Toporov's book breaks ground on covering the key fundamentals of oxycoal technologies, which have not yet been covered in this depth.
Combustion of Pulverised Coal in a Mixture of Oxygen and Recycled Flue Gas summarizes the main results from a pioneering work on experimental and numerical investigations of oxyfuel technologies. It provides the theoretical background of the process, the problems to be faced, and the technical solutions that were achieved during these investigations.
- Summarizes results from investigations of oxyfuel technologies performed at Aachen University, Germany
- Provides theoretical background, as well as the primary problems of these technologies and how they can be solved
Combustion of Pulverised Coal in a Mixture of Oxygen and Recycled Flue Gas focuses on a niche technology, combustion of coal in an oxygen rich environment, which is one approach to obtaining 'clean coal,' by making it easier to capture carbon that is released in the combustion process. Toporov's book breaks ground on covering the key fundamentals of oxycoal technologies, which have not yet been covered in this depth. Combustion of Pulverised Coal in a Mixture of Oxygen and Recycled Flue Gas summarizes the main results from a pioneering work on experimental and numerical investigations of oxyfuel technologies. It provides the theoretical background of the process, the problems to be faced, and the technical solutions that were achieved during these investigations. Summarizes results from investigations of oxyfuel technologies performed at Aachen University, Germany Provides theoretical background, as well as the primary problems of these technologies and how they can be solved
Nomenclature
Symbol
A Area [m2]
A Pre-exponential factor [varies]
Ak Mole fraction [–]
A, B Empirical coefficients in EDM [–]
c Molar concentration [mol/m3]
C Function, coefficient, constant [–]
CD1, CD2 Empirical coefficients in EDC [–]
cp Specific heat capacity [J/kg-K]
d Diameter [m]
D Coefficient [–]
E Activation energy [kJ/mol]
f Force [N]
ΔH Heat of formation [J/kg]
h Heat transfer coefficient [W/m2-K]
I Radiation intensity [W/m2-sr]
k Turbulent kinetic energy [m2/s2]
K Constant [–]
L Characteristic length [m]
m, M Mass [kg]
M Molecular weight [kg/mol]
m Mass flow rate [kg/s]
p, P Pressure [Pa]
p Ratio [–]
Q Thermal input [W]
r Stoichiometric ratio [–]
R Reaction rate [kg/(m3 s)]
R Universal gas constant 8,314 kJ/(kmol K)
S Particle internal surface area [m2]
S Source terms [varies]
t Time [s]
T Temperature [K], [°C]
u, v Velocity components [m/s]
u′,v′ Fluctuation of velocity [m/s]
V Mass [kg]
X Distance [m]
Y Mass fraction [–]
Greek Letters
α Absorptivity [–]
γ Mass fraction [–]
ε Emissivity [–]
ε Effectiveness factor [–]
ε Dissipation rate of turbulent energy [m2/s3]
Φ Source term [varies]
ϕ Ratio [–]
Γ Diffusion coefficient [kg/(m s)]
δ,Δ Difference operator [–]
δ Particle pore diameter [10−9 m]
η Dynamic viscosity [kg/(m s)]
λ Excess air ratio [–]
ν Kinematic viscosity [m2/s]
ν Stoichiometric coefficient [–]
ν Frequency [1/s]
ρ Density [kg/m3]
ρ Reaction-rate ratio in CPD model [–]
τ Time constant [s]
τ Tortuosity [–]
τ Shear stresses [kg/(s2 m)]
σ Model constants [–]
σ Stefan-Boltzmann constant 5,669 W/(m2 k)
ω Reaction rate [1/s]
Abbreviations
AFT Adiabatic Flame Temperature
ASTM American Society for Testing and Materials
BFB Bubbling Fluidised Bed
BO Burnout
d.a.f. Dry Ash-Free
DIN Deutsches Institut fuer Normung
CBK Char Burnout Kinetics Model
CCS Carbon Capture and Storage
CCR Carbon Capture and Reuse
CDL Coal Devolatilisation Laboratory
CFB Circulating Fluidised Bed
CFD Computational Fluid Dynamics
CPD Chemical Percolation Devolatilisation Model
CR Conversion Ratio
EDC Eddy Dissipation Concept
EDM Eddy Dissipation Model
ER External Recirculation
ESP Electrostatic Precipitators
EWBM Exponential Wideband Model
FB Fluidised Bed
FGD Flue Gas Desulphurisation
FG-DVC Functional Group, Depolymerisation, Vaporisation, and Cross-Linking
GHG Greenhouse Gas
GCV Gross Calorific Value
IGCC Integrated Gasification Combine Cycle
IPFR Isothermal Plug Flow Reactor
IRZ Internal Recirculation Zone
KIN Kinetics
LES Large Eddy Simulation
L-H Langmuir-Hinshelwood
max Maximum
min Minimum
Mtoe Million (Mega-) Tonnes of Oil Equivalent
NMR Nuclear Magnetic Resonance
OECD Organisation for Economic Cooperation and Development
OFA Overfire Air
PFBC Pressurised Fluidised Bed Combustion
PFR Plug Flow Reactor
PM Primary Stream Momentum Ratio
ppm Parts Per Million
PS Primary Stream
RANS Reynolds Averaged Navier Stokes
RFG Recirculated Flue Gas
R/P Reserves-to-Production
SCR Selective Catalytic Reduction
SK Steinkohle
SM Secondary Stream Momentum Ratio
SS Secondary Stream
TA Thermal Annealing
TGA Thermogravimetric Analysis
TS Tertiary Stream
VM Volatile Matter
Vol Volume
URANS Unsteady Reynolds Averaged Navier Stokes
WSGGM Weighted Sum of Grey Gases Model
wt Weight
WTA Wirbelschicht-Trocknung von Braunkohle mit interner Abwärmenutzung
Dimensionless Numbers
Nu Nusselt number
Re Reynolds number
Sh Sherwood number
Subscripts
ad Adsorption
ash Related to fuel ash
app, a Apparent
b...
Erscheint lt. Verlag | 30.5.2014 |
---|---|
Sprache | englisch |
Themenwelt | Technik ► Bauwesen |
Technik ► Elektrotechnik / Energietechnik | |
Technik ► Umwelttechnik / Biotechnologie | |
ISBN-10 | 0-08-100004-9 / 0081000049 |
ISBN-13 | 978-0-08-100004-5 / 9780081000045 |
Haben Sie eine Frage zum Produkt? |
Größe: 6,2 MB
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