estimation and selection of air for a fuel p m v subbarao professor mechanical engineering...
TRANSCRIPT
![Page 1: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/1.jpg)
Estimation and Selection of Air for a Fuel
P M V SubbaraoProfessor
Mechanical Engineering Department
A Criteria for Sizing of Furnace & Furnace Accessories.
![Page 2: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/2.jpg)
Chemical Models for Real Fuels
Wood 5106 OHCn
5108 OHCnPeat
41635 OHCnLignite
41949 OHCnSub-bituminours
![Page 3: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/3.jpg)
Production of Useful Fuels from Crude
![Page 4: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/4.jpg)
Boiling range, and molecule size for typical refinery
• BOILING RANGE # CARBON ATOMS
• Refinery Gas <25 oC 3
• Gasoline 40-150 oC 4-10
• Naptha 150-200 oC 10-12
• Kerosene 200-300 oC 12-16
• Diesel Fuel 300-400 oC 16-25
• Residual Oil >400 oC >25
![Page 5: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/5.jpg)
Generation of Fuel Model• Practical fuels are complex mixtures of compounds.
• Some useful for generation of heat & some are useless.
• Some are threat to environment.
• Proximate Analysis & Ultimate Analysis.
• Proximate analysis - to determine the moisture, ash, volatiles matter and fixed carbon
National Capital Power Station Dadri
Equilibrated BasisSample MOIS. ASH V.M. FC UHV
(%) (%) (%) (%) K.CaI/Kg.
Wash Coal 7.1 33.7 25.0 34.2 3270
Raw Coal 6.4 35.2 25.8 32.6 3159
![Page 6: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/6.jpg)
Commercial Use of Proximate Analysis
The Energy content -- CFRI Formulae --Low Moisture Coal(M < 2% ) -- CV (Kcal/kg) = 71.7 FC + 75.6 (VM-0.1 A) - 60 MHigh Moisture Coal(M > 2%) -- CV(kcal.kg) = 85.6 {100 - (1.1A+M)} - 60 M
Where, M, A, FC and VM denote moister, ash , fixed carbon and Volatile mater (all in percent), respectively.
![Page 7: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/7.jpg)
Ultimate Analysis
• Ultimate or elementary analysis - to determine the elemental composition of the fuel
Ultimate Analysis: On Air Dried Basis
Wash Coal
%
Gross Calorific Value 4370
Carbon Content 51.28
Hydrogen Content 3.18Oxygen Content 9.72
Nitrogen Content 0.45
Sulfur Content 0.30
Ash Content 35.07
Raw Coal
Gross Calorific Value 4250
Carbon Content 51.00
Hydrogen Content 3.14Oxygen Content 8.20
Nitrogen Content 0.35
Sulfur Content 0.35
Ash Content 36.96
![Page 8: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/8.jpg)
Ultimate Analysis: On Air Dried Basis
Raw Coal
Gross Calorific Value 3884
Carbon Content 42.6
Moisture Content 6.0
Hydrogen Content 3.3
Oxygen Content 11.5
Nitrogen Content 0.7
Content 0.35
Ash Content 35.7
![Page 9: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/9.jpg)
Fuel Model
![Page 10: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/10.jpg)
Ash Model
![Page 11: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/11.jpg)
![Page 12: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/12.jpg)
Fuel Model
• Ultimate Analysis of fuel: Gravimetric
• Percentage of carbon : x --- Number of moles, X = x/12
• Percentage of combustible hydrogen : y --- Number of atomic moles, Y = y/1
• Percentage of combustible oxygen: k --- Number of atomic moles, K = k/16
• Percentage of sulfur: z – Number of atomic moles, Z = z/32
• Equivalent chemical formula : CXHYSZOK
• Equivalent Molecular weight : 100 kgs.
![Page 13: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/13.jpg)
![Page 14: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/14.jpg)
Ideal Combustion
• Ideal combustion
• CXHYSZOK + 4.673 (X+Y/4+Z-K/2) AIR → P CO2 +Q H2O + R N2 + G SO2
• Ideal Air- Fuel Ratio:
1
10024
9.28773.4
stoistoi A
FK
ZY
X
F
A
![Page 15: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/15.jpg)
Second law limit on possibility of extent of reaction
• Reactants Products
• At any time a reactor contains a combination of reactants and products.
• A reaction is said to be complete when the entropy of an adiabatic furnace reaches its maximum value.
• The value of maximum entropy will vary with the pressure and temperature of the reaction.
• A reaction system and parameters of reaction should be designed such the the maximum entropy is obtained when the reaction is almost complete (>98%).
![Page 16: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/16.jpg)
i jPjjRii
i jjjii
sYsXMaximize
PYRX
:
Mathematical Model for Completion of Reaction
For every fuel, a designer should know all possible reactants !!!Some products will influence the efficiency of reaction.Few other may not influence the efficiency of reaction but severely affect the environment.The optimal parameters for efficient reaction may not be optimal for safe reaction !!
![Page 17: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/17.jpg)
Generalized Theory of Extent of Reaction Possible
Extent of Reaction
Ent
ropy
of
Uni
vers
e
P1,T1 P2,T2
P3,T3
![Page 18: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/18.jpg)
Model Testing for Determination of important species
Air Flow Rate
Fuel Flow Rate
Water Flow Rate
Flue gas Analysis
![Page 19: Estimation and Selection of Air for a Fuel P M V Subbarao Professor Mechanical Engineering Department A Criteria for Sizing of Furnace & Furnace Accessories](https://reader030.vdocuments.mx/reader030/viewer/2022032600/56649dc95503460f94abee10/html5/thumbnails/19.jpg)
Results of Model Testing.
• For a given fuel and required steam conditions.
• Optimum air flow rate.
• Optimum fuel flow rate.
• Optimum steam flow rate.
• Optimum combustion configuration!!!
Realization of MATt Theory• Mixing: Fuel preparation systems.
• Air: Draught systems.
• T : Preheating of fuel.
• t : Dimensions of combustion chamber. : Turbulence generation systems.