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THUYẾT TRÌNH THIẾT BỊ BOILERS

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2 Boilers
Syllabus





Boiler Types, Combustion in boilers
Performances evaluation of boilers, Analysis of losses
Feed water treatment, Blow down
Energy conservation opportunities.


2.1 Introduction to Boiler



It is an enclosed Pressure Vessel



Process: Evaporation



Steam volume increases to 1,600 times
from water and produces tremendous
force
Care is must to avoid explosion.




Heat generated by Combustion of
Fuel is transferred to water to
become steam

What is a boiler?


Boiler Specification


Boiler Make & Year



MCR(Maximum Continuous Rating) :10TPH (F & A 100oC)



Rated Working Pressure

:10.54 kg/cm2(g)



Type of Boiler

: 3 Pass Fire tube





Fuel Fired
Heating surface

:XYZ & 2003

: Fuel Oil
: M2


2.2 Boiler Systems
Water treatment system
Feed water system
Steam System
Blow down system
Fuel supply system
Air Supply system
Flue gas system


2.3 Boiler Types and Classifications


Fire in tube or Hot gas through tubes and boiler feed
water in shell side



Fire Tubes submerged in water

Application



Used for small steam capacities
( upto 25T/hr and 17.5kg/cm2

Merits





Low Capital Cost and fuel Efficient (82%)
Accepts wide & load fluctuations
Packaged Boiler

Fire Tube Boiler





Boiler Types and Classifications
Water Tube Boiler

Water flow through tubes

Water Tubes surrounded by hot gas
Application





Used for Power Plants
Steam capacities range from 4.5- 120 t/hr
Characteristics




High Capital Cost




Demands more controls

Used for high pressure high capacity steam
boiler
Calls for very stringent water quality




Package boilers are generally of shell
type with fire tube design

 More number of passes-so more heat
transfer


 Large number of small diameter tubes
leading to good convective heat
transfer.

 Higher thermal efficiency

Packaged Boiler


Chain Grate or Traveling Grate Stoker Boiler

 Coal is fed on one end

of a moving steel chain
grate

 Ash drops off at end
 Coal grate controls rate
of coal feed into
furnace by controlling
the thickness of the
fuel bed.

 Coal must be uniform

in size as large lumps will
not burn out completely



Spreader Stoker Boiler
Uses both suspension and grate
burning
Coal fed continuously over burning
coal bed
Coal fines burn in suspension and
larger coal pieces burn on
grate
Good flexibility to
meet changing load requirements
Preferred over other type of stokers
in industrial application


Pulverized Fuel Boiler
Coal is pulverised to a fine powder, so that less than 2% is +300
microns, and 70-75% is below 75 microns.
Coal is blown with part of the combustion air into the boiler plant
through a series of burner nozzles.
• Combustion temperatures from
1300-1700°C
• Particle residence time in the
boiler is 2-5 seconds
• Most popular system for firing
pulverized coal is the tangential
firing using four burners corner to
corner to create a fire ball at the
center of the furnace
Tangential firing



Pulverized Fuel Boiler (Contd..)
Advantages



Its ability to burn all ranks of coal from anthracitic to lignitic, and it permits
combination firing (i.e., can use coal, oil and gas in same burner). Because
of these advantages, there is widespread use of pulverized coal furnaces.

Disadvantages




High power demand for pulverizing
Requires more maintenance, flyash erosion and pollution complicate unit
operation


Fluidized bed Combustion (FBC) boiler
Distributed air is passed upward through a bed of solid particles
The particles are undisturbed at low velocity.As air velocity is increased,
a stage is reached when the particles are suspended in the air
Further,
increase
in
velocity gives rise to
bubble formation, vigorous
turbulence

and
rapid
mixing and the bed is said
to be fluidized.
Coal is fed continuously in
to a hot air agitated
refractory sand bed, the
coal will burn rapidly and
the bed attains a uniform
temperature


Fluidised Bed Combustion


Fluidized-bed boiler (Contd..)
Advantages :



Higher rates of heat transfer between combustion process and boiler tubes (thus



combustion temperature 850oC is lower than in a conventional furnace. The lower



In addition, the limestone (CaCO ) and dolomite (MgCO ) react with SO to form
3

3
2
calcium and magnesium sulfides, respectively, solids which do not escape up the

reduced furnace area and size required),

furnace temperatures means reduced NO production.
x

stack; This means the plant can easily use high sulfur coal.



Fuel Flexibility: Multi fuel firing


2.4 Performance Evaluation of Boilers
 

There are two methods of assessing boiler efficiency.
 
1)      The Direct Method: Where the energy gain of the working
fluid (water and steam) is compared with the energy content of the
boiler fuel. 
2)      The Indirect Method: Where the efficiency is the difference
between the losses and the energy input.
Boiler Efficiency
Evaluation Method

1. Direct Method


2. Indirect
Method


Efficiency Calculation by Direct
Method
Example:
Type of boiler: Coal fired Boiler
Heat input data
Qty of coal consumed

:1.8 TPH

GCV of coal

:3200K.Cal/kg

Heat output data







Qty of steam gen

: 8 TPH


Steam pr/temp:10 kg/cm2(g)/1800C
Enthalpy of steam(sat) at 10 kg/cm2(g) pressure
Feed water temperature : 850 C
Enthalpy of feed water

: 85 K.Cal/kg

Find out the Find efficiency ?
Find out the Evaporation Ratio?

:665 K.Cal/kg


Boiler efficiency (η): = Q x (H – h) x 100
(q x GCV)
 
Where Q = Quantity of steam generated per hour (kg/hr)
H = Enthalpy of saturated steam (kcal/kg)
h = Enthalpy of feed water (kcal/kg)
q = Quantity of fuel used per hour (kg/hr)
GCV = Gross calorific value of the fuel (kcal/kg)
 
Boiler efficiency (η)=

8 TPH x1000Kg/Tx (665–85) x 100
1.8 TPH x 1000Kg/T x 3200
= 80.0%

 
Evaporation Ratio


= 8 Tonne of steam/1.8 Ton of coal
= 4.4


What are the losses that occur in a boiler?
Steam Output

6. Surface loss

1. Dry Flue gas loss
2. H2 loss
3. Moisture in fuel
4. Moisture in air
5. CO loss

7. Fly ash loss

Fuel Input, 100%

Boiler

Flue gas

Air
8. Bottom ash loss

Efficiency
(by In Direct Method)


= 100 – (1+2+3+4+5+6+7+8)


Example:
The following are the data collected for a typical oil fired boiler. Find out the efficiency of the
boiler by indirect method and Boiler Evaporation ratio.
Ultimate analysis of Oil

C : 84.0 %
H2: 12.0 %
S: 3.0 %
O2: 1.0 %
GCV of Oil
: 10200 kcal/kg
Steam Generation Pressure
: 7kg/cm2(g)-saturated
Enthalpy of steam
: 660 kCal/kg
Feed water temperature
: 60oC
Percentage of Oxygen in flue gas: 7
Percentage of CO2
in flue gas: 11
Flue gas temperature (Tf)
: 220 0C
Ambient temperature (Ta)
: 27 0C
Humidity of air
: 0.018 kg/kg of dry air



 

Solution

Step-1: Find the theoretical air requirement
  [(11 .6 x C ) + {34.8 x ( H

2

− O2 / 8)} + (4.35 x S )] / 100

= kg/kg of oil
 

=[(11.6 x 84) + [{34.8 x (12 – 1/8)} + (4.35 x 3)]/100 kg/kg of oil
=14 kg of air/kg of oil
 

Step-2: Find the %Excess air supplied7%
O2 %
x100
21 − O2%

x100
 
Excess air supplied (EA) =
= 21 − 7
= 50%
Step-3: Find the Actual mass of air supplied

Actual mass of air supplied /kg of fuel = [ 1 + EA/100] x Theoritical Air
(AAS)
= [1 + 50/100] x 14
= 1.5 x 14
= 21 kg of air/kg of oil


Step-4: Estimation of all losses
 

i. Dry flue gas loss
Percentage heat loss due to dry flue gas =

m x C p x (T f − Ta )
GCV of fuel

x 100

m= mass of CO2 + mass of SO2 + mass of N2 + mass of O2
 

0.84 x 44 0.03 x 64 21 x 77 
23 
m=
+
+
+  (21 − 14) x

12
32

100
100 


m

=

21 kg / kg of oil

 

21 x 0.23 x (220 − 27)
x 100
10200

= 9.14 %


Alternatively a simple method can be used for determining the
dry flue gas loss as given below.
m x C p x (T f − Ta )
x 100
a) Percentage heat loss due to dry flue gas =
GCV of fuel
Total mass of flue gas (m) = mass of actual air supplied + mass of
fuel supplied
= 21 + 1=22
 
22 x 0.23 x ( 220 − 27)

x 100 = 9.57%
%Dry flue gas loss =
10200


ii. Heat loss due to evaporation of water formed due to H2 in fuel

9 x H 2 x {584 + C p (Tf - Ta )}

 
=

GCV of fuel

Where, H2 – percentage of H2 in fuel
 
=
 

x 100

9 x 12 x {584 + 0.45 (220 - 27 )}
x 100
10200

= 7.10%
iii. Heat loss due to moisture present in air
AAS x humidity x C p x (T f − Ta )
 
x 100

=
GCV of fuel

=

21 x 0.018 x 0.45 x (220 − 27)
x 100
10200

= 0.322


iv Heat loss due to radiation and other unaccounted losses

For a small boiler it is estimated to be 2%
Boiler Efficiency 
i. Heat loss due to dry flue gas

: 9.14%

 

ii.        Heat loss due to evaporation of water formed due to H2 in fuel

: 7.10 %

iii.       Heat loss due to moisture present in air
iv.        Heat loss due to radiation and other unaccounted loss

: 2%


 

 

: 0.322 %

 

Boiler Efficiency = 100- [9.14+7.10+0.322+2] 
= 100 – 18.56 = 81 (app)

Evaporation Ratio = Heat utilised for steam generation/Heat addition to the steam
= 10200 x 0.81/ (660-60)
= 14.11


2.5 Why Boiler Blow Down ?
When water evaporates Dissolved solids gets concentrated
and Solids precipitates on tubes. Reduces the heat transfer rate


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