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Improving Boiler EfficiencyImproving Boiler Efficiency
Utility and power plant Course
Assistant Chief Engineer
Qusay A.M.Saeed
Participant
for
How to Increase boiler Efficiency?
20 proven methods that
save up to 30% in fuel
costs
Efficiency Equation
Boiler heat losses
Efficiency
improvements
without Expenses
Method 1
Reduce Excess Air
Potential savingPotential saving :5%-10%
ProblemProblem :unneeded excess air is used, probably to dilute the flue gas so that
smoke is not seen.
SolutionsSolutions: reduce excess air to the minimum 10%-15% requird.
Typical Excess Air Values
Excess Air
Normal combustion efficiencies for natural gas at different amounts of
excess air and flue gas temperatures are indicated below
68.271.975.679.382.810.081.6
72.175.278.281.284.17.044.9
74.076.779.582.184.75.028.1
75.477.980.482.885.23.015
76.078.480.883.185.42.09.5
600500400300200OxygenAir
Net Stack Temperature1)
(o
F)Excess %
Combustion Efficiency (%)
Flue Gas Loss Combustion Oil
The relationship
between temperature
difference flue gas and
supply air,
CO2concentration in
the flue gas, and the
efficiency loss in the flue
gas combustion oil, is
expressed in the
diagram below.
Method 2
Decrease Flue-Gas Temperature
Potential savingPotential saving :1% for every 40°F.the potential saving are 3%,since many
stacks run 120°F too high.
ProblemProblem :Either excess air or fouling water and /or fire side tubes.
Solutions:Solutions:
1- If there is excess fuel,the fuel rate can be decreased to decease the
temperature .
2- if the tube are fouling up, steam production will suffer ,and the only solution
is to shut down and clean them up or blow soot on fireside.
2- An economizer may be economical (see method 15)
The TDS inside a boiler should be maintained at recommended levels else it can
lead to scaling of the boiler tubes and eventually failure of the tubes which is a
safety hazard.
Energy Loss from Scale
Deposits
Commerce
Increased Boiler Heating Time
due to Scale
Method 3
Reduce Boiler Pressure
Potential savingPotential saving :1%for every 70psig reduction
Problem :the boiler is being operated at a pressure higher
than necessary.
Solution :slowly reduce boiler pressure to a point where
the amount of steam produced is sufficient to fulfill plant
requirements
Method 4
Increase Fuel Oil Temperature
Potential saving : 5%
Problem :Atomize the fuel at the right
viscosity .Too high or too low a viscosity
will yield poor atomization and poor
efficiency .
Solution:
Preheat the fuel at 212°F-230°F or more so
that the fuel viscosity will be 100-300 sus
Fuels oils - their viscosity versus
temperature
Fuel Oil Heating System
Method 5
Optimize Fuel Atomization Pressure
Potential saving: 1%
Problem :The fuel atomization pressure is
lower or higher than that specified by the
nozzle or burner design
Solution: Adjust fuel pressure according to
nozzle operating instructions
Method 6
Reduce Boiler blowdown
Potential saving : 1%
Problem :excessive blowdown due to poor water
treatment and /or poor operating practices .the
hot blowdown stream has energy that is lost
unless it is recovered (see Method 16)
Solution: control feed water quality with the
appropriate water treatment; review operation
Procedures
Flash tank
Method 7
Optimize Single-boiler Firing
Potential saving :5%-10%
Problem: A boiler may come on for afew
minutes and then be off for several
minutes, resulting in large energy losses
due to the removal of useful heat when the
boiler is off; or a boiler may “hunt” i.e. the
firing rate is continually adjusting ,resulting
in much more excess air.
• Solution :for an on –off boiler ,fire the
boiler at an intermediate rate or buy a
smaller boiler ; for boiler that “hunt” adjust
the firing so that larger steam – pressure
fluctuation are allowed.
Method 8
Optimize multiple-boiler operation
Potential saving :2%-5%
problem: A plant have tow or more boilers
operates them without distributing the load
according to the efficiency each boiler .
Solution : Obtain the efficiency of each
boiler vs. load ; adjust each boiler to
operate at peak efficiency.
boiler efficiency vs. load
Method 9
Stop Steam Leaks
Potential :5%-10%
Problem: piping leak
Solution: plug leak as soon as they appear
• The biggest steam losses are caused by failing steam
traps or leaks into the steam system net. These
uncontrolled leaks can lead to enormous losses and also
enormous costs. The leaking traps can cause problems
with tracing of your equipment, problems with back
pressure into the condensate lines (which causes failure
of groups of steam traps), and make your cost for the
production of steam much higher. Problems with tracing
in one unit can be caused by leaking traps in a other unit
on the other side of the plant which indicates that
monitoring steam traps important is for the proper
working of your steam system.
Flange Leak Repair
Piping System Leaks 90ELL Enclosure
Flange Clamps
Valve Packing Leaks
Before - Steam Leak on Valve Packing
After - Repaired Steam Leak on Valve Packing
Steam leak rates
Steam leak rates
In addition to costing energy, steam leaks waste boiler
water and chemicals, and it can be dangerous to people
and equipment.
NOTE:
One pound of 100 psi steam contains about 1,200 BTUs. If
the steam is produced at 85% efficiency, the input
energy is 1,200 / 85% = 1,411 BTUs per pound.
Therefore, 1,000 pounds of steam requires at least 1.4
million BTUs to produce it. (1,411 BTUs per pound x
1,000)
1 MCF of Natural Gas contains 1 million BTUs
Cost to produce 1,000 lbs of steam from natural gas = 1.4 x
$ per MCF of Natural Gas
When natural gas costs $7.00 per MCF, 1,000 lbs of steam
costs (1.4 x $7) = $9.80
Method 10
Stop Steam-Trap Leaks
Potential saving :5%-10%
Problem: steam trap malfunctioning and
leaking steam.
Solution : check steam trap routinely and
repair them.
Steam trap leak
checking steam trap
Steam trap piping system
Efficiency
Improvements with
some Expenses
Method 11
Reduce Deposits in Burner
Potential saving : 1%-5%
Problem : organic and inorganic deposits
build in burner, reducing atomization
efficiency and therefore reducing
combustion efficiency .
Solution : use a fuel oil additive with
detergent dispersant to keep burners
clean
Burner
Clean burnerDeposit burner
Tips
Replacement and cleaning burners
Method 12
Reduce Scale and Soot Deposits on Fireside
Potential saving : 2% - 9%
Problem : soot and /or vanadium-based deposit
decrease the heat transfer rate. If all condition
are constant ,this decrease is noticeable when
the flue gas temperature increase with time.
Solution : treat fuel with additives to minimize
either soot deposits or vanadium-based scale.
Use soot blowers if available
Combustion
products
resulting from
burning of
fuels.
Layers of deposit associated with
coal-ash corrosion.
The flue pipe over half filled with
soot and deposit
Soot and scale do not only
increase energy consumption but
are as well a major cause of tube
failure
Fuel energy loss due to soot
Effect of Soot on Fuel Consumption
0
2
4
6
8
10
0.5
1.5
2.5
3.5Thickness of Soot Layer, mm
%FuelEnergyLoss
Warning triangle - risk of soot fire
Boiler Sootblowers
Soot Blower
Method 13
Reduce Scale and Deposits on Waterside
Potential saving : 2% - 4%
Problem : inorganic scale and deposits
decrease heat transfer rate ; i.e. flue gas
temperature increase with time.
Solution : treat feed water properly using
guidelines of boiler manufacturer or water
boiler standardizing
Energy loss due to scale deposits
Fuel energy loss due to scale
Effect of Scale on Fuel Energy Losses
0
2
4
6
8
10
12
0
0.25
0.5
0.75
1
1.25
1.5
1.75
2
Scale Thickness,mm
%FuelLoss
High density
Medium Density
Low Density
Water tube with soot outside and
scale inside
Fire tube with soot inside and
scale outside
Method 14
Increase Combustion Air
Temperature
Potential saving : 1%
Problem : preheat combustion air .every 40 °F rise
yields a 1% gain in efficiency.
Solution : there are several possible solutions:
relocate air intake duct so that a maximum air
duct temperature is obtained ,or install an air
preheater if possible and economically feasible.
Recoverable heat from boiler flue
gases
Air Heaters
Air heaters cool flue gases before they pass into
the atmosphere, increasing fuel-firing efficiency
and raising the temperature of the incoming air
of combustion. In low pressure gas or oil-fired
industrial
boilers, air heaters function as gas coolers
as there is no need to preheat the oil or gas
in order for it to burn.
Air Heaters
Method 15
Increase Feedwater Temperature
Potential saving :3%
Problem : raise water temperature
Solution : the equipment needed is an
economizer that uses the heat from flue gases, if
economically feasible. Also , the water can be
preheated using the waste heat from blowdown
(method 16).
10°F rise in feedwater temperature raisea
efficiency 1%
Economizers
Economizers help to improve boiler efficiency by
extracting heat from the flue gases discharged
from the final superheater section of a
radiant/reheat unit or the evaporative bank of a
non-reheat boiler. Heat is transferred to the
feedwater, which enters at a much lower
temperature
than saturated steam.
Economizes
Location of Air heaters and Economizers
Dew point of the flue gas
Method 16
Recover Heat Energy From Blowdown
Potential saving : 1%
Problem : preheat water by recovering energy from
blowdown.
Solution : add flash tank to system .the blowdown is
flashed by lowering the pressure in the flash tank;
the steam produced is then vented into the feed
water to boiler .some 50% of the heat in the
blowdown is recovered. Send blowdown at 220°F
to wast.
• Also aflash tank may be added ,followed
by aheat exchanger to extract one-third
more energy from the blowdown before
going to wast.
Recoverable heat from boiler
blowdown
Boiler Blowdown Heat Recovery
exchanger System
Install an Automatic Blowdown
Control System
Saving through Installion of
Automatic Blowdown
Control System
Method 17
Energy Recovery From Excessive Steam
Pressure
Potential saving :variable
Problem : use throttling or back pressure
turbine .
Solution : the idea is to utilize the energy
from steam rather than to decrease its
pressure though a throttling valve
Steam turbines
back pressure steam turbine Condensing Steam Turbine
Back-Pressure Steam Turbine
Condensing Steam Turbine
Replace Pressure-Reducing Valves
with Backpressure Turbogenerators
Many industrial facilities produce steam at a higher pressure than is demanded
by process requirements. Steam passes through pressure-reducing valves
(PRVs,
also known as letdown valves) at various locations in the steam distribution
system to let down or reduce its pressure. A non-condensing or backpressure
steam turbine can perform the same pressure-reducing function as a PRV,
while
converting steam energy into electrical energy.
In a backpressure steam turbogenerator, shaft power is produced when a
nozzle
directs jets of high-pressure steam against the blades of the turbine’s rotor. The
rotor is attached to a shaft that is coupled to an electrical generator. The steam
turbine does not consume steam. It simply reduces the pressure of the steam
that is subsequently exhausted into the process header.
Consider Installing High-Pressure Boilers
with Backpressure Turbine-Generators
When specifying a new boiler, consider a high-pressure boiler with a backpressure
steam turbine-generator placed between the boiler and the steam distribution
network. A turbine-generator can often produce enough electricity to justify the
capital cost of purchasing the higher-pressure boiler and the turbine-generator.
Since boiler fuel usage per unit of steam production increases with boiler pressure,
facilities often install boilers that produce steam at the lowest pressure consistent
with end use and distribution requirements.
In the backpressure turbine configuration, the turbine does not consume steam.
Instead, it simply reduces the pressure and energy content of steam that is subsequently
exhausted into the process header. In essence, the turbo-generator
serves the same steam function as a pressure-reducing valve (PRV)—it reduces
steam pressure—but uses the pressure drop to produce highly valued electricity
in addition to the low-pressure steam. Shaft power is produced when a nozzle
directs jets of high-pressure steam against the blades of the turbine’s rotor. The
rotor is attached to a shaft that is coupled to an electrical generator.
Method 18
Reduce Heat Losses in Boiler, Steam and
Valves
Potential saving :5% - 8%
Problem : heat is lost by radiation and convection
through the walls of uninsulated or poorly
insulated boiler surfaces and piping.
Solution : use a surface thermometer and
determine where heat losses are present ; then
insulate.
Surface Thermometer
Digital Surface Thermometer
Infrared (IR) Thermometer
Boiler Wall Insulation
Heat loss of uninsulated steam line
Pipe and Fitting Insulation
Tank Insulation
Valve Insulation
Jacket
Flue Duct
Method 19
Use Fuel Oil Rather Than Natural Gas
Potential saving : 2%
Problem : If the price of natural gas is the
same or higher than that of fuel oil,which is
more economical?
Solution: use fuel oil.even if both cost the
sam per MMBtu,fuel oil gives about a 2%
higher efficiency than natural gas ,the
• The reason for this is that natural gas has
more hydrogen atoms per unit weight than
fuel oil. therefore, more water is formed
from the gas, the the latent heat of
vaporization of water is lost when the
water vapor leaves the stack.
• MMBtu=Million Metric British Thermal
Units
Method 20
Change From Steam to Air Atomization
Potential saving : 1%
Solution : use are atomization for fuel oils.
The energy required to produce the are of
atomization is a small fraction of the
energy required to produce the steam of
atomization.
Air Atomization burner
References
• Manual for improving boiler and furnace
performance –borras
• Improving Steam System Performance
U.S. Department of Energy

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Energy conservation

  • 2. Utility and power plant Course Assistant Chief Engineer Qusay A.M.Saeed Participant for
  • 3. How to Increase boiler Efficiency? 20 proven methods that save up to 30% in fuel costs
  • 7. Method 1 Reduce Excess Air Potential savingPotential saving :5%-10% ProblemProblem :unneeded excess air is used, probably to dilute the flue gas so that smoke is not seen. SolutionsSolutions: reduce excess air to the minimum 10%-15% requird.
  • 10. Normal combustion efficiencies for natural gas at different amounts of excess air and flue gas temperatures are indicated below 68.271.975.679.382.810.081.6 72.175.278.281.284.17.044.9 74.076.779.582.184.75.028.1 75.477.980.482.885.23.015 76.078.480.883.185.42.09.5 600500400300200OxygenAir Net Stack Temperature1) (o F)Excess % Combustion Efficiency (%)
  • 11. Flue Gas Loss Combustion Oil The relationship between temperature difference flue gas and supply air, CO2concentration in the flue gas, and the efficiency loss in the flue gas combustion oil, is expressed in the diagram below.
  • 12.
  • 13. Method 2 Decrease Flue-Gas Temperature Potential savingPotential saving :1% for every 40°F.the potential saving are 3%,since many stacks run 120°F too high. ProblemProblem :Either excess air or fouling water and /or fire side tubes. Solutions:Solutions: 1- If there is excess fuel,the fuel rate can be decreased to decease the temperature . 2- if the tube are fouling up, steam production will suffer ,and the only solution is to shut down and clean them up or blow soot on fireside. 2- An economizer may be economical (see method 15)
  • 14. The TDS inside a boiler should be maintained at recommended levels else it can lead to scaling of the boiler tubes and eventually failure of the tubes which is a safety hazard.
  • 15. Energy Loss from Scale Deposits
  • 17.
  • 18. Method 3 Reduce Boiler Pressure Potential savingPotential saving :1%for every 70psig reduction Problem :the boiler is being operated at a pressure higher than necessary. Solution :slowly reduce boiler pressure to a point where the amount of steam produced is sufficient to fulfill plant requirements
  • 19. Method 4 Increase Fuel Oil Temperature Potential saving : 5% Problem :Atomize the fuel at the right viscosity .Too high or too low a viscosity will yield poor atomization and poor efficiency . Solution: Preheat the fuel at 212°F-230°F or more so that the fuel viscosity will be 100-300 sus
  • 20. Fuels oils - their viscosity versus temperature
  • 22. Method 5 Optimize Fuel Atomization Pressure Potential saving: 1% Problem :The fuel atomization pressure is lower or higher than that specified by the nozzle or burner design Solution: Adjust fuel pressure according to nozzle operating instructions
  • 23. Method 6 Reduce Boiler blowdown Potential saving : 1% Problem :excessive blowdown due to poor water treatment and /or poor operating practices .the hot blowdown stream has energy that is lost unless it is recovered (see Method 16) Solution: control feed water quality with the appropriate water treatment; review operation Procedures
  • 25. Method 7 Optimize Single-boiler Firing Potential saving :5%-10% Problem: A boiler may come on for afew minutes and then be off for several minutes, resulting in large energy losses due to the removal of useful heat when the boiler is off; or a boiler may “hunt” i.e. the firing rate is continually adjusting ,resulting in much more excess air.
  • 26. • Solution :for an on –off boiler ,fire the boiler at an intermediate rate or buy a smaller boiler ; for boiler that “hunt” adjust the firing so that larger steam – pressure fluctuation are allowed.
  • 27. Method 8 Optimize multiple-boiler operation Potential saving :2%-5% problem: A plant have tow or more boilers operates them without distributing the load according to the efficiency each boiler . Solution : Obtain the efficiency of each boiler vs. load ; adjust each boiler to operate at peak efficiency.
  • 29.
  • 30. Method 9 Stop Steam Leaks Potential :5%-10% Problem: piping leak Solution: plug leak as soon as they appear
  • 31.
  • 32. • The biggest steam losses are caused by failing steam traps or leaks into the steam system net. These uncontrolled leaks can lead to enormous losses and also enormous costs. The leaking traps can cause problems with tracing of your equipment, problems with back pressure into the condensate lines (which causes failure of groups of steam traps), and make your cost for the production of steam much higher. Problems with tracing in one unit can be caused by leaking traps in a other unit on the other side of the plant which indicates that monitoring steam traps important is for the proper working of your steam system.
  • 34. Piping System Leaks 90ELL Enclosure
  • 36. Valve Packing Leaks Before - Steam Leak on Valve Packing After - Repaired Steam Leak on Valve Packing
  • 39. In addition to costing energy, steam leaks waste boiler water and chemicals, and it can be dangerous to people and equipment.
  • 40. NOTE: One pound of 100 psi steam contains about 1,200 BTUs. If the steam is produced at 85% efficiency, the input energy is 1,200 / 85% = 1,411 BTUs per pound. Therefore, 1,000 pounds of steam requires at least 1.4 million BTUs to produce it. (1,411 BTUs per pound x 1,000) 1 MCF of Natural Gas contains 1 million BTUs Cost to produce 1,000 lbs of steam from natural gas = 1.4 x $ per MCF of Natural Gas When natural gas costs $7.00 per MCF, 1,000 lbs of steam costs (1.4 x $7) = $9.80
  • 41. Method 10 Stop Steam-Trap Leaks Potential saving :5%-10% Problem: steam trap malfunctioning and leaking steam. Solution : check steam trap routinely and repair them.
  • 46. Method 11 Reduce Deposits in Burner Potential saving : 1%-5% Problem : organic and inorganic deposits build in burner, reducing atomization efficiency and therefore reducing combustion efficiency . Solution : use a fuel oil additive with detergent dispersant to keep burners clean
  • 48. Tips
  • 50. Method 12 Reduce Scale and Soot Deposits on Fireside Potential saving : 2% - 9% Problem : soot and /or vanadium-based deposit decrease the heat transfer rate. If all condition are constant ,this decrease is noticeable when the flue gas temperature increase with time. Solution : treat fuel with additives to minimize either soot deposits or vanadium-based scale. Use soot blowers if available
  • 52. Layers of deposit associated with coal-ash corrosion.
  • 53. The flue pipe over half filled with soot and deposit
  • 54. Soot and scale do not only increase energy consumption but are as well a major cause of tube failure
  • 55.
  • 56. Fuel energy loss due to soot Effect of Soot on Fuel Consumption 0 2 4 6 8 10 0.5 1.5 2.5 3.5Thickness of Soot Layer, mm %FuelEnergyLoss
  • 57. Warning triangle - risk of soot fire
  • 60. Method 13 Reduce Scale and Deposits on Waterside Potential saving : 2% - 4% Problem : inorganic scale and deposits decrease heat transfer rate ; i.e. flue gas temperature increase with time. Solution : treat feed water properly using guidelines of boiler manufacturer or water boiler standardizing
  • 61. Energy loss due to scale deposits
  • 62. Fuel energy loss due to scale Effect of Scale on Fuel Energy Losses 0 2 4 6 8 10 12 0 0.25 0.5 0.75 1 1.25 1.5 1.75 2 Scale Thickness,mm %FuelLoss High density Medium Density Low Density
  • 63. Water tube with soot outside and scale inside
  • 64. Fire tube with soot inside and scale outside
  • 65. Method 14 Increase Combustion Air Temperature Potential saving : 1% Problem : preheat combustion air .every 40 °F rise yields a 1% gain in efficiency. Solution : there are several possible solutions: relocate air intake duct so that a maximum air duct temperature is obtained ,or install an air preheater if possible and economically feasible.
  • 66. Recoverable heat from boiler flue gases
  • 67. Air Heaters Air heaters cool flue gases before they pass into the atmosphere, increasing fuel-firing efficiency and raising the temperature of the incoming air of combustion. In low pressure gas or oil-fired industrial boilers, air heaters function as gas coolers as there is no need to preheat the oil or gas in order for it to burn.
  • 69. Method 15 Increase Feedwater Temperature Potential saving :3% Problem : raise water temperature Solution : the equipment needed is an economizer that uses the heat from flue gases, if economically feasible. Also , the water can be preheated using the waste heat from blowdown (method 16). 10°F rise in feedwater temperature raisea efficiency 1%
  • 70. Economizers Economizers help to improve boiler efficiency by extracting heat from the flue gases discharged from the final superheater section of a radiant/reheat unit or the evaporative bank of a non-reheat boiler. Heat is transferred to the feedwater, which enters at a much lower temperature than saturated steam.
  • 72. Location of Air heaters and Economizers
  • 73. Dew point of the flue gas
  • 74. Method 16 Recover Heat Energy From Blowdown Potential saving : 1% Problem : preheat water by recovering energy from blowdown. Solution : add flash tank to system .the blowdown is flashed by lowering the pressure in the flash tank; the steam produced is then vented into the feed water to boiler .some 50% of the heat in the blowdown is recovered. Send blowdown at 220°F to wast.
  • 75. • Also aflash tank may be added ,followed by aheat exchanger to extract one-third more energy from the blowdown before going to wast.
  • 76. Recoverable heat from boiler blowdown
  • 77.
  • 78.
  • 79. Boiler Blowdown Heat Recovery exchanger System
  • 80. Install an Automatic Blowdown Control System
  • 81.
  • 82. Saving through Installion of Automatic Blowdown Control System
  • 83. Method 17 Energy Recovery From Excessive Steam Pressure Potential saving :variable Problem : use throttling or back pressure turbine . Solution : the idea is to utilize the energy from steam rather than to decrease its pressure though a throttling valve
  • 84. Steam turbines back pressure steam turbine Condensing Steam Turbine
  • 87. Replace Pressure-Reducing Valves with Backpressure Turbogenerators Many industrial facilities produce steam at a higher pressure than is demanded by process requirements. Steam passes through pressure-reducing valves (PRVs, also known as letdown valves) at various locations in the steam distribution system to let down or reduce its pressure. A non-condensing or backpressure steam turbine can perform the same pressure-reducing function as a PRV, while converting steam energy into electrical energy. In a backpressure steam turbogenerator, shaft power is produced when a nozzle directs jets of high-pressure steam against the blades of the turbine’s rotor. The rotor is attached to a shaft that is coupled to an electrical generator. The steam turbine does not consume steam. It simply reduces the pressure of the steam that is subsequently exhausted into the process header.
  • 88. Consider Installing High-Pressure Boilers with Backpressure Turbine-Generators When specifying a new boiler, consider a high-pressure boiler with a backpressure steam turbine-generator placed between the boiler and the steam distribution network. A turbine-generator can often produce enough electricity to justify the capital cost of purchasing the higher-pressure boiler and the turbine-generator. Since boiler fuel usage per unit of steam production increases with boiler pressure, facilities often install boilers that produce steam at the lowest pressure consistent with end use and distribution requirements. In the backpressure turbine configuration, the turbine does not consume steam. Instead, it simply reduces the pressure and energy content of steam that is subsequently exhausted into the process header. In essence, the turbo-generator serves the same steam function as a pressure-reducing valve (PRV)—it reduces steam pressure—but uses the pressure drop to produce highly valued electricity in addition to the low-pressure steam. Shaft power is produced when a nozzle directs jets of high-pressure steam against the blades of the turbine’s rotor. The rotor is attached to a shaft that is coupled to an electrical generator.
  • 89. Method 18 Reduce Heat Losses in Boiler, Steam and Valves Potential saving :5% - 8% Problem : heat is lost by radiation and convection through the walls of uninsulated or poorly insulated boiler surfaces and piping. Solution : use a surface thermometer and determine where heat losses are present ; then insulate.
  • 90. Surface Thermometer Digital Surface Thermometer Infrared (IR) Thermometer
  • 92. Heat loss of uninsulated steam line
  • 93. Pipe and Fitting Insulation
  • 96.
  • 98. Method 19 Use Fuel Oil Rather Than Natural Gas Potential saving : 2% Problem : If the price of natural gas is the same or higher than that of fuel oil,which is more economical? Solution: use fuel oil.even if both cost the sam per MMBtu,fuel oil gives about a 2% higher efficiency than natural gas ,the
  • 99. • The reason for this is that natural gas has more hydrogen atoms per unit weight than fuel oil. therefore, more water is formed from the gas, the the latent heat of vaporization of water is lost when the water vapor leaves the stack. • MMBtu=Million Metric British Thermal Units
  • 100.
  • 101.
  • 102.
  • 103. Method 20 Change From Steam to Air Atomization Potential saving : 1% Solution : use are atomization for fuel oils. The energy required to produce the are of atomization is a small fraction of the energy required to produce the steam of atomization.
  • 105. References • Manual for improving boiler and furnace performance –borras • Improving Steam System Performance U.S. Department of Energy