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E B Muhammedshafiet al. Int. Journal of Engineering Research and Applications www.ijera.com
ISSN: 2248-9622, Vol. 5, Issue 9, (Part - 1) September 2015, pp.118-120
www.ijera.com 118|P a g e
Effect of Combustion Air Pre-Heating In Carbon Monoxide
Emission in Diesel Fired Heat Treatment Furnace
E B Muhammed Shafi, Mr. PadmanabhaAdiga, Dr. T C Mohankumar
PG Scholar MES Engineering College Kuttippuram, Kerala, India
Dy Manager, Quality Assurance Peekay Steels Castings (P) Ltd Nallalam, Calicut, Kerala
Professor MES Engineering College Kuttippuram, Kerala, India
ABSTRACT
This paper describes the effect of combustion air pre- heating in Diesel fired heat Treatment Furnace. The main
heat treatment processes are Normalizing, Tempering, Hardening, Annealing, Solution Annealing and Stress
Relieving. The emission of carbon monoxide is measured with combustion air pre-heating and without pre-
heating. The results are then compared and it is found that the emission of CO is reduced by 29.12%. With the
Combustion air pre-heating a considerable reduction in Specific Furnace Fuel Consumption (SFFC) is obtained.
The test was caaried out at Peekay Steels Casting (P) ltd, Nallalam, Calicut.
General Terms: Heat Treatment Furnace
Keywords: SFFC, Pre- heating, Combustion,Emission
I. INTRODUCTION
Heat treatment is a process on metals or alloys to
cause relief of internal stress, harden or strengthen
metals, improve machinability, change grain size
etc... Different types heat treatment process are
Annealing, Normalizing, Hardening, Tempering etc..
It involves heating and cooling of metals or alloys at
different rates depending up on requirements. In the
company Peekay Steels there are three diesel fired
furnaces, four LPG fired furnace of which one is idle
and one is under construction and one electric
furnace. The capacities of three different diesel fired
furnaces are 7 ton, 10 ton and 13 ton. The objective
of the project is to improve the thermal efficiency of
a diesel fired heat treatment furnace and to reduce
diesel consumption by some experimental
investigations. Here for the sake of furnace a new
term (SFFC) Specific Furnace Fuel Consumption is
introduced. It is the amount of diesel consumed per
unit tonnage of material processed in the furnace and
per hour of furnace operation. Our objective is to
reduce SFFC or increase thermal or furnace
efficiency. Thermal efficiency improvement is done
by reducing diesel consumption in the furnace
without affecting homogeneity in heat treatment. This
is achieved by
1. Increasing the pressure inside the furnace
chamber by adjusting the damper plate in the
exhaust gas pipe or chimney.
2. Utilizing the heat produced more effectively
which includes.
a. Pre-heating the air for combustion.’’
II. FURNACE OPERATIONS
Different furnace operations or heat treatment
processes carried out in Peekay Steels are
Normalizing, Tempering, Annealing, Solution
Annealing, Stress Relieving etc. All heat treatment
process consists of Heating, Soaking and Cooling.
All these processes are done at a specific rate
depending upon the requirement. Heating means
rising the temperature of the stock from room
temperature to soaking temperature at a specific rate.
Soaking means maintaining the temperature of the
stock at soaking temperature for a particular
time.Cooling means bringing down the temperature
of stock to a predetermined temperature or room
temperature at a particular rate depending up on the
requirement.
Figure 1 Graphical representation of heat treatment
RESEARCH ARTICLE OPEN ACCESS
E B Muhammedshafiet al. Int. Journal of Engineering Research and Applications www.ijera.com
ISSN: 2248-9622, Vol. 5, Issue 9, (Part - 1) September 2015, pp.118-120
www.ijera.com 119|P a g e
All heat treatment processes can be represented
graphically as shown above. It shows the variation of
stock temperature with time. Here AB represents
heating process, BC represents soaking process and
CD represents cooling process. Area under the curve
give an indication of energy absorbed by the stock.
Time t1, t2 and t3 are time of heating , soaking and
cooling respectively. These times are used for
calculation of SFFC. If cooling process are
quenching, normal cooling or forced air cooling, then
for calculation of SFFC time t3 is not used. If cooling
rate needed is less than the rate of above said cooling
processes, time t3 will be used for SFFC calculation
(For getting less cooling rate, fuel is to be burned )
III. FURNACE EFFICIENCY
Furnace efficiency (ƞf) greatly depends up on
Flame temperature, Air/fuel ratio, Furnace structure,
Insulation level of furnace, Radiation loss from the
furnace and Method of Furnace operation. Generally
Furnace efficiency or Thermal efficiency is defined
as the percentage of heat input that is effectively
utilized to heat the stock.
ƞf =
Heat in the stock ℎ
Heat in the fuel consumed for heating the stock
=
M ∗ C ∗ T−Tamp ∗ 1000
L ∗ρ∗ Cv
Let (T-Tamp) = ∆T
ƞf =
M ∗ C ∗∆T ∗ 1000
L ∗ρ∗ Cv
(1)
Where
M Tonnage of material processed in the furnace
(*1000 kg)
C  Specific heat of material processed in the
furnace (490 J/kg/K)
T Soaking temperature (K)
TampAmbient temperature (K)
L Amount of diesel consumed in the furnace (Liter)
𝛒Density of diesel (840 kg/m3
)
CvCalorific value of diesel (43200 kJ/kg)
Here the fuel used to heat the stock is diesel
IV. SPECIFIC FURNACE FUEL
CONSUMPTION (SFFC)
The efficiency of the furnace can be judged by
measuring the amount of diesel needed per unit time
per unit weight of the material. It is known as
Specific Furnace Fuel Consumption (SFFC). It’s unit
is Liter/Ton/hr. As far as a furnace is concerned
SFFC and Thermal efficiency are related very much
deeply and constant can be introduced, known as
furnace coefficient
SFFC = Amount of diesel consumed in liter per unit
tonnage of material processed per unit Hour.
=
L
M ∗ t
M
L
=
1
SFFC ∗ t
(2)
(2) in (1) gives
Ƞf = (
1
SFFC ∗ t
) * (
C ∗∆T
ρ∗Cv
) * 1000
From the above equation we get a new equation
relating furnace efficiency and SFFC with parameters
furnace operating time and soaking temperature
Ƞf * SFFC = (
∆T
t
) * (
C
ρ∗Cv
) * 1000 (3)
Substituting the values of the constant (C, and Cv),
we get equation (3) as
Ƞf * SFFC = (
∆T
t
)* (
490
840 ∗ 43200 ∗ 1000
) * 1000
Ƞf * SFFC = (
∆T
t
) * 13.344 * 10-6
The constant 13.344*10-6
is known as Furnace
Coefficient. This coefficient is dependent only on
specific heat value of the material, which is processed
in the heat treatment furnace, density of the fuel
which is used to heat the stock and lower calorific
value of the fuel. Usually performance of a heat
treatment furnace is explained in terms of Specific
Furnace Fuel Consumption (SFFC). The unit of
Furnace Coefficient is kg/m3
/K.
V. EXPERIMENTAL SETUP
The experimental setup is shown in Figure 2. By
operating the three valves simultaneously we can get,
combustion air for burning of fuel with and without
preheating. Closing the valve V1, V3 and opening
V2, it is a system without combustion air preheating.
Closing the valve V2 and opening the valve V1, V3 it
is a system with combustion air preheating
Figure 2 Schematic representation of APH with three
valves
A Sandwich type valves is used for making these
arrangements, ie for doing exhaust gas analysis with
and without air-preheater (APH).
E B Muhammedshafiet al. Int. Journal of Engineering Research and Applications www.ijera.com
ISSN: 2248-9622, Vol. 5, Issue 9, (Part - 1) September 2015, pp.118-120
www.ijera.com 120|P a g e
It is welded in the pipe way between blower and
burner. Air preheating system is working with
combustion air flowing in the counter clock wise
direction around the chimney. Since area of heat
transfer is more, radiation heat loss is more. Due to
this, combustion air is not getting heated much. So
the APH system around the chimney is insulated. The
insulation on APH system is done by pasting ceramic
wool around the system. For this Sodium Silicate is
used as gum.
VI. RESULTS AND DISCUSSION
The fuel saving or the reduction in Specific
Furnace Fuel Consumption with the introduction of
combustion air pre-heating system for different
furnace operations Normalizing, Stress Relieving,
tempering and Annealing is as shown below.
Sl
No:
Operation
Weig
ht
(kg)
Total
Time
(hr)
Reducti
on in
SFFC
(Lit/Ton
/hr)
fuel
savings
(Liter)
1
Normalizin
g
6168
15.5 1.712 164
2 Stress
Relieving
6244 10.9 1.274 87
3 Tempering 5509 15.8 0.696 61
4 Annealing 5956 15.7 1.672 156
Table 1 Fuel Savings with Exhaust Damper and APH
System
The Table 1 describes the quantity of fuel saved
for different operations. For Normalizing operation
with an average weight of 6.168 Ton material for
15hr 30min operation 164 litre of diesel was
saved.For Stress relieving operation with an average
weight of 6.244 Ton material for 10hr 54min
operation 87 litre of diesel was saved .For Tempering
operation with an average weight of 5.509 Ton
material for 15hr 48 min operation 61 litre of diesel
was saved. For Annealing operation with an average
weight of 5.956 Ton material for 15hr 42 min
operation 156 litre of diesel was saved.
Emission Parameters
With Air
Pre-
heating
Without
Air Pre-
heating
Combustion Air Temperature
o
C
103 45
Flue Gas Temperature o
C 544 634
Oxygen in % 14 12
Carbon dioxide in % 5 7
Carbon monoxide in PPM 33 46
Table 2 Exhaust Gas Parameters
With introduction of APH system Carbon
Monoxide emission is reduced from 46 ppm to 33
ppm, ie combustion is improved by an amount 29 %.
Flue gas temperature is reduced from 634o
C to
544o
C. With APH system combustion air temperature
is increased from 45o
C to 103o
C.
VII. CONCLUSION
With introduction APH ie. Combustion Air Pre-
Heating, (CO) Carbon Monoxide emission is reduced
by 29 %. The other benefits obtained by the APH
system are that, the temperature of flue gas is
reduced and diesel consumption for different heat
treatment processes are reduced.
REFERENCE
[1] Manish Kumar Tiwari, Achintya
Mukhopadhyay, Dipankar Sanyal, “Process
modeling for control of a batch heat
treatment furnace with low NOx radiant tube
burner”, Elseiver, Energy Conversion and
Management 46 2093–2113,2005.
[2] M. Hasanuzzaman1, R. Saidur and N. A.
Rahim, “Energy, exergy and economic
analysis of an annealing furnace”,
International Journal of the Physical
Sciences Vol. 6(6), pp. 1257-1266, 18
March, 2011.
[3] K.K. Alaneme and S.O. Olanrewaju,
“Design of a Diesel Fired Heat-Treatment
Furnace”, Journal of Minerals & Materials
Characterization & Engineering, Vol. 9,
No.7, pp.581-591, 2010.
[4] Jeetendra Mohan Khare, Sandip Kumar
Mishra, ShashankShrivastava, “Improving
Thermal Efficiency Of Push Type Furnace
In A Hot Re-Rolling Steel Mill By Direct
Method : Case Study”, International Journal
of Scientific Engineering and Technology
(ISSN : 2277-1581) Volume 2 Issue 4, pp :
288-290 1 April 2013.
[5] Radha Krishnan Purushotham an,
“Evaluation and Improvement of Heat Treat
Furnace Model”, A Dissertation Submitted
to the Faculty of the worcester polytechnic
institute in partial fulfillment of the
requirements for the Degree of Doctor of
Philosophy in Manufacturing Engineering
June 2008.
[6] Dr Liza Sreejith, Effect of preheating of
combustion air on Carbon Monoxide
emission in heat treatment furnace. Personal
Discussion. Professor in Engineering
Chemistry, National Institute of Technology,
Calicut on 2nd
June 2015

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Effect of Combustion Air Pre-Heating In Carbon Monoxide Emission in Diesel Fired Heat Treatment Furnace

  • 1. E B Muhammedshafiet al. Int. Journal of Engineering Research and Applications www.ijera.com ISSN: 2248-9622, Vol. 5, Issue 9, (Part - 1) September 2015, pp.118-120 www.ijera.com 118|P a g e Effect of Combustion Air Pre-Heating In Carbon Monoxide Emission in Diesel Fired Heat Treatment Furnace E B Muhammed Shafi, Mr. PadmanabhaAdiga, Dr. T C Mohankumar PG Scholar MES Engineering College Kuttippuram, Kerala, India Dy Manager, Quality Assurance Peekay Steels Castings (P) Ltd Nallalam, Calicut, Kerala Professor MES Engineering College Kuttippuram, Kerala, India ABSTRACT This paper describes the effect of combustion air pre- heating in Diesel fired heat Treatment Furnace. The main heat treatment processes are Normalizing, Tempering, Hardening, Annealing, Solution Annealing and Stress Relieving. The emission of carbon monoxide is measured with combustion air pre-heating and without pre- heating. The results are then compared and it is found that the emission of CO is reduced by 29.12%. With the Combustion air pre-heating a considerable reduction in Specific Furnace Fuel Consumption (SFFC) is obtained. The test was caaried out at Peekay Steels Casting (P) ltd, Nallalam, Calicut. General Terms: Heat Treatment Furnace Keywords: SFFC, Pre- heating, Combustion,Emission I. INTRODUCTION Heat treatment is a process on metals or alloys to cause relief of internal stress, harden or strengthen metals, improve machinability, change grain size etc... Different types heat treatment process are Annealing, Normalizing, Hardening, Tempering etc.. It involves heating and cooling of metals or alloys at different rates depending up on requirements. In the company Peekay Steels there are three diesel fired furnaces, four LPG fired furnace of which one is idle and one is under construction and one electric furnace. The capacities of three different diesel fired furnaces are 7 ton, 10 ton and 13 ton. The objective of the project is to improve the thermal efficiency of a diesel fired heat treatment furnace and to reduce diesel consumption by some experimental investigations. Here for the sake of furnace a new term (SFFC) Specific Furnace Fuel Consumption is introduced. It is the amount of diesel consumed per unit tonnage of material processed in the furnace and per hour of furnace operation. Our objective is to reduce SFFC or increase thermal or furnace efficiency. Thermal efficiency improvement is done by reducing diesel consumption in the furnace without affecting homogeneity in heat treatment. This is achieved by 1. Increasing the pressure inside the furnace chamber by adjusting the damper plate in the exhaust gas pipe or chimney. 2. Utilizing the heat produced more effectively which includes. a. Pre-heating the air for combustion.’’ II. FURNACE OPERATIONS Different furnace operations or heat treatment processes carried out in Peekay Steels are Normalizing, Tempering, Annealing, Solution Annealing, Stress Relieving etc. All heat treatment process consists of Heating, Soaking and Cooling. All these processes are done at a specific rate depending upon the requirement. Heating means rising the temperature of the stock from room temperature to soaking temperature at a specific rate. Soaking means maintaining the temperature of the stock at soaking temperature for a particular time.Cooling means bringing down the temperature of stock to a predetermined temperature or room temperature at a particular rate depending up on the requirement. Figure 1 Graphical representation of heat treatment RESEARCH ARTICLE OPEN ACCESS
  • 2. E B Muhammedshafiet al. Int. Journal of Engineering Research and Applications www.ijera.com ISSN: 2248-9622, Vol. 5, Issue 9, (Part - 1) September 2015, pp.118-120 www.ijera.com 119|P a g e All heat treatment processes can be represented graphically as shown above. It shows the variation of stock temperature with time. Here AB represents heating process, BC represents soaking process and CD represents cooling process. Area under the curve give an indication of energy absorbed by the stock. Time t1, t2 and t3 are time of heating , soaking and cooling respectively. These times are used for calculation of SFFC. If cooling process are quenching, normal cooling or forced air cooling, then for calculation of SFFC time t3 is not used. If cooling rate needed is less than the rate of above said cooling processes, time t3 will be used for SFFC calculation (For getting less cooling rate, fuel is to be burned ) III. FURNACE EFFICIENCY Furnace efficiency (ƞf) greatly depends up on Flame temperature, Air/fuel ratio, Furnace structure, Insulation level of furnace, Radiation loss from the furnace and Method of Furnace operation. Generally Furnace efficiency or Thermal efficiency is defined as the percentage of heat input that is effectively utilized to heat the stock. ƞf = Heat in the stock ℎ Heat in the fuel consumed for heating the stock = M ∗ C ∗ T−Tamp ∗ 1000 L ∗ρ∗ Cv Let (T-Tamp) = ∆T ƞf = M ∗ C ∗∆T ∗ 1000 L ∗ρ∗ Cv (1) Where M Tonnage of material processed in the furnace (*1000 kg) C  Specific heat of material processed in the furnace (490 J/kg/K) T Soaking temperature (K) TampAmbient temperature (K) L Amount of diesel consumed in the furnace (Liter) 𝛒Density of diesel (840 kg/m3 ) CvCalorific value of diesel (43200 kJ/kg) Here the fuel used to heat the stock is diesel IV. SPECIFIC FURNACE FUEL CONSUMPTION (SFFC) The efficiency of the furnace can be judged by measuring the amount of diesel needed per unit time per unit weight of the material. It is known as Specific Furnace Fuel Consumption (SFFC). It’s unit is Liter/Ton/hr. As far as a furnace is concerned SFFC and Thermal efficiency are related very much deeply and constant can be introduced, known as furnace coefficient SFFC = Amount of diesel consumed in liter per unit tonnage of material processed per unit Hour. = L M ∗ t M L = 1 SFFC ∗ t (2) (2) in (1) gives Ƞf = ( 1 SFFC ∗ t ) * ( C ∗∆T ρ∗Cv ) * 1000 From the above equation we get a new equation relating furnace efficiency and SFFC with parameters furnace operating time and soaking temperature Ƞf * SFFC = ( ∆T t ) * ( C ρ∗Cv ) * 1000 (3) Substituting the values of the constant (C, and Cv), we get equation (3) as Ƞf * SFFC = ( ∆T t )* ( 490 840 ∗ 43200 ∗ 1000 ) * 1000 Ƞf * SFFC = ( ∆T t ) * 13.344 * 10-6 The constant 13.344*10-6 is known as Furnace Coefficient. This coefficient is dependent only on specific heat value of the material, which is processed in the heat treatment furnace, density of the fuel which is used to heat the stock and lower calorific value of the fuel. Usually performance of a heat treatment furnace is explained in terms of Specific Furnace Fuel Consumption (SFFC). The unit of Furnace Coefficient is kg/m3 /K. V. EXPERIMENTAL SETUP The experimental setup is shown in Figure 2. By operating the three valves simultaneously we can get, combustion air for burning of fuel with and without preheating. Closing the valve V1, V3 and opening V2, it is a system without combustion air preheating. Closing the valve V2 and opening the valve V1, V3 it is a system with combustion air preheating Figure 2 Schematic representation of APH with three valves A Sandwich type valves is used for making these arrangements, ie for doing exhaust gas analysis with and without air-preheater (APH).
  • 3. E B Muhammedshafiet al. Int. Journal of Engineering Research and Applications www.ijera.com ISSN: 2248-9622, Vol. 5, Issue 9, (Part - 1) September 2015, pp.118-120 www.ijera.com 120|P a g e It is welded in the pipe way between blower and burner. Air preheating system is working with combustion air flowing in the counter clock wise direction around the chimney. Since area of heat transfer is more, radiation heat loss is more. Due to this, combustion air is not getting heated much. So the APH system around the chimney is insulated. The insulation on APH system is done by pasting ceramic wool around the system. For this Sodium Silicate is used as gum. VI. RESULTS AND DISCUSSION The fuel saving or the reduction in Specific Furnace Fuel Consumption with the introduction of combustion air pre-heating system for different furnace operations Normalizing, Stress Relieving, tempering and Annealing is as shown below. Sl No: Operation Weig ht (kg) Total Time (hr) Reducti on in SFFC (Lit/Ton /hr) fuel savings (Liter) 1 Normalizin g 6168 15.5 1.712 164 2 Stress Relieving 6244 10.9 1.274 87 3 Tempering 5509 15.8 0.696 61 4 Annealing 5956 15.7 1.672 156 Table 1 Fuel Savings with Exhaust Damper and APH System The Table 1 describes the quantity of fuel saved for different operations. For Normalizing operation with an average weight of 6.168 Ton material for 15hr 30min operation 164 litre of diesel was saved.For Stress relieving operation with an average weight of 6.244 Ton material for 10hr 54min operation 87 litre of diesel was saved .For Tempering operation with an average weight of 5.509 Ton material for 15hr 48 min operation 61 litre of diesel was saved. For Annealing operation with an average weight of 5.956 Ton material for 15hr 42 min operation 156 litre of diesel was saved. Emission Parameters With Air Pre- heating Without Air Pre- heating Combustion Air Temperature o C 103 45 Flue Gas Temperature o C 544 634 Oxygen in % 14 12 Carbon dioxide in % 5 7 Carbon monoxide in PPM 33 46 Table 2 Exhaust Gas Parameters With introduction of APH system Carbon Monoxide emission is reduced from 46 ppm to 33 ppm, ie combustion is improved by an amount 29 %. Flue gas temperature is reduced from 634o C to 544o C. With APH system combustion air temperature is increased from 45o C to 103o C. VII. CONCLUSION With introduction APH ie. Combustion Air Pre- Heating, (CO) Carbon Monoxide emission is reduced by 29 %. The other benefits obtained by the APH system are that, the temperature of flue gas is reduced and diesel consumption for different heat treatment processes are reduced. REFERENCE [1] Manish Kumar Tiwari, Achintya Mukhopadhyay, Dipankar Sanyal, “Process modeling for control of a batch heat treatment furnace with low NOx radiant tube burner”, Elseiver, Energy Conversion and Management 46 2093–2113,2005. [2] M. Hasanuzzaman1, R. Saidur and N. A. Rahim, “Energy, exergy and economic analysis of an annealing furnace”, International Journal of the Physical Sciences Vol. 6(6), pp. 1257-1266, 18 March, 2011. [3] K.K. Alaneme and S.O. Olanrewaju, “Design of a Diesel Fired Heat-Treatment Furnace”, Journal of Minerals & Materials Characterization & Engineering, Vol. 9, No.7, pp.581-591, 2010. [4] Jeetendra Mohan Khare, Sandip Kumar Mishra, ShashankShrivastava, “Improving Thermal Efficiency Of Push Type Furnace In A Hot Re-Rolling Steel Mill By Direct Method : Case Study”, International Journal of Scientific Engineering and Technology (ISSN : 2277-1581) Volume 2 Issue 4, pp : 288-290 1 April 2013. [5] Radha Krishnan Purushotham an, “Evaluation and Improvement of Heat Treat Furnace Model”, A Dissertation Submitted to the Faculty of the worcester polytechnic institute in partial fulfillment of the requirements for the Degree of Doctor of Philosophy in Manufacturing Engineering June 2008. [6] Dr Liza Sreejith, Effect of preheating of combustion air on Carbon Monoxide emission in heat treatment furnace. Personal Discussion. Professor in Engineering Chemistry, National Institute of Technology, Calicut on 2nd June 2015