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REHEATING FURNACE
Presented By:
Vikas Vishnuchandra Yadav
Kalyani Charitable Trust's
Late G. N. Sapkal College of Engineering
Department of Mechanical Engineering
PRESENTAION ON :
FURNACES
 Design and manufacture furnaces on
turn key basis for the following
industries
Rolling Mills
Forging Plants
Heat Treatment Centers
Wire Drawing Plants
Aluminum Plant
Steel Plants
 Guaranteed fuel consumption of as
low as 33 ltr/ton for billet reheating
furnaces
DESIGN METHODOLOGY
 Capacity Rating
 Material Handeling
 Hearth Loading
 Heat Loading & Zoning
 Automation levels
 Planning of Combustion System
CAPACITY RATING
 Depends on the size and mix of produce to be preheated.
 The material of the billets play an important part in
finalizing capacity.
MATERIAL HANDLING
 Reheating furnaces can be divided into the following
categories:
 Pusher Type
 Walking beam /Walking hearth
 Rotary hearth
 Considering the charge we plan the material handling
HEARTH LOADING
 Based on the type of furnace hearth loading is
determined , with the focus on
 heat transfer ,
 pattern of heating i.e Top Heating or Top and Bottom heating
HEAT LOADING AND
ZONING
 Considering the design and capacity of the furnace
different types and sizes of burners are recommended in
the different zones of the furnace.
 Types of Burners
 LAP Burners
 High Velocity/ Oxy Fuel
AUTOMATION IN THE FURNACE
 In order to achieve greater efficiency in the
furnace and further increase production and
reduce scale losses the following automation in
the furnace can be carried out:
 Temperature Control
 Pressure Control
 Air/Fuel or Oxygen/Fuel Ratio Control
OXY FUEL TECHNOLOGY
 Reduced Emissions
NOx emissions are reduced substantially with a oxy-fuel conversion.
 Improved Efficiency and Production
Improvement in fuel efficiency as compared with traditional air-fuel
furnaces. The energy savings partially offsets the cost of oxygen. There
scale formation also comes down to 0.3%
 Increased Furnace Refractory Life
Temperature homogeneity of the furnace increases thus minimizing the
chances of thermal shocks in the refractory
 Simplified Operation
With no recuperator, the furnace operation and maintenance are simplified
CFD OF FURNACE
RESULTS OF CFD
ANALYSIS
CASE STUDY
Revamping of Furnace at TATA SSL,
BOISAR
PROBLEMS FACED BY
SSL IN THE FURNACE
 High Fuel Consumption up to 47 ltr/ton
 Improper Soaking of the Billets
 High Power Consumption by the Mill
 Frequent break down of the Mill
 The Furnace was only producing 36 Ton against the
designed capacity of 45 ton
MODIFICATIONS
 Heat Load calculation were done and accordingly the
combustion equipment's were changed
 Burners
 Blowers
 Recuperators
 Air and Oil pipeline were redesigned and modified
accordingly.
 Complete refractory lining was done again
 Walls
 Roof
 Hearth
 Water Cooled skid
RESULTS ACHIEVED
 Increase in production by 16-25% from 36 tons/hr to 42-
45 tons/hr.
 Fuel consumption reduced by 23-30% from 47 ltrs/ton to
33-36 ltrs/ton.
 Electrical Power consumption reduced by about 8%.
 Reduction in breakdowns due to better quality heated
billets
FURNACE DESIGN
 Designed a Top and Bottom fired furnace with
water cooled skids and PID based control.
 The furnace is designed for firing Mixed Gas
(Blast Furnace Gas and Producer Gas). The gas
will be either enriched with Oxygen or
supplementary firing of furnace oil will be done.
ELEVATION OF THE
FURNACE
BURNERS
 Oil Burners
 Gas Burners
 Dual Firing Burning Systems
 High Velocity Burners
(OIL/GAS)
 Pilot Burner for Coke Oven
Gas/ LPG/NG
 Coke Oven & Blast Furnace
Burner
RECUPERATORS
 Recuperators with flue temperatures of
up to 950oC
 Preheat temperature of combustion air
as high as 450oC
 Guaranteed savings of 15-20% and a
minimum life of 3 years for
Recuperators
THANK YOU!
“ Adopt eco-friendly technologies”

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Reheating Furnace in Rolling Mill Industries

  • 1. REHEATING FURNACE Presented By: Vikas Vishnuchandra Yadav Kalyani Charitable Trust's Late G. N. Sapkal College of Engineering Department of Mechanical Engineering PRESENTAION ON :
  • 2. FURNACES  Design and manufacture furnaces on turn key basis for the following industries Rolling Mills Forging Plants Heat Treatment Centers Wire Drawing Plants Aluminum Plant Steel Plants  Guaranteed fuel consumption of as low as 33 ltr/ton for billet reheating furnaces
  • 3. DESIGN METHODOLOGY  Capacity Rating  Material Handeling  Hearth Loading  Heat Loading & Zoning  Automation levels  Planning of Combustion System
  • 4. CAPACITY RATING  Depends on the size and mix of produce to be preheated.  The material of the billets play an important part in finalizing capacity.
  • 5. MATERIAL HANDLING  Reheating furnaces can be divided into the following categories:  Pusher Type  Walking beam /Walking hearth  Rotary hearth  Considering the charge we plan the material handling
  • 6. HEARTH LOADING  Based on the type of furnace hearth loading is determined , with the focus on  heat transfer ,  pattern of heating i.e Top Heating or Top and Bottom heating
  • 7. HEAT LOADING AND ZONING  Considering the design and capacity of the furnace different types and sizes of burners are recommended in the different zones of the furnace.  Types of Burners  LAP Burners  High Velocity/ Oxy Fuel
  • 8. AUTOMATION IN THE FURNACE  In order to achieve greater efficiency in the furnace and further increase production and reduce scale losses the following automation in the furnace can be carried out:  Temperature Control  Pressure Control  Air/Fuel or Oxygen/Fuel Ratio Control
  • 9. OXY FUEL TECHNOLOGY  Reduced Emissions NOx emissions are reduced substantially with a oxy-fuel conversion.  Improved Efficiency and Production Improvement in fuel efficiency as compared with traditional air-fuel furnaces. The energy savings partially offsets the cost of oxygen. There scale formation also comes down to 0.3%  Increased Furnace Refractory Life Temperature homogeneity of the furnace increases thus minimizing the chances of thermal shocks in the refractory  Simplified Operation With no recuperator, the furnace operation and maintenance are simplified
  • 12. CASE STUDY Revamping of Furnace at TATA SSL, BOISAR
  • 13. PROBLEMS FACED BY SSL IN THE FURNACE  High Fuel Consumption up to 47 ltr/ton  Improper Soaking of the Billets  High Power Consumption by the Mill  Frequent break down of the Mill  The Furnace was only producing 36 Ton against the designed capacity of 45 ton
  • 14. MODIFICATIONS  Heat Load calculation were done and accordingly the combustion equipment's were changed  Burners  Blowers  Recuperators  Air and Oil pipeline were redesigned and modified accordingly.  Complete refractory lining was done again  Walls  Roof  Hearth  Water Cooled skid
  • 15. RESULTS ACHIEVED  Increase in production by 16-25% from 36 tons/hr to 42- 45 tons/hr.  Fuel consumption reduced by 23-30% from 47 ltrs/ton to 33-36 ltrs/ton.  Electrical Power consumption reduced by about 8%.  Reduction in breakdowns due to better quality heated billets
  • 16. FURNACE DESIGN  Designed a Top and Bottom fired furnace with water cooled skids and PID based control.  The furnace is designed for firing Mixed Gas (Blast Furnace Gas and Producer Gas). The gas will be either enriched with Oxygen or supplementary firing of furnace oil will be done.
  • 18. BURNERS  Oil Burners  Gas Burners  Dual Firing Burning Systems  High Velocity Burners (OIL/GAS)  Pilot Burner for Coke Oven Gas/ LPG/NG  Coke Oven & Blast Furnace Burner
  • 19.
  • 20. RECUPERATORS  Recuperators with flue temperatures of up to 950oC  Preheat temperature of combustion air as high as 450oC  Guaranteed savings of 15-20% and a minimum life of 3 years for Recuperators
  • 21. THANK YOU! “ Adopt eco-friendly technologies”