Energy Optimizing Furnace

Energy Optimizing Furnace

Energy optimizing furnace (EOF) is a primary steel making furnace. This process was developed by the mini steelworks pioneer Willy Korf along with his colleagues. This process is presently being operated in India at JSW SISCOL plant and at Hospet Steel plant of Mukand. The first unit went into production in1982.


EOF is a melting/refining furnace for the production of liquid steel. It is having a scrap preheater.  The basic principle consists of working with combined submerged and atmosphere oxygen blown in an initial charge containing hot metal, preheated solid scrap and fluxes for slag formation. Scrap is preheated to around 850 deg C by the sensible heat in the off gas in one or two chambers located above the furnace roof. Blown submerged oxygen reacts with the carbon from hot metal and generates CO bubbles that travel through the liquid bath to the furnace atmosphere. Here CO is burnt to CO2 by the oxygen blown through atmospheric injectors and supersonic lances. The bubbling of CO generates a very strong stirring and increases greatly the bath surface. This allows transfer of a good amount of heat to the bath. The process also constitutes deslagging and formation of the secondary slag.

The process has possibility of using high percentage of solid charge (even greater than 40 %). The process owes its thermal efficiency due to the following factors:

i)             Chemical energy released due to the exothermic reactions between the injected oxygen and the various elements in the bath including added carbon.

ii)           Chemical energy released from the gaseous oxidation reactions in the furnace atmosphere involving CO and H2 released from the bath.

iii)          Sensible heat transferred by the hot gases from the furnace to the cold scrap charged into the pre heater 

Steel quality aspects

In EOF all types and qualities of steels can be produced. The tapped steel is having similar chemistry as been obtained from combined blowing steel making process. Due to the continuous deslagging during the process good amount of dephosphorization (up to 0.008 %) and desulphurization (Up to 0.025 %)  is achieved.

Since EOF process has a high percentage (greater than 60 %) of hot metal in the charge, the tapped liquid steel has a very low content of tramp elements. This is of advantage while producing special steel grades such as die forging steels, special clean steels and steels for seamless pipes etc.

The high partial pressure of CO during the whole blowing period results to very low nitrogen and hydrogen levels in the  tapped steel. In case of high quality and special steels tapped liquid steel is treated in secondary steel making units as per need. 

Basic characteristics:

Energy Optimizing furnaces of standard capacities 30/40t, 60/80t and 100/120t are available. The furnaces have the following basic features and dimensions:

  1. Hearth surface in the range of 6.6 to 22.0 Sq m
  2. Shell diameter is in the range of 5.3 to 7.5 m
  3. Total height from working platform to top level is about 17 to 25 m.
  4. There are one or two numbers of scrap pre heater stages
  5. Tilting angle for tapping and deslagging is up to 8 deg.

The schematic diagram of an EOF is given in Fig 1.


                                  Fig. 1 Schematic diagram of EOF

Operating parameters

The following are the typical operating data of an EOF:

  1. Furnace availability: – 340 days per annum
  2. Charge composition: hot metal – 50 % – 90 %
  3. solid charge – 50 % – 10 %
  4. Tap to tap time: – 30 – 50 minutes
  5. Tapping temperature – 1700 deg. C without ladle furnace, 1650 deg. C with ladle furnace
  6. Bottom exchange (between campaigns): – 12 to 24 hours.

The typical specific consumption per ton of liquid steel are:

i)     Hot Metal – 778 Kg/t (70 %)

ii)   Pig iron and Steel scrap – 333 Kg/t (30 %)

iii)  Metallic yield – 87 to 89 %

iv)  Lime – 45 Kg/t (depending on P in hot metal)

v)    Oxygen – 50 to 70 N Cum/t

vi)  Nitrogen – 3 to 5 N Cum/t

vii) Fuel – 5 to 10 M Cal/t

Description of main equipment

EOF is having the following major equipments/components.

  1. Two numbers bottom cars of shuttle type are used for quick bottom change during a new campaign. One bottom car carries the the EOF in operation while the second car carries the other bottom and is parked for relining at one or other side of the bottom under use. Both cars are equipped with roll collar tracks to tilt the furnace for tapping or deslagging. Tilting is performed by high speed hydraulic cylinders. This allows slag free tapping.
  2. Energy optimizing furnace is equipped with bottom refractory lining, split water cooled shell, water cooled roof, sealing between the furnace and scrap preheater, hot metal launder, steel tapping launder, submerged tuyeres, atmosphere injectors and supersonic lance for oxygen blowing, oxy-fuel burners for heating-up new bottom.
  3. Scrap preheater placed immediately above the furnace is provided with water cooled tilting fingers to support the solid metallic charge which is heated by the furnace off-gas. At the time of scrap charging, the fingers tilt and release the preheated scrap into the EOF bottom. Water-cooled inclined chute is also provided below the fingers for additions into the furnace.
  4. Other components of an EOF are air injectors for post combustion of carbon monoxide, water sprays to control the off-gas temperature before the scrap layer, off-gas uptake, water cooled sliding door and scrap charging system both placed at the scrap preheater top.

A view of the EOF from the working platform is shown in Fig 2.

Fig 2 View of the EOF from working platform

Scrap preheater:

Scrap preheater is an essential part of the EOF and is provided with one or two layers of water cooled fingers on which cold scrap is placed. Hot off-gas evolved from the EOF flow through the scrap and heating it up to 850 deg C. The fingers are tilted for dropping the scrap into the furnace.

Process flow of the EOF process is at Fig 3.

Fig 3 Process flow of the EOF process

A typical cross section of the shop is shown in Fig 4

Fig 4 Typical cross section of the shop

Advantages of EOF:

Various advantages of the EOF process are as follows:

  1. There is a wide flexibility with regards to the metallic charge mix. The advantages are more when hot metal availability is less say 50 % from the iron making process. There is flexibility also with respect to solid charge (scrap, pig iron).
  2. The process is advantageous in case of low availability of electrical energy.
  3. The process has high productivity and good furnace availability
  4. The produced liquid steel has good metallurgical properties, specially with regards to dephosphorization and desulphurization
  5. The liquid steel has low content of tramp elements.
  6. The inclusion level in the steel is reduced greatly due to continuous flushing of slag during the blow and also due to slag free tapping
  7. The tapped steel can be directly transferred to the continuous casting machine or can be sent to secondary metallurgy units.
  8. EOF has simple process control and can be fully automated.
  9. The process is energy efficient.
  10. The process works under slightly negative pressure hence there is hardly any dust emissions.
  11. There is low noise level.
  12. Flexibility with respect to solid charge materials (scrap, pig iron) is another attraction.

Comments on Post (15)

  • subhasis ghosh

    good technology

    • Posted: 19 February, 2013 at 06:12 am
    • Reply
  • Gunajit Roy

    Well defined and it is great for flexibility and order based heats to service. Hope, no quality control issues.

    • Posted: 21 February, 2013 at 08:45 am
    • Reply
    • Satyendra

      There are no quality control issues

      • Posted: 21 February, 2013 at 09:19 am
      • Reply
  • walter Cassete

    I woud like to know about refractories consumptions ( mixes and bricks) in this process
    Thanks Walter Cassete

    • Posted: 25 March, 2013 at 19:59 pm
    • Reply
    • Satyendra

      It will be around 2.5 to 3 Kg/ton

      • Posted: 28 March, 2013 at 03:22 am
      • Reply
  • D.C.Singhal

    The Schematic (Fig.1) shows the the taphole below the bath level requiring plugging. Your text mentions that tapping is done by tilting the furnace bottom. If so, the tapping launder should be above the metal line. Would be grateful if you please clarify.

    • Posted: 03 July, 2013 at 15:05 pm
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    • Satyendra

      Tap hole is situated below the bath level and tapping and de slagging is done by tilting to empty out the furnace

      • Posted: 03 July, 2013 at 23:00 pm
      • Reply
  • S.K.Das

    What will be connected power required for a 30t EOF and can it be compatible with a 250 Cu.M MBF to produce steel billets from the Molten Pig Iron from the MBF.

    • Posted: 09 July, 2013 at 13:50 pm
    • Reply
    • Satyendra

      specific Power requirement is in the range of 45 to 50 kWh/ ton of liquid steel and specific hot metal consumption is in the range of 800 to 900 Kg/ton of liquid steel.

      • Posted: 09 July, 2013 at 15:35 pm
      • Reply
  • S.K.Das

    What will be the connected power load required to operate this furnace

    • Posted: 09 July, 2013 at 17:40 pm
    • Reply
    • Satyendra

      The connected power will be around 3 MW.

      • Posted: 09 July, 2013 at 21:23 pm
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      • S.K.Das

        I have send u a message regarding my project of 350 Cu.M and 30T EOF 30T LF please revert back me asap my email id is

        • Posted: 10 July, 2013 at 08:02 am
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      • S.K.Das

        I have send u a message regarding my project of 350 Cu.M MBF and 30T EOF 30T LF please revert back me asap.

        • Posted: 10 July, 2013 at 08:03 am
        • Reply
  • Navee

    How to maintain the taphole & to avoid slag entraped into steel in tapping

    • Posted: 27 August, 2013 at 13:00 pm
    • Reply
  • Navee

    How to make slag fomay sometimes very difficult to flushing slag.

    • Posted: 27 August, 2013 at 13:14 pm
    • Reply

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