Reheating Furnaces and their Types
Reheating Furnaces and their Types
Reheating furnaces are used in hot rolling mills to heat the steel stock (Billets, blooms or slabs) to the rolling temperatures of around 1200 deg C which is suitable for plastic deformation of steel and hence for rolling in the mill. The heating process in a reheating furnace is a continuous process where the steel stock is charged at the furnace entrance, heated in the furnace, and discharged at the furnace exit. Heat is transferred to the steel stock (Fig 1) during its traverse through the furnace mainly by means of convection and radiation from the burner gases and the furnace walls.
Fig 1 Heat transfer mechanism in a reheating furnace
The charging temperature of the steel stock can range from ambient temperature to 800 deg C. The target exit temperature of the steel stock is governed by the requirement of the process of rolling which is dependent on the rolling speed, stock dimension and steel composition. Steel quality aspects put constraints on temperature gradient and surface temperature. Fuel used in these furnaces can be solid, liquid, or gaseous fuel. The schematic diagram of a pusher type reheating furnace is shown at Fig 2.
Fig 2 Schematic diagram of a pusher type reheating furnace
The size of reheating furnace is usually expressed as the capacity to supply hot steel stock to the rolling mill from the cold stock and is expressed in tons per hour. The energy efficiency of reheating furnace is usually defined as increase of steel stock heat content when heated from 10 deg C to 1200 deg C divided by the fuel energy (latent heat plus sensible heat) used for it. Typical longitudinal section of a reheating furnace is shown in Fig 3.
Fig 3 Typical longitudinal section of a reheating furnace
Many design features of the furnace affects the energy efficiency. These include (i) type of burners, (ii) furnace dimensions, (iii) number of furnace zones, (iv) type of wall and roof insulation, (v) skid design, and (vi) preheating of fuel and combustion air in recuperators by the hot flue gases coming out from the furnace exit. An efficient furnace is designed in such a way so that in a given time the steel stock as per furnace capacity is heated to a uniform temperature with the least possible fuel and man-hours. The parameters important for furnace design include (i) the quantity of heat to be imparted to the charge, (ii) generation of sufficient heat which is is available within the furnace to heat the steel stock as well as to overcome all steel losses, (iii) transfer of generated heat to the surface of the steel stock to be heated, (iv) equalization of temperature within the steel stock, and (v) loss of heat from the furnace to the minimum.
Operational practices are also important for the energy efficiency. The ideal situation is to run the furnace at the rated capacity with one type of steel stock with same composition and uniform dimension. But in practice, this does not happen and the factors which affect the furnace efficiency are (i) steel stock of the different dimension, composition and initial temperature can reside in the furnace at the same time, (ii) rolling delays can slow down or stop the movement of steel stock in the furnace, (iii) fuel composition and availability can vary, and (iv) burners and furnace internal conditions have been degraded.
Energy efficiency of a furnace is normally depicted by a Sankey diagram. A typical Sankey diagram for a reheating furnace with cold charging is shown in Fig 4.
Fig 4 Typical Sankey diagram of a reheating furnace
Classification of reheating furnaces
The reheating furnace classification can be done in four ways namely (i) based on the method of heating, (ii) based on method of charging the reheating furnace, (iii) based on the movement of steel stock in the reheating furnace, and (iv) based on the heat recovery methods.
Based on the method of heating, a reheating furnace can be combustion heating type or electrical heating type. The combustion heating type furnace can use solid, liquid, or gaseous fuel.
Based on the method of charging, the reheating furnace can be classified as batch type or continuous type. In batch furnaces the charged material remains in a fixed position on the hearth until heated to rolling / forging temperature while in continuous furnaces the charged material moves through the furnace and is heated to rolling temperature as it progresses through the furnace.
Based on the movement of steel stock inside the furnace, continuous furnace can be further classified as pusher furnace, rotary hearth furnace, walking beam furnace, walking hearth furnace, and roller hearth furnace.
Based on heat recovery, the reheating furnace can be either regenerative type or recuperative type. Regenerating type reheating furnace uses regenerative burners while recuperative type furnace uses recuperators for heat recovery from the exhaust gases.
Different types of reheating furnaces are described below.
These are the older type of furnaces which are capable of heating all grades and sizes of steel. The steel stock to be heated in this type of furnace is charged and drawn through front doors by a charging machine. These furnaces vary in size ranging from hearths of less than a square meter with a single access door to those with hearths of around 6 metres (m) in depth and around 15 m in length and with 5 to 6 numbers of access doors. Batch furnaces can be operated to heat materials to temperatures around 1320 deg C more satisfactorily than a continuous furnace. They can also be used as a reservoir for holding hot material directly from the primary mill for later rolling in the finishing mill.
The disadvantages of batch furnaces are (i) high capital investment per unit of production, (ii) low hearth area efficiency, (iii) high man hours required per ton of heated product, (iv) practically no flexibility, and (v) limitation on length of pieces to be heated.
Pusher type furnace
In the pusher type of furnace, cold steel stock is pushed forward with the help of pushers at the charging side. Earlier, these furnaces were designed for heating billets or smaller sections of blooms. The hearth of earlier furnaces was short in length and sloped downward longitudinally towards the discharge end in order to permit easy passage of steel stock through the furnace. Presently pusher furnaces are longer with hearths of around 25 m to 30 m in length. These furnaces are equipped with either top firing or top and bottom firing. These furnaces normally have three zones namely (i) preheating zone, (ii) heating zone, and (iii) soaking zone. Multiple zone furnaces such as five zone slab reheating furnace have also been designed and operated.
Cold steel stock can be charged in such furnace either from the end or through a side door. In either case, the steel stock is moved forward by pushing the last piece charged with a pusher at the charging end. With each pushing of the cold steel stock against the continuous line of material, a heated piece is discharged at the discharge end either by gravity through an end door upon a roller table feeding the rolling mill, or pushed through a side door to the mill roller table by suitable manual or mechanical means, or withdrawn through the end door by a mechanical extractor.
Advantages of the pusher type furnaces include (i) high production per unit capital investment, (ii) high hearth area efficiency, (iii) higher specific production per unit of space utilized, (iv) low maintenance cost, (v) ease of charging and discharging of material, (vi) lower temperature differences between two pieces of material pushed, (vii) more control of the rate of heating at all temperature levels, (viii) gradual rise in temperature permits charging of all grades of cold materials, and (ix) can be built for larger length of the piece to be heated to have higher rolling mill yield.
Disadvantages of pusher type furnaces include (i) limits the cross section of the steel stock since the contacting surface is to be square to prevent piling of steel stock in the furnace, (ii) has practically no flexibility for heating efficiently small quantity or thicknesses of steel stock, (iii) water cooled skid maintenance is difficult, (iv) water cooled skids result into colder stripes on the heated steel stock, (v) limits the thickness of steel stock to a maximum of 300 mm to 350 mm when water cooled skids are used, (vi) build-up of scale on hearth causes problems and emptying of the furnace at end of the schedule is expensive, (vii) is not desirable to push the mixed sizes of steel stock through the furnace.
Rotary hearth furnace
A rotary hearth furnace is used for heating round billets in pipe rolling mills and for heating short length blooms or billets in forging plants. The rotary hearth furnace consists of the furnace and the auxiliary equipments for charging and discharging. The furnace has a fixed furnace roof, supported on a fixed furnace wall, and a rotary circular hearth, as shown in Fig 5. A positive pressure is maintained in the furnace to prevent external cold air from entering the furnace. Furnace has internal and external water seal for maintaining pressure in the furnace.
Burners are mounted on the external and internal walls or the furnace roof. The external wall of the furnace has charging and discharging furnace doors, and charging and discharging is done with the help of charging and discharging machines. Charging and discharging proceed simultaneously. When a round billet is placed in the furnace, the bottom rotates at a certain angle. Round billets follow a radial path inside the furnace and are arranged either in a single row or in multi rows. The furnace rotary hearth is divided into preheating, heating, and soaking zones. There are no burners in the preheating zone. A flue opening is arranged on the side wall near the charging furnace door. High temperature exhaust gas flows toward the opposite direction through the rotary hearth, enter the flue and chimney outside the furnace, and exit to the atmosphere. During the flow process of high-temperature exhaust gas, the billets in the preheating zone are mainly heated by convection. The length of the preheating zone accounts for around one-fourth of the peripheral length of the rotary furnace. The length of the soaking zone is around three-twentieth of the peripheral length of the rotary hearth furnace. In addition, no round billet and burner are present between the charging and discharging furnace doors. A partition wall is placed in the middle. The distance between the charging and discharging furnace doors is around one-tenth of the peripheral length of the rotary furnace.
Fig 5 Rotary hearth reheating furnace
The steel stock in the rotary hearth furnace move forward either on horizontal or moderately sloped hearth. Thus it does not have the disadvantage of excessively sloped hearth of a continuous pusher furnace. This furnace has better means of controlling the rate of heating at all temperature levels when compared with a batch type furnace. The disadvantage of this furnace includes (i) high capital cost per unit of production, (ii) high space per unit ratio, (iii) low hearth area efficiency, and (iv) wall refractories and seals at the hearth level need high maintenance level.
Walking beam furnaces
Initially walking beam furnaces were designed with alloy steel walking beams which were exposed directly to the furnace heat and were also subjected to heat corrosion. Hence these furnaces were operated at maximum temperatures of 1065 deg C. These furnaces were not suitable for heating steels where the temperature of reheat is upto 1320 deg C.
Presently the walking beam is made of water cooled steel members lined with refractories so that only the refractories are exposed to the heat of the furnace. Alternatively, the beams and supports are constructed of water cooled pipe sections with buttons on the top surfaces to keep away the hot material from direct contact with the water cooled pipes. Walking beam furnaces are now used to reheat billets, blooms and slabs.
Walking beam furnaces have two sets of beams. The steel stock rests on the stationary or fixed beams. For moving forward, the steel stock is lifted by moving beams which move forward at a preset distance and placed the stock to the next step on the hearth. After placing the stock on the next step oon the hearth, the moving beams comes back to the original position. This is shown in Fig 6.
Fig 6 Walking beam mechanism
Walking beam furnaces are usually designed with end or side charging and discharging. The beams can be actuated either hydraulically or mechanically. Cross firing with side wall burners above and below the material stock being heated are being used. In some furnaces, the material is heated with radiant type roof burners or with burners placed in the roof and below the material.
The advantages of walking-beam furnaces are (i) the material to be heated can be separated from each other in order to avoid stickers, (ii) pile ups in the furnace and the retention time in the furnace are reduced, (iii) it is feasible to empty the furnace from either side by activating the beam mechanisms, (iv) skid marks are not there since there is no line contact with water cooled skids, (v) hearth wear and material damage is practically absent since there is no rubbing between the material and with the hearth, (vi) better hearth utilization can be obtained when charging mixed sizes by selecting the proper number of walking beams, and (vii) there is potential available for the extension of overall furnace length to improve the utilization of furnace waste gases and to reduce fuel consumption.
The disadvantages of walking beam furnaces are (i) system complexity, (ii) high capital cost, (iii) high maintenance of hearth seals and hearth refractory and (iv) the problems caused by the scale which drops off during the heating of the material.
Walking hearth furnaces
It is similar to the walking beam furnace with regards to the passage of steel stock through the heating chamber. The difference lies in the method of conveyance in these two furnaces. In the walking hearth furnace, the steel stock rests on the fixed refractory piers. These piers extend through openings in the hearth and their tops are above the hearth surface during the time when the material is stationary in the furnace. The furnace gases can thus circulate between most of the bottom surface of the work and the hearth.
For movement of the material toward the discharge end of the furnace, the hearth is raised vertically to first contact the material and then raised further for a short distance above the piers. The hearth then moves forward to a preset distance, stops, lowers the material on to its new position on the piers, continues to descend to its lowest position and then moves backward to its starting position toward the charging end of the furnace to await the next stroke. The advantages and disadvantages of a walking hearth furnace are similar to those of a walking beam furnace. The mechanism of walking hearth reheating furnace is shown in Fig 7.
Fig 7 Mechanism of walking hearth reheating furnace
Roller hearth reheating furnace
Roller hearth furnaces are used to advantage when heating very long billet, bloom or slabs in the situation where it is not practical for heating in a pusher or walking beam furnace. In the roller hearth furnace, the hearth consists of a set of water cooled driven rollers on which the steel stock moves forward. A cross section of roller hearth furnace is shown in Fig 8.
Fig 8 Typical cross section of the roller hearth furnace
The advantages of the roller hearth reheating furnaces are (i) it has ability to handle very long pieces, (ii) the zone control in this furnace is simpler when cross-firing is employed, (iii) material suffers little or no mechanical damage, (iv) skid marks are not there, and (iv) roller hearth furnace is self emptying.
The disadvantages of the roller hearth furnace include (i) high initial cost per unit of capacity, (ii) if the rollers are not properly insulated then there is increased heat loss due to the water cooling of the rollers, and (iii) roller hearth furnaces are narrower and longer than pusher type or walking beam furnaces of the same capacity.
General issues related to reheating furnaces
There are some general issues related to continuous reheating furnaces. The furnaces with single zone firing are associated with higher scale losses. Single zone fired furnaces also have higher tendency to cause decarburization of high carbon steel than the top and bottom fired furnaces because the steel is exposed to furnace gases with hydrogen and water vapour combinations for a longer duration. The scaling of steel is practiced sometimes deliberately to remove the decarburized surface layer. The furnaces with top firing have longer hearths for equal production when compared with furnaces having top and bottom firing. Side discharge furnaces have less air infiltration at the hot end than end door discharge furnaces. End door discharge of the usual gravity type induces cold air into the furnace by the chimney effect at the discharge end of the furnace. However end door discharge is mechanically simpler for removing the heated material. A level hearth eliminates the chimney effect of hearths sloping upwards towards the charging end. This chimney effect draws cold air into the furnace at the hot end and therefore causes higher fuel consumption and scale losses.