HEAT TREATMENT PROCESS AND APPARATUS

Abstract: A process for heat treating a metallic substance (12) com­ prises passing such metallic substance (12) to be heated to within a predetermined heat treatment temperature range through a controlled heating zone (20). In such zone (20), the metallic substance (12) is passed by electrically powered shortwave infrared radiation sources (28, 30) capable of pro­ ducing high intensity radiation and whose radiation intensity, which heats such metallic substance (12), can be immediately varied in accordance with input electrical energy thereto. The electrical input energy to the sources is controlled so that their cumulative heating effect brings the temperature of such metallic substance (12) to within said temperature range as such metallic substance (12) leaves said zone.

Description: Heat Treatment Process and Apparatus This invention relates to a process and an apparatus for heat treating metallic substances, such as iron based alloys, by the use of shortwave infrared radiation The common approach for heat treating metallic substances, such as iron based alloys, is to pass the substance through or place the substance in a gas-fired furnace, or other form of ambient heating furnace, or induction furnace which heats the metallic substance to the desired heat treatment temperature. For example, in heat treating steel in the form of sheet, strip, strapping, wire and the like, it is passed through a gas-fired or induction furnace for purposes of heating. The steel, as it exits from the furnace, is either cooled or quenched according to various known techniques to achieve the desired physical properties in the steel depending upon whether the steel has been heated above or below its transformation temperature or selected critical temperatures thereof. Very substantial capital investment is needed to provide a gas-fired furnace of the size which is capable of heat treating steel sheet and the like. In addition to this drawback, substantial floor area is also needed due to the relatively large size of the furnace. Another drawback with a gas-fired furnace is its inability to adjust quickly to changing temperature requirements for metal heat treatment. Substantial periods of time are needed to bring the furnace up to the desired heat treatment temperature for a particular metal and to adjust that temperature requires additional extended periods. Another difficulty with the use of gas-fired furnaces where coiled material is being treated, is that the system operates within a small range for control parameters, for example, the temperature is set for a particular line speed. Should there be a variation of any one of the parameters, such as speed varying, there is a resultant change in the temperature to which the steel is elevated. The system cannot react quickly enough to compensate or adjust for line speed change, thereby producing unacceptable heat treated product which must be rejected. A further requirement in the use of gas-fired furnaces to continously heat treat steel sheet and the like is the use of accumulators. Such a system is disclosed in Canadian patent 661,066, where accumulators are used in combination with a gas-fired furnace to manufacture strapping. The use of accumulators requires substantial floor area in the plant and also a high capital investment in setting up the operation. In instances where it is desired to relieve stresses in coiled steel sheet, strip, strapping, wire and the like by heating such steel to a temperature below its transformation temperature, the coil is heated on a bulk basis, which is commonly referred to as "box" stress relieving of coils. Aside from overcoming the internal distortion aspects in the coil, an extended period of time is needed to stress relieve the product, such as up to three days or more of heat treating. A further drawback with "box" stress relieving is the inconsistencies in the characteristics of the heat treated steel in the particular coil. Various attempts have been made to heat treat metals using infrared radiation. Heat treatment has been on a batch basis, where a portion of the metal to be treated, such as steel or aluminum, is exposed to infrared radiation to heat the metal. For example, aluminum may be preheated to a desired temperature prior to forming 90 degree bends in the aluminum by using a brake press. Other uses involve the localized stress relieving of welds on welded products using a portable infrared radiation unit. Such infrared radiation heaters may be purchased from several companies, including Barry & Sewell of Minneapolis, Minnesota. It is thus apparent that in the past, it has been fairly costly, and time consuming to establish an installation for heat treating metallic substances, such as iron based alloys, steel sheets, strips, strapping, wire and the like. The heat treatment may be carried out at temperatures below the transformation temperature or critical temperature of the steel to relieve high internal stresses therein or to heat the steel to above its critical temperature for purposes of annealing the steel to relieve all residual stresses in the steel and then by well-known quenching techniques, impart new desired physical characteristics into that steel. A process and apparatus has now been discovered using shortwave infrared heating for heat treating metallic substances to heat them in an efficient, responsive, precise manner to a desired heat treatment temperature range. It is, therefore, an object of the invention to heat treat metallic substances, such as iron based alloys, using shortwave infrared radiation. It is a feature of this invention to heat treat metallic substances by using shortwave infrared radiation heaters to obtain precise control on the consistent heating of the substances to the desired heat treatment temperature and the ability to adjust the intensity of the radiation to compensate for changes in substance temperature so as to maintain consistent temperatures for the heat treated material. It is, therefore, an advantage of this invention to provide a process which is adapted to heat treat metallic susbstances in an economical manner, where substantially lower capital costs are needed to establish equipment in which the process is carried out. It is another advantage of the invention that the established line may be started and stopped at will without causing any damage to the heat treated substance because the intensity of the infrared radiation may be .t adjusted almost instantaneously. The ability to reduce or shut off the infrared radiation emiters contributes to the economy of running the system, because of low power requirements when the line is stopped. It is another advantage of the invention that precise control can always be maintained on heat treating steel and that lighter gauges of steel sheet, strapping and the, like may be heat treated by using this process. It is a further advantage of the invention that metal objects to be treated may be conveyed through the heat treatment zone and heated to the desired temperature with precise control on the temperature of the objects as they leave the heat treating zone. Another advantage of the invention is that a form of cooling is provided for the infrared radiation emitters which prevents emitter burn-out when they are operating at high intensity settings. According to the present invention there is provided a process for heat treating a heat treatable metallic substance in a controlled heating zone characterised by the steps of exposing the metallic substance in said zone to shortwave infrared radiation from electrically powered shortwave infrared radiation sources capable of producing high intensity radiation and controlling the intensity of said radiation by controlling the electric energy input to said sources to bring the temperature of said substance to within a predetermined temperature range. In order to achieve or maintain consistent heat treatment temperatures the electrical input energy to the sources is controlled soihattheir cumulative heating effect is such to bring the temperature of such metallic substance to within said temperature range, as such metallic substance leaves said zone. In instances where the metallic substance, such as iron based alloys, are heated above their transformation temperature range, for purposes of annealing, a controlled atmosphere may be used to prevent oxidation of the steel surface. Such controlled atmosphere may be provided to at least bridge the gap between the exit portion of the heating zone and the entrance portion of a quenching bath which may be used to impart desired physical properties to the annealed steel. The shortwave infrared radiation is capable of heating the steel from its inside to its outside. Therefore, as the steel travels through the heating zone, it is only at the downstream end of the zone that the surface of the steel exceeds its transformation temperature in the annealing process. This type of heating, therefore, provides the significant advantage that a controlled atmosphere need only be provided at the downstream end of the heating zone. This is different from gas-fired annealing furnaces, where the steel surface exceeds its critical temperature first and, therefore, requires a controlled atmosphere along the length of the furnace heat treament area. In order to maintain consistent heat treatment temperatures, the temperature of the material as it leaves the zone may be sensed and thus the intensity of the radiation is varied dependent upon a sensed change in temperature. The speed at which the material travels through the zone may be sensed and such input may be used in combination with or independently of the sensed temperature signal to vary the radiation intensity, such that for a given line speed, an intensity may be set such that as the product emerges from the zone, it is at the desired temperature. The invention also provides apparatus for use in heat treating a metallic substance comprising a heat treatment furnace characterised in that the furnace is provided with a series of infrared radiation emitters having ceramic reflectors along said series and located behind said emitters, each emitter being an elongate lamp having an electrode at each end, opposing spaced-apart suitable supports secured within said furnace and provided with aligned apertures to permit said lamp ends to extend through such apertures in supporting each lamp in a series, each lamp electrode being external of a corresponding support, means defining a channel along the outside of each support and in which said lamp electrodes are disposed and means for forcing sufficient cooling air through each channel to maintain said lamp electrodes at operating temperatures. Embodiments of the invention will now be described by way of example, reference being made to the accompanying draw- ings in which: Figure 1 is a schematic of apparatus for heat treating coiled steel sheet; Figure 2 is a view showing in more detail, structural aspects of the heatingazone lower portion; Figure 3 is an enlarged view of the mounting of an end of an infrared lamp on a ceramic support; Figure 4 is an elevation of the heating zone of Figure 1 showing lamp electrode cooling; Figure 5 is a schematic showing various aspects of the electronic controller for controlling the intensity of the infrared radiation lamps; ; Figure 6 is a side elevation of a portion of the apparatus for heat treating steel strapping and painting same where the strapping has been heat treated above its transformation temperature and quenched prior to painting; Figure 7 is a detail at the upper portion of the heat treating apparatus and entrance to the heat treating zone; Figure 8 is a detail of the exit portion of the heat treating zone and entrance to the quench bath; Figure 9 is a side elevation of the lower portion of the heat treating zone and lead quench bath; Figure 10 is a section through the arrangement of Figure 9; and Figure 11 is a block diagram setting out the relationship of the components in controlling lamp intensity for heat treating the metal product. The apparatus, as shown in Figure 1, is adapted to uncoil steel sheet, pass it upwardly through the controlled heating zone optionally over chilled rollers and downwardly into a cooling bath prior to recoiling. Such arrangement is suitable for heating of steel sheet where it is desired to heat the steel to temperatures less than its transformation or critical temperatures for purposes of relieving internal stresses in the steel to increase the toughness of the steel and reduce its brittleness The apparatus for heat treating the steel sheet is generally designated 10. A pay-off reel 11 has coiled sheet 12 which is fed through a joint welding device 14. An additional pay-out reel 15 has another coil of steel sheet 12. The joint welding device 14 is used to connect the end of the sheet from pay-out reel 11 to the beginning of the sheet from pay-out reel 15, thus reducing the time needed to join the coils of material when it is desired to heat treat several similar coils. By way of the roller arrangements 16 and 18, the steel sheet 12 is passed upwardly through the heat treating zone or heating tower 20. The sheet 12 is returned downwardly to roller 22 which passes the heated sheet 12 through a cooling bath 24. The sheet 12 emerges from the cooling bath 24 and by roller 26 is passed to sheet recoiling device 27. The sheet is recoiled on coiling spool 29. The drive for the coiling spool 29 pulls the sheet through the line and thus the speed at which the recoiler 27 is driven determines the speed at which the steel sheet passes through the furnace 20. The recoiler draws the sheet through the tower and in meeting resistance from the pay-out reel 12, places the sheet under tension between rollers 16 and 36. As a result, the sheet is unsupported within the heating zone of the tower as it is spaced from the internal components of the tower. Instead of recoiling the sheet, it may at that time be passed to a slitting device to slit the sheet into desired strapping or strip sizes and optionally edge conditioned and painted before recoiling. The furnace 20 comprises opposing banks 28 and 30 of infrared radiation emitters capable of operating at high intensity. The emitters may be of the tungsten filament/quartz tube body type. These may be obtained from various manufacturers and distributors, such as Barry & Sewell of Minneapolis. The infrared radiation emitted by such lamps, when electrically powered, is shortwave. The wavelength ranges from approximately .76 microns to 5 microns. The energy distribution of such lamps reaches a peak energy at approximately 1.15 microns. The shortwave infrared radiation is transmitted directly to the strapping without heating the surrounding air. The radiation quickly penetrates the steel to heat it from the inside to its outside. Depending upon the intensity of the radiation emitted by the lamps, the steel sheet, as it passes through the furnace, may be heated by the cumulative heating effect of the furnace to any desired heat treatment temperature range which, in this embodiment, is at a range below the transformation temperature range of the steel. Factors to be considered in setting the intensity of the lamps are: 1) the speed at which the sheet passes through the tower; 2) the composition of the steel sheet; 3) the distance between the emitter banks 28 and 30 and any protection bars which may be used to keep any slack sheet when the line is shut down away from the lamps; 4) the thickness and width of the steel sheet; and 5) the desired temperature range to which the steel must be elevated, as it reaches the point of exit, to achieve the desired physical characteristics for a heat treated product It has been found that the lamps respond quickly in changing the intensity of radiation emitted by varying the electrical input to the lamps. Thus, it is possible to vary the intensity of the lamps dependent upon one or more of the sensed temperature of the heat treated product, the line speed colour of emerging product or other detectable product characteristics, which can be related to product temperature, to maintain a constant desired heat treatment temperature range for the steel sheet. Such quick response for changing lamp intensity provides superior control on heat treating steel sheet compared to gas-fired furnace heating, because of the precision in controlling the temperature to which the steel is heated to yield a product with consistent physical properties. As explained, it is necessary to use the accumulators with prior art gas-fired furnaces in order to maintain a passage of steel through the furnace to avoid damage to the heat treated steel. With the apparatus and process of this invention, in view of its very quick response time, it is possible to eliminate the need for costly accumulators, because the line can be started and stopped at will by providing a controller which quickly adjusts the intensity of the lamps. The start/stop feature of this invention is also important with respect to connecting one coil of sheet to another. Joints between the sheet may be made at will and the line restarted. When it is desired to remove the welded joint from the coil, after it has been passed through the furnace, it is possible to stop the line when the joint reaches the recoiler 27, remove the joint and subseqently start up the line again to heat treat the new coil of steel. The roller device 18 is provided with cooling lines 32 to cool the individual rollers 34 and 36. Depending upon the properties desired in the tempered steel sheet for relieving internal stresses therein, a selected amount of cooling may be provided in rollers 34 and 36. In instances where no cooling is desired, then the amount of refrigerant passing through lines 32 may be reduced to the extent to keep the rollers at a desired operating temperature to avoid damage to the rollers by overheating. The steel sheet is passed through final cooling bath 24, where roller 22 is cooled by refrigerant in line 38. Again the temperataure, at which the bath 24 is held, depends upon the properties desired in the tempered steel sheet. Water may be used in bath 24 for controlling the cooling of the steel before recoiling. The furnace 20 may be provided with various forms of forced-air devices to cool the lamp electrodes and to provide a flow of air up through the centre of the furance. As shown in Figure 1, ducts 40 and 42 supply forced-air to plenums or channels 44, 46 alongside the rear of the ceramic reflectors 48 and 50 of the emitter banks 28 and 30. The ceramic reflectors 48 and 50 may include a plurality of openings, such as shown in Figure 2, to permit air, as it passes upwardly along channels 44, 46 to pass through the openings, pass over the emitter banks 28 and 30 and upwardly through the central area 52 of the furnace. The air emerging from the furnace into the funnel portion 54 is exhausted in direction of arrows 56, by a fan schematically represented at 58. Referring to Figure 2,further details of the forced-air arrangements for the tower and the lamp supports is shown. The steel sheet 12 is fed upwardly into the furance 20 by the lower roller device 16. The relationship of the sheet 12 to the emitter banks 28 and 30 is shown. Each bank in furnace 20 is made up of a plurality of horizontally spaced-apart emitter lamps 60 which, according to this embodiment, are elongate, thin, tubular lamps having end electrodes 62. Suitable supports 64 and 66 are secured to the furnace structure They are spaced-apart and oppose one another with horizontally aligned apertures 68. The horizontally aligned apertures support lamp ends as shown in more detail in Figure 3. Support 66, with opening 68, supports the lamp 60 at its end portion 60a with the electrode 62 projecting exteriorly of the support 66. According to this embodiment, the support material may be ceramic. Behind and extending along the furnace are spaced-apart ceramic reflectors 70 and 72 According to this embodiment, the reflectors include a plurality of openings 74 which, as mentioned, permit the air, flowing upwardly in channels 44 and 46, to pass through the openings, pass over the lamps 60 and provide an upward flow of air in channel 52. The passage of air through the openings 74 provides cooling for the ceramic reflectors 70, 72. The channels 44, 46 are defined on the outside by fabricated sheet metal 76 which is secured to the furnace frame. The ducts 40 and 42 supply air to the channels 44, 46 at three different locations along the height of the furnace. Each duct 40 and 42 is connected to a common duct 78 which carries the main flow of air in the direction of arrow 80. Duct 42 is in communication with the main duct 78 by opening 82. Deflectors (not shown) are used to direct a portion of the air from the main duct into the branch duct 42 which is forced into channel 46 in the direction of arrow 84 through opening 96. A similar arrangement for the remaining branch ducts is provided. In operating the infrared radiation lamps at high outputs in order to achieve the desired heat treatment temperatures for the steel sheet 12, there was a significant problem with lamp burn-out. I discovered that this problem can be overcome by cooling the lamp electrodes as they are positioned just exterior of the support ceramic 66. According to this embodiment, outside of the ceramic support 66, is a length of formed sheet metal 88 which defines a channel. A partition 90 separates the so-formed channel into portions 92 and 94. Although not shown, the lamp electrodes 62 are electrically connected to a bus-bar to supply voltage to the lamp electrodes. The bus-bar may be located on each side of the partition 90. A supply of forced air is provided to each channel portion 92, 94 by independent fans 96 and 98 which, by flexible ducting 100, are connected to upwardly sloped entrance nozzles 102 and 104 which direct the flow of air upwardly over the lamp electrodes 62. As shown in Figure 4, there are three sets of entry ducts 102, 106 and 108 for each side of the furnace to provide cooling for each series of electrodes in the manner described with respect to Figure 2. Similarly on the other side, additional ducts 110, 112 and 114 supply a flow of air upwardly in the channel portions to cool the lamp electrodes independently of the flow of air upwardly through the middle of the furnace. The air for cooling the lamp electrodes flows upwardly in the channel portions and exhausts into the funnel-shaped portion 54 in the direction of arrows 116. This air, along with the air emerging from the centre of the tower, is exhausted by fan 58. Also as shown in Figure 4, the main duct 78 extends upwardly and supplies forced air to the branch ducts 42 which, as explained with respect to Figure 2, supply the forced air to the channels 44, 46. The electrical input energy to the sources may be controlled based on various inputs to ensure that the steel sheet, as it leaves the heat treating zone, is always heated to within the desired heat treatment temperature range. Various approaches may be used to effect such control, an example of which will be discussed in more detail with respect to Figure 5. A controller 120 is powered by terminals 122 through fuses 124. Power to the controller may be of the magnitude of approximately 570 volts with three phase 60 hertz cycle. Power may be derived from the controller 78 to operate and control the operation of the fans supplying air to various ducts in the furnace and to power the lamps, such as lamp bank 28, which in this embodiment, is in a delta load configuration. Either bank of lamps in the furnace, therefore, consists of three sets 126, which are connected in the manner shown. Another set is connected in a similar manner to provide the other bank 30 of lamps. Current sensors 128 sense the current in the lines supplying terminals 130 for lamp bank 28. A volt meter 132 is provided to display the sensed voltage in the lines leading to the terminals 130. In this particular embodiment, there are peripheral inputs to the controller 120, such as manual adjustment network 134, programmable input 136, tachometer signal through network 138 which represents the measured line speed and temperature sensor 168 input. The manual adjustment for the output of the controller 120 at terminals 130 is determined by the network 134. The double-pole/doublethrow switch 140 is shown in the manual intensity adjustment position. The setting of potentiometer 142 provides input to the controller 120 via lines 144, 146. Potentiometer 148 determines the intensity of the lamps when the line is stopped and steel sheet is located in the furnace. This setting is called the "idle" or "stand-by" setting for the lamp intensity by the controller 120. This "idle" setting for the furnace, when the line is stopped, is desired to provide energy in the lamps, so that they may be reactivated immediately to commence increasing the radiation intensity to the desired level before commencing movement of the sheet through the furnace. This "idle" setting is selected such that with the steel sheet stationary in the tower, the sheet temperature does not exceed a level which would cause harm to the sheet. Input to the controller from a tachometer is fed to the network 138 via lines 150, 152. A tachometer may be located conveniently on the line 10 to detect the linear speed at which the sheet 12 is travelling. For example, a tachometer may be located at 154 on roller 11 to detect the speed at which the sheet is travelling through the furnace 20 The tachometer generates a signal corresponding to the speed at which the sheet is travelling and this signal is fed via lines 150, 152 to the network 138. The signal may then be fed directly to the controller 120 through lines 156, 158 or to the programmable input device 136 via lines 160, 162. The controller 120 may include internally a programmable device which, when the switch 140 is in the other position, will control the intensity of the lamp 28 according to its program to provide the necesary power at terminals 130 to give the intensity needed to heat the steel sheet to the desired temperature for a particular sensed line speed. On the other hand, it is advantageous to provide a separate programmable input 136 which can have its program readily changed to accommodate heat treating of various forms of steel sheet. The programmable input 136 may be of the type which has its program recorded on a chart. Such a unit may be that sold under the trademark "Data-Trak" and obtainable from Barry & Sewell of Minneapolis. This device converts the signal input from the tachometer in terms of sensed line speed into a signal based on the chart program which causes the controller 120 for the lamp bank 28 to adjust or set lamp intensity at a level to heat the steel to the desired temperature for the particular sensed speed. Various programmed charts may be prepared to accomplish heat treatment in different types of steel sheet. Thus, the controller program can be varied easily by replacing charts to provide the desired metal properties in each different coil to be heat treated. The lamps banks, as electrically powered, are, as mentioned, very responsive to change in voltage applied. Thus, with the programmable input 136 and measuring of line speed, the controller can immediately vary the intensity applied to the lamps on detecting either an increase or decrease in line speed to adjust accordingly the intensity to always obtain the same desired degree of heating in the steel sheet on its emerging from the tower. In view of the responsiveness of this unit and the measuring of the line speed in combination with the programmable aspect of the controller, very consistent physical characteristics can be obtained over wide variations in line speed. The preciseness in the control of the intensity of the furnace also enables the heat treating of very thin steel sheet, such as sheet of a thickness of .015 inches. In the past, it was very difficult to achieve heat treating of such thin steel, because in gas-fired furnaces, the control was very poor and thus with the thinner steels, they were subject to quicker heating so that minor variations in line speed and furnace temperature resulted in substantial variations in the characteristics of the heat treated product. However, with the controller, according to this invention, the program may be changed to adjust accordingly the intensity of the lamps to achieve a consistent heat treatment of thinner sheet to give constant characteristics in the product. Restart of the line, depending upon the thickness and characteristics of the sheet, may involve preheating the sheet to a predetermined temperature so that when the sheet begins moving through the furance, it will emerge at the desired stress relieve temperature. While the sheet is stationary in the furnace, the potentiometer 142 determines the "idle" setting for the lamps. On the controller 120 receiving a start-up signal from unit 164, the controller may be pre-programmed or access the programmable input 136 to determine the needed intensity in the lamp banks 28 and 30 to raise the temperature of the sheet to a proper temperature before start-up Depending upon the makeup of the steel sheet, its thickness and the speed at which it is to be processed, the lamp banks 28, 30 as positioned in the delta load configuration, may have its upper section increased to an intensity greater than the lower sections. The sections are then balanced as the line begins to move, so that the upper portion of the sheet in the furnace emerges at the required temperature. The controller may be adapted to provide a signal at output 166 to energize the recoiler 27 to commence drawing the sheet through the furnace after the sheet has been preheated to the desired temperature. At this point, the recoiler can be accelerated to the desired line speed where the controller determines lamp intensity to achieve the desired stress relieve temperatures in the emerging steel sheet. The programmable input 136 is useful in adjusting the intensity of the lamps according to particular steel sheet to be treated. Such unit is most suitably adapted for use in heat treating steel when heated to temperatures less than its transformation temperature to relieve high internal stresses in the steel sheet to increase the steel's toughness and ductility. I have found, however, that there are other situations wherein the process of heat treating requires sensing the temperature of the steel sheet as it leaves the heat treating zone. This is most applicable with respect to heat treating where the steel sheet is to be annealed, that is heated to or above selected critical temperatures and subsquently quenched. In situations of that nature, the heat treatment must be such to heat the steel to within a desired heat treatment temperature plus or minus a few degress. In addition, I have found that, over prolonged periods of operation of this type of furnace using the shortwave infrared radiation lamps, an unexplained increase in temperature of the heat treated steel over extended periods of operation of the unit arises. Thus, it is necessary in a situation such as this to sense the temperature of the product as it is leaving the furnace to ensure that it remains within the desired temperature range. Another situation where temperature monitoring is important is where there may be slight variatons in the thickness of the steel which can result in the variation of the temperature of the sheet as it emerges from the tower, even though programmable input 136 is compensating for variation in line speed, it cannot compensate for variation in sheet thicknesses. To overcome these difficulties, as explained, the temperature of the product may be measured as it leaves the tower. With respect to tempering of the coiled steel, reference is made to Figure 1 where a temperature sensing device is located at 168 to measure the temperature of the sheet as it emerges from the tower. Ideally the temperature sensor is a form of optical pyrometer which measures the amount of infrared radiation emitted by the product as it leaves the tower and from this information, the pyrometer with associated amplifier and processing circuitry is capable of generating an output signal representative of the product temperature. Such units are readily available on the market and one which has been found to be particularly useful is that sold by Williamson Corporation of Concord, Massachussets, sold under the trademark "System 4000". The signal from the temperature sensor 168 is input to the controller via lines 170. The controller may be adapted to either control intensity of the lamps based on input from the temperature system sensor, or from the programmable input based on line speed. It may also be adapted to permit input from the temperature sensor when it senses a change outside the desired range to override the input from the programmable unit to effect change in intensity to bring the emerging product back within the desired temperature range. The controller provides better control on temperture of emerging product when determining lamp intensity based on input from line speed. However, in other situations such as line startup where it is desired that the sheet obtain a desired temperature before emerging from the tower, the temperature sensor at the end of the tower is most helpful in this regard to establish when the recoiler should be activated via signal designated 166 in Figure 5. The embodiments of the invention, as desribed with respect to the apparatus of Figure 1, are particularly useful in the heat treatment of steel sheet where such steel is heated to temperatures less than its transformation temperature range t6 relieve internal stresses. In situations where it is desired to heat treat steel and a particular steel sheet, strip, strap, tubing, wire and the like, where such steel is heated to or above its transformation or selected critical temperature, a preferred apparatus including a controlled atmosphere and quench bath to impart certain physical characteristics in the annealed steel is shown in Figure 6. The apparatus is arranged to heat treat several spaced-apart juxtaposed steel straps. The strapping is formed by slitting uncoiled sheets with well known slitters and passing the so formed strapping 200 beneath rollers 202 and upwardly to roller 204. Additional rollers 206 and 208 define the path of travel for the strapping 200 downwardly through the heat treatment zone 210. The rollers 204 and 206 are supported from the roof structure 212. The strapping 200, as it passes downwardly through heating zone 210, is heated by use of the shortwave infrared radiation lamps of the type discussed with respect to Figure 1 to heat such strapping 200 at the lower portion 212 of the tower to the desired heat treatment temperature range which, as explained in this embodiment, is above the transformation temperature. A controlled atmosphere is provided generally in the area 214 to prevent oxidation of the strapping as it emerges from the tower 210 and passes into a lead quench bath 216, which is controlled at a particular temperature to impart into the annealed strapping the desired physical characteristics. The gases, as combusted and used in heating the lead bath 216, are vented through the chimney 217. In addition to roller 208, rollers 218 and 220 define the path of travel of the strapping 200 through the quench bath 216 and exiting therefrom over roller 222 into a cooler 224. The cooler 224 cools the annealed quenched heat treated strap to a sufficiently low temperature to permit application of paint thereto by roll coat painter 226. The cooler 224 receives its refrigerant from lines 232 from a chiller 234 located on the roof of the housing structure. The paint is dried on the strapping in paint dryer 228 which exhausts the volatile substance through exhaust stack 230. The paint dryer 228 may also be a unit which employs shortwave infrared radiation lamps to dry the paint on the strapping. Such a unit is described in Applicant's co-pending Canadian application Serial Number 318,901 and United States application Serial Number 000,559 The intensity of the lamps are controlled in a manner so as to provide sufficient heating within the strap to heat it to a temperature which dries or bakes the paint thereon. The control of the intensity may be based on the speed at which the line is travelling so as to provide the proper intensity of shortwave infrared radiation to effect the desired drying of the strapping. The strapping 200, as it emerges from the paint dryer 228, is recoiled in the usual manner, such as using recoilers as shown in Figure 1, where the individual straps would be individually coiled. The arrrangement for the infrared lamps in the heat treating zone 210 may be similar to that shown in Figures 1, 2 and 4 of the drawings. There is a flow of air upwardly through the centre of the tower 210, which is created by air passing up the outsides of the ceramic reflectors and through apertures therein, over the lamps and into the central zone of the tower. The flow of air is provided by outer ducts 236 where air is forced into such ducts by fans 238 and 240, the air being exhausted at the top of the tower and withdrawn by fan 242 through exhausting duct 244. Since the unit is operated at high intensities, cooling for the lamps ends may be provided, as discussed with respect to Figures 2 and 4 where as shown in Figure 6, a channel 246 as provided on each side of the tower and housing the lamps ends, has cooling air forced there through on each side by fan 248. The air as it exits the upper portions of the channels 246 enters into the exhaust duct 240 and is exhausted by fan 242. The lamps in the tower 210 are serially arranged in a spaced-apart parallel manner similar to that shown in Figure 1. The strapping 200 is placed under tension and passed downwardly through the tower 210, so as to be unsupported within the tower and thus spacedfrom the opposing banks of infrared heater lamps. Referring to Figure 7, the upper portion of the tower is shown in more detail, wherein roller 204 has a plurality of straps 200 passing thereover, through a retraction device 248 and over other roller 206 and downwardly through the slit opening 250 into the upper portion of tower housing 252. The slit 250 is, as shown, of a size to minimize air escaping from the tower through the entrance to within the building. Instead the air is exhausted through duct 244. The purpose of the retraction device 248 will be discussed in more detail after reference to other components of the heat treating line. Referring to Figure 8, the lower portion 254 of the tower 210 is shown, where the strap emerges from slit opening 256 in tower base. The strap passes over roller 208 and beneath roller 218 into the lead quench bath 216, the molten lead being generally designated at 215. As is appreciated by those skilled in the art, in the heat treatment of steel where it is heated above its transformation temperature and heavy oxidation of steel surface is to be avoided, it is necessary to provide a controlled atmosphere to minimize or eliminate the oxidation of the strapping as it passes from a furnace to a lead quench bath. The controlled atmosphere of this arrangement is provided by an enclosure 258 which supports roller 208. The enclosure extends from the base 254 of the tower 210, downwardly to its lower portion 260, as shown in dot, which is beneath the level of the molten lead 250. Within this enclosure, nitrogen (a non-oxidizing atmosphere) is forced in through inlets 261 and 262 in the direction of the arrow shown to purge the enclosure and thus provide basically a nitrogen atmosphere, where the nitrogen moves upwardly through slit 256 to within the tower and is eventually exhausted through exhaust duct 244. Thus, as the strapping emerges from slit 256 of the lower portion of the tower at the desired annealing temperature, the strapping moves into the controlled atmosphere to thereby minimize or eliminate oxidizing of the steel surface prior to its being quenched in bath 216. The shortwave infrared radiation emitted by the lamps is capable of heating the metal from the inside to its outside. With proper selection of lamp intensity based upon the speed at which the strap travels through the unit and in combination with the use of the temperature sensor, it is possible to heat the strap to the desired heat treat temperature. This novel approach to heat treating minimizes the distance through which the strap travels while its surface is above its transformation or selected critical temperature. With this type of heating zone, if needed a controlled atmosphere may be provided in the lower portion of the tower. With reference to Figure 9, the lead pot 216 has the heat treated strap 200 moving into it past rollers 208 and 218. The enclosure 258 is pressurized with nitrogen to ensure that the strap, as it leaves the zone, is in a non-oxidizing atmosphere. Should it be necessary to also enclose the strap 200 in the lower portion of the tower where the strap surface has now exceeded its critical temperature in a controlled atmosphere, it is possible to arrange a quartz tube 264 with a small entrance slit 266 and secured to an asbestos curtain 268 at 270. The nitrogen in enclosure 258 is forced upwardly through the opening 272 in the asbestos curtain upwardly through the quartz tube 264 and exiting at entrance 266. The quartz tube is transparent to the infrared radiation emitted by the lamps 274, thus the heating of the strap 200 is continued within the quartz tube enclosure 264 to ensure that the strapping is heated to the desired temperature while maintaining the strap above its critical temperature within a controlled atmosphere. The nitrogen, as it exits entrance 266 is exhausted through the exhaust duct 244. As shown in Figure 10, the section shows more clearly the enclosure 258 as its free end 259 is immersed in the molten lead 215 of the bath 216. The quartz tube 264, is as explained, secured to the asbestos muffle 268 to continue the controlled atmosphere upwardly within the tower. Such quartz tube arrangement permits circulation of normal air over the lamps and cooling the lamp ends and does not in any way interfere with the operation of the lamps and thus, conveniently provides a controlled atmosphere when desired in the downstream portion of the heating zone. It should be appreciated that, in some instances where the strap linear speed is quite high, the strap surface as it is above its critical temperature, may only be exposed to oxygen in the tower for less than a second before entering the controlled atmosphere enclosure 258. This very brief exposure of the strap to oxygen in the tower may not cause a significant, harmful scale buildup. As a result, it is not always necessary to provide a controlled environment in the tower. When the line is stopped and the lamps are either shut off or at idle setting, the portion of the strapping, which extends from the lead bath at 276 to at least its exit from the heating tower at opening 272, is permitted to cool down. This portion of the strapping has not been passed through the molten bath, so that on startup of the line, this section of the strapping between points 272 and 276, if passed through the bath unheated, would not provide the desired properties in the steel, since it would not have been quenched from its upper heat treat temperature. To overcome this problem, the length of strap is retracted in the direction of arrow 278 to place at least the portion of the strap from point 276 upwards to within the heat treating tower. This retraction of the strapping is accomplished with the unit 248. The unit 248 consists of a supporting structure 280 to which a pneumatic cylinder 282 is connected. The cylinder rod 284 is connected to a roller arrangement 286 beneath which strapping 200 travels. To retract the strapping, the pneumatic cylinder 282 is actuated to withdraw the cylinder rod 284 in the direction of arrow 288 and thus pull the strapping 200 downwardly towards the dotted region 290 between rollers 204 and 206. The slitting mechanism or a brake located on pay-out reel is used to prevent the strapping from moving over roller 204. Thus, as the pneumatic cylinder pulls downardly, the strapping is withdrawn from the molten bath and over roller 206 down to the region as shown in dot at 290. The stroke of the pneumatic cylinder 282 is selected to retract into the tower at least the section of strapping between tower exit and bath which has cooled down. Therefore, on startup of the line, the strapping is heated by the lamps 274 to its heat treatment temperature. Upon the strap achieving the heat treatment temperature, the line is restarted by actuating the recoiling devices to commence moving the strap out of the tower and, since it is at its heat treatment temperature, may now be passed into the lead bath and properly quenched to derive the desired tensile properties in the strapping. As to the length of strapping which has remained in the molten bath 216 during the shutdown time, as is appreciated, such continued soaking times will not significantly detract from, if anything, may improve its physical characteristics so that portion of the strapping need not be retracted. In order to measure the temperature of the strapping as it emerges from the heat treating zone through the exit porton 272, optical pyrometer 292,as shown in Figure 10, is located proximate a window 294 provided in the enclosure 258. The optical pyrometer 292 is aimed on the strapping at the point where it emerges or exits from the tower at 272 to measure the surface temperature of the strapping. The optical pyrometer works on the basis of measuring the infrared energy emitted by the strapping surface. As can be appreciated by those skilled in the art, the infrared wavelengths emitted vary depending upon the temperature of the strapping. By measuring the amount of radiant energy emitted by the strapping at selected wavelengths, the surface temperature of the material may be determined through an optical-electronic conversion process. Thus, the optical pyrometer 292 generates a signal which is transmitted through line 294 to the control equipment, the signal being indicative of the temperature of the strapping. As a modification to the embodiment shown in Figure 5 for controlling the heating of the strapping, a control arrangement, as shown in block form, is illustrated in Figure 11. The heat treating zone controller 296 and paint drying zone controller 298 are similar to the controller discussed with respect to Figure 5. However, a micro-processor 300 is used to interpret the signals, which have been converted to digital form, from the optical pyrometer 292 via line 294 and the line speed signal from tachometer 302 transmitted through line 304 to pins 306 and 308. The micro-processor in accordance with its program analyzes such inputs to control through lines 310, heat treating zone controller 296 and line 312 paint drying zone controller 298. Additional control is also provided on the start/stop of the strap recoiling machine 314 via line 316 and on the paint coating device 318 via line 320. For purposes of quality control the sensed temperature of the material as it leaves the heat treating zone may be recorded on recorder 322 which receives its signal through line 295. Thus, should subsequent faults in the material show up by testing, the temperature at which the material was heat treated can be checked from past records. The micro-processor is loaded with a program, which dependent upon the conditions, can cause the heat treating zone controller and paint drying zone controller to set the proper intensities for the respective lamp banks 324 and 326 connected to the controllers via lines 328 and 330. In considering the sequence of events in starting the line, running the line at a desired line speed and slowing it down, the components interact in the following manner. On startup, the micro-processor,upon receiving a start signal, causes the controller 296 to increase the input electrical energy to the lamp banks 324 to preheat the strap in the tower to within the desired heat treatment temperature range. When the optical pyrometer, as positioned close to the exit of the tower, senses that the strapping is at that temperature, the signal from the optical pyrometer, by way of the micro-processor program, actuates the strap recoiling machine 314 by transmitting a start signal via line 316. As the line speed is increasing all the while the optical pyrometer measuring the temperature to detect any changes, the tachometer is transmitting a signal which is in relationship to the line speed. The micro-processor may rely on either or both of the signals, which by its program, will transmit to the heat treating zone controller a signal through line 310 which is representative of either causing an increase, decrease or holding of the intensity of the lamp banks. This signal is dependent upon the sensed temperature of the strapping as it emerges from the zone and the sensed line speed to ensure that the strapping is always elevated to the desired heat treating temperature range. As to the paint drying zone controller, the micro-processor increases the intensity of the lamp banks 326 through the controller 298 by way of transmitting the appropriate signal in line 312. With the paint line, the strapping which was previously painted and resting in the tower is usually dry. Thus, by way of the micro-processor program, the intensity of the lamps is increased to a level dependent upon line speed to ensure that all painted strap emerging from the drying zone is dry or properly baked. In order to achieve a constant coat or paint thickness on the strapping as applied by the paint coating device 318, a signal may be transmitted through line 320 to the device. This signal varies the rate of application of paint dependent upon the sensed line speed to ensure a consistent application of paint thickness over varying line speeds. On slow down of the line, the paint drying zone controller decreases the intensity of the lamp banks dependent upon the magnitude of the signal at line 312. Correspondingly, the micro-processor in sensing a decrease in line speed through the tachometer and a corresponding increase in temperature by way of the optical pyrometer, makes an adjustment to the intensity of lamp bank 324 by transmitting a signal through line 310 to controller 296. This ensures that, while the line slowing down, all strapping which emerges from the heat treating zone is within the desired heat treatment temperature range. The micro-processor may be programmed upon receiving a signal that the line is stopped and prior to restarting of the line to retract the strap by retracting device 284 to ensure that that portion of the strapping which has not yet entered the bath and has not been properly quenched is withdrawn back into the tower for reheating and subsequent heat treatment and quenching. It is appreciated that the heat treating zone controller and the paint drying zone controller may also be provided with the manual adjustment hookups, as demonstrated in Figure 5. In addition by way of remote control and appropriate contact switches, the unit may be switched from automatic to manual control and vice versa in the running of the heat treating and painting line. The lamp banks 324 and 326 may be in the delta load configuration, as is demonstrated in Figure 5, where the capability may be provided that the controller control the intensity of the sets of lamps in each bank individually of each other. A further refinement is that, with the system shown in Figure 6, two sections may be provided where the upper section has three sets of lamps and so does the lower section with a bank on each side. The heat treating zone controller may therefore be constructed to control the sets independent of each other. This may be of assistance on startup in the heat treating, where some materials may require a different preheat treatment before emerging from the tower, thus permitting heating of the material which is about to emerge from the tower to a far greater temperature than that which is at the entrance portion to the tower. Thus on linefistartup, the portion at the entrance by the time it has travelled through the heat treating zone will be at the proper temperature without overheating the remaining portion of the material in the zone on the startup. It is understood that various forms of steel may be heat treated with this apparatus, as previously mentioned, such as sheet, strip, strapping, wire, tubing and the like. In the instance of treating strapping and wire, the rollers may be provided with grooves or the like to prevent strapping or wire overlapping during its travel through the tower and subsequent cooling devices. Protection bars may be included in the tower to prevent any slack strapping from contacting the lamps when the line is shut down. In the paint drying device 228, protection bars are provided to prevent strapping contacting the lamps when the line is shut down, where the strapping in the horizontal position would tend to rest on such bars. In locating the protection bars, they are spaced from the lamps where no lamps are located directly behind the protecting bars. This prevents overheating of the bars and thus eliminates any effect residual heat in the bars may have on the strapping particularly in paint drying to avoid burning or damaging of the dried painted strap. Thus, the use of electrically powered shortwave infrared radiation emitter banks with their quick response is a substantial advance over prior art processes for heat treating. This apparatus considerably reduces the capital investment needed to provide a heat treatment line while achieving unexpectedly substantial increases in the preciseness with which the steel may be heat treated to thereby increase the quality of the heat treated product. In addition the apparatus involving the use of compact infrared emitters requires considerably less floor area to set up the line and, since the tower can be oriented vertically, further reduces the need for floor space. The unit provides the option of doing away with accumulators, thereby reducing further the capital investment in establishing a heat treating line. However, it is understood that in instances where an established line has accumulators this form of heat treatment furnace may be incorporated with such lines to work in combination with the accumulators to maintain essentially continued operation until there is a breakdown in the line at which time the start/stop feature of the line is important to accommodate such requirements. A further consideration is that, in the heat treatment of steel in heating it above its critical temperature a controlled atmosphere is easily provided with this system, as demonstrated with respect to the embodiment of Figure 6. Thus, there is no need to use costly equipment needed in large gas-fired furnaces which use large volumes of nitrogen in providing the controlled atmosphere. Depending upon the intensities which can be achieved within the furnace various line speeds may be used to heat treat the steel sheet, strapping and the like. With a sufficiently large furnace, speeds of up to approximately 150 centimeters per second or more may be achieved in heat treating the sheet and at the same time provide consistency in the characteristics of the heat treated product. As explained, several factors determine parameters of the process. As an example in the instance of relieving stresses within coil sheet where it is heated to a temperature below its transformation range, a sheet having a chemistry of .25% to .28% carbon and 1% to 1.35% manganese may be heated to a temperture of 565 degrees C. at speeds in the range of 127 centimeters per second. Such sheet, having a thickness in the range of .088 centimeters and having a break strength of approximately 2950 kilograms, after heat treating has a break strength in the range of 2810 kilograms to 2900 kilograms with an elongation in the range of 7% to 8%. As to the parameters of the process for annealing a steel sheet having a chemistry of .36 to .42% carbon and .90 to 1.158 manganese, using the apparatus of Figure 6 it may be heated to a temperture of 825 degrees C. at speeds in the range of 75 centimeters per second. The thickeness of the sheet may be in the area of .078 centimeters where it is quenched in the lead bath for two to three seconds at 415 degrees C and held at that temperature for an additional six to eight seconds to give a high tensile strapping having a break strength in the range of 2450 kilograms and elongation of 7 to 8%. The above examples demonstrate exemplary parameters for the process, but are in no way to be interpreted as limiting the scope of the claims for this invention.

Claims: Claims: 1. A process for heat treating a heat treatable metallic substance in a controlled heating zone characterised by the steps of exposing the metallic substance in said zone to shortwave infrared radiation from electrically powered shortwave infrared radiation sources capable of producing high intensity radiation and controlling the intensity of said radiation by controlling the electric energy input to said sources to bring the temperature of said substance to within a predetermined temperature range. 2. A process according to Claim 1 in which the metallic substance is advanced through said zone characterised by the steps of sensing the temperature of the substance leaving the zone and modifying at least one of the speed of advance of the substance through the zone and the electrical energy input to said sources as a function of the sensed temperature to maintain the temperature of the metallic substance leaving the zone within said temperature range. 3. A process according to Claim 1 in which the metallic substance is advanced through said zone characterised by the steps of sensing the speed of advance of the metallic substance through said zone and modifying at least one of such speed of advance and the electrical energy input to said sources as a function of the sensed speed of advance to maintain the temperature of the metallic substance leaving the zone within said temperature range. 4 A process according to Claim 1 in which the metallic substance is advanced through said zone characterised by the steps of sensing both the speed of advance of the metallic substance through said zone and the temperature of the metallic substance leaving said zone and modifying at least one of such speed of advance and the electrical energy input to said sources as a function of said sensed speed and temperature to maintain the temperature of the metallic substance leaving the zone within said temperature range. 5. A process according to any one of the preceding claims in which the metallic substance is advanced through said zone characterised in that the process is initiated by elevating the electrical energy input to said sources to a level sufficient to heat the substance to a temperature within said temperature before it leaves said zone. 6. A process according to Claim 5 characterised in that the electrical energy input is controlled while the speed of advance of the metallic substance through said zone is increased to a desired speed to maintain the temperature of the metallic substance leaving said zone within said temperature range. 7. A process according to any one of the preceding claims in which the metallic substance is in the form of steel sheet, strip, strap, tubing or wire characterised by the step of advancing said steel under tension substantially vertically through and unsupported within said zone. 8. A process according to Claim 7 characterised in that the steel is initially in coiled form and is uncoiled for advance through said zone. 9. A process according to Claim 7 or 8 characterised in that the steel is heated to a temperature within said temperature range above its critical temperature and is advanced from said zone to a quenching bath through a controlled atmosphere. 10. A process according to Claim 9 characterised in that the steel is advanced through a chamber extending from said zone to said bath and a non-oxidising gas is supplied to said chamber to provide said controlled atmosphere for avoiding oxidation of the steel while above its critical temperature before entry into said bath. 11. A process according to Claim 9 or 10 characterised in that the electrically powered radiation sources emit a shortwave infrared radiation which heats the steel from the inside to the outside. 12. A process according to Claim 9, 10 or,11 characterised by, in the event of an interruption in the advance of steel from said zone to said bath, the step of reversing the direction of advance of the steel to retrace into said zone at least that portion of steel about to enter the quenching bath for reheating and advancing the steel from the zone to the quenching bath when the steel leaving said zone is reheated to said temperature. 13. A process according to Claim 12 characterised by the steps of elevating the electrical input energy to said sources to heat the steel to a temperature within said temperature range before re-advancing the steel from said zone to said quenching bath and controlling the intensity of radiation while the speed of advance of the steel is increased to a desired value. 14. A process according to Claim 7 or 8 characterised in that the steel is heated to a temperature within said temperature range which is below its critical temperature to relieve to a predetermined extent internal stresses in the steel. 15. A process according to any one of Claims 7 to 14 characterised in that after heat treatment the steel is cooled and painted and the freshly painted steel is then dried and coiled. 16. A process according to any one of Claims 7 to 15 characterised in that the steel is advanced through said heating zone between opposing, spaced, parallel banks of electrically powered shortwave infrared radiation lamps. 17. A process according to Claim 16 characterised in that the banks of lamps are vertically oriented to provide a tower through which the steel is advanced under tension. 18. A process according to Claim 16 or 17 characterised in that said lamps emit radiation at wavelengths of approximately 0.76 to 5 microns with peak energy at a wavelength of approximately 1.15 microns. 19. A process according to any one of the preceding claims characterised in that the metallic substance is initially coiled steel which is slitted into a plurality of steel strips which are advanced through said zone. 20. Apparatus for use in heat treating a metallic substance comprising a heat treatment furnace characterised in that the furnace is provided with a series of infrared radiation emitters having ceramic reflectors along said series and located behind said emitters, each emitter being an elongate lamp having an electrode at each end, opposing spaced-apart suitable supports secured within said furnace and provided with aligned apertures to permit said lamp ends to extend through such apertures in supporting each lamp in a series, each lamp electrode being external of a corresponding support, means defining a channel along the outside of each support and in which said lamp electrodes are disposed and means for forcing sufficient cooling air through each channel to maintain said lamp electrodes at operating temperatures. 21. Apparatus according to Claim 20 characterised in that said lamp supports are ceramic. 22. Apparatus according to Claim 20 or 21 characterised in that said furnace is oriented vertically. 23. Apparatus according to Claim 20, 21 or 22 characterised in that each lamp is a tungsten filament with quartz body which, when powered, emits radiation at wavelengths approximately 0.76 to 5 microns with peak energy at a wavelength of approximately 1.15 microns. 24. Apparatus according to any one of Claims 20 to 23 characterised in that two series of lamps are arranged as opposing spaced-apart parallel banks of lamps. 25. Apparatus according to any one of Claims 20 to 24 for heat treating coiled steel sheet characterised by combination with means for uncoiling such steel, a roller arrangement for passing such uncoiled steel through said furnace, means for cooling such steel as it emerges from said furnace and means for recoiling such cooled heat treated steel. 26. Apparatus according to any one of claims 20 to 25 characterised in that a controller is provided to control the intensity of said lamps to consistently heat such sheet to the desired heat treatment temperature range. 27. Apparatus according to any one of Claims 20 to 24 characterised by means for advancing said metallic substance through said furnace, means for sensing the temperature of the substance leaving the furnace and means responsive to said sensed temperature to control at least one of the speed of advance of the substance through the furnace and the intensity of radiation of said emitters to maintain the temperature of the substance leaving the furnace within a predetermined temperature range. 28. Apparatus according to any one of Claims 20 to 24 characterised by means for advancing said metallic substance through said furnace, means for sensing the speed of advance of said substance and means responsive to said sensed speed to control at least one of the speed of advance of the substance through the furnace and the intensity of radiation of said emitters to maintain the temperature of the substance leaving the furnace within a predetermined temperature range.

Inventors: HEATH, JAMES EARL
Applicants: SAMUEL STRAPPING SYSTEMS LTD.
Application year: 1980
Main classification: C21D9
IPC codes: C21D9, H05B3, C21D1, C21D11