EP0075438B1 - Wärmebehandlung von Metallen - Google Patents

Wärmebehandlung von Metallen Download PDF

Info

Publication number
EP0075438B1
EP0075438B1 EP19820304867 EP82304867A EP0075438B1 EP 0075438 B1 EP0075438 B1 EP 0075438B1 EP 19820304867 EP19820304867 EP 19820304867 EP 82304867 A EP82304867 A EP 82304867A EP 0075438 B1 EP0075438 B1 EP 0075438B1
Authority
EP
European Patent Office
Prior art keywords
furnace
thermal treatment
gas
region
treatment region
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
EP19820304867
Other languages
English (en)
French (fr)
Other versions
EP0075438A1 (de
Inventor
Robert Gwynn Bowes
Robert David Chapman
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BOC Ltd Great Britain
Original Assignee
BOC Ltd Great Britain
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=26280755&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP0075438(B1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by BOC Ltd Great Britain filed Critical BOC Ltd Great Britain
Publication of EP0075438A1 publication Critical patent/EP0075438A1/de
Application granted granted Critical
Publication of EP0075438B1 publication Critical patent/EP0075438B1/de
Expired legal-status Critical Current

Links

Images

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D99/00—Subject matter not provided for in other groups of this subclass
    • F27D99/0073—Seals
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/74—Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D9/00—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
    • C21D9/52—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
    • C21D9/54—Furnaces for treating strips or wire
    • C21D9/56—Continuous furnaces for strip or wire
    • C21D9/561—Continuous furnaces for strip or wire with a controlled atmosphere or vacuum
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/14—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment
    • F27B9/20—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path tunnel furnace
    • F27B9/24—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path tunnel furnace being carried by a conveyor
    • F27B9/243—Endless-strand conveyor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D1/00—Casings; Linings; Walls; Roofs
    • F27D1/18—Door frames; Doors, lids, removable covers
    • F27D1/1858—Doors
    • F27D2001/1875—Hanging doors and walls
    • F27D2001/1883—Hanging curtains

Definitions

  • This invention relates to the heat treatment of metals.
  • heat treatment processes such as annealing, spheroidising, sintering, brazing, malleabilising and hardening
  • the heat treatment may be performed on a batch or continuous basis.
  • Continuous heat treatment furnaces are typically open-ended. They have an inlet for the metal or work to be heat treated, a thermal treatment region, a cooling region, and an outlet for the work.
  • the work is advanced through the furnace at a chosen rate so that it is moved through the thermal treatment zone where it is raised to the necessary treatment temperature and is then passed through the cooling region, in which the work is cooled to a temperature at which it will not become oxidized on exposure to ambiant air.
  • the required atmosphere is typically generated in, for example, an exothermic or endothermic gas generator or an ammonia cracker.
  • the atmosphere is supplied to the thermal treatment region and expands to fill the whole gas space in the furnace. Since the atmosphere is particularly flammable, it is generally necessary to burn the atmosphere both the furnace entrance, and furnace outlet. There is thus a bidirectional flow regimen in the furnace with gas diverging in both directions from the thermal treatment zone.
  • US-A-3 407 366, US-A-3 950 192, DE-A-861 569 and FR-A-55 831 relate to processes of operating continuous heat treatment furnaces in which baffles are employed at one or both ends of the furnace and in which the furnace has different zones, typically with different atmospheres in the respective zones. None of these documents, however, teaches minimising the gas consumption of the furnace.
  • a method of operating a continuous horizontal heat treatment furnace having, in sequence, an entrance, a thermal treatment region, a cooling region and an exit, work to be heat treated being passed through the furnace from the entrance to the exit, and the furnace being of a kind that is adapted to be operated conventionally by supplying reducing gas and non-reactive gas selected from nitrogen and argon to its thermal treatment region with there being substantial flows of gas out of the thermal treatment region both in the direction of the entrance and in the direction of the exit, and with all the gas that passes out of the furnace leaving from the exit and entrance regions of the furnace, wherein means are provided for restricting the ingress of air into the furnace through its entrance and exit, reducing gas is introduced into the furnace, and non-reactive gas selected from nitrogen and argon is introduced into the furnace at a plurality of locations chosen so as to create a flow regimen in which atmospheres of different compositions from one another subsist in the thermal treatment and cooling regions of the furnace, providing at least one curtain or partition in the cooling region at
  • non-reactive gas is meant a gas which is non-reactive towards other constituents of the atmosphere and the work or metal being heat treated.
  • nitrogen is used as the non-reactive gas, though, in certain instances, it may be desirable to use argon as an alternative if nitrogen has any deleterious effect on the metal being heat treated.
  • 'heat treating metal' as used herein includes annealing (including spheroidising), sintering (e.g. of powders including non-metallic powders) brazing, hardening and malleabilising.
  • annealing including spheroidising
  • sintering e.g. of powders including non-metallic powders
  • the method according to the invention is particularly suited for use in annealing and sintering.
  • horizontal continuous furnaces which may be operated in accordance with the invention include continuous strip wire furnaces, mesh belt furnaces, roller hearth furnaces and pusher furnaces.
  • non-reactive gas and reducing gas are introduced directly into the thermal treatment region of a horizontal furnace.
  • they can be introduced into the furnace at a location in the cooling region, for example, at one or more locations near to the thermal treatment region, but alternatively or additionally at one or more locations remote from the thermal treatment region, the flow being such that a substantial portion of the reducing gas flows into the thermal treatment region.
  • the non-reactive gas and the reducing gas are typically introduced into the furnace at about ambient temperature, while the thermal treatment region may be at temperature of up to 1100 degrees C depending on the kind of heat treatment to be performed, there is a substantial expansion of the gases in the thermal treatment region.
  • non-reactive gas is supplied to the cooling region at one or more locations, typically with a component of velocity horizontally in the direction of the thermal treatment region, so as further to impede the flow of gases out of the thermal treatment region through the cooling region.
  • any flue or the like at or near the exit is desirably sealed to prevent air from flowing into the furnace therethrough.
  • non-reactive gas may also perform the above-mentioned function of reducing the proportion of reactive gas in the atmosphere leaving the exit of the furnace.
  • flow restriction means are provided there so as to impede the flow of gas into the furnace without preventing the metal being treated from passing out of the furnace.
  • said means providing a physical obstruction to the flow of gas out of the cooling region are also used to help impede in leakage of gas into the furnace through the exit.
  • a suitable flow restriction means comprises one or more curtains comprising a multitude of generally vertically depending fibres or filaments which when not displaced obturate substantially the whole cross-sectional area of the furnace at or near the outlet but whose lower ends can be displaced laterally by metal being passed through the furnace to allow the metal to pass through the or each curtain.
  • a combination of such flow restriction means and means for introducing non-restrictive gas into the furnace at or near to the flow restrictions means is generally particularly effective in substantially preventing ingress of air into the furnace through the outlet.
  • a part of the cooling region near to the furnace exit has spaced-apart partitions and/or curtains or the like defining at least one chamber into which nitrogen or other non-reactive gas is introduced, the partitions being arranged to permit metal being treated to pass through the chamber or chambers.
  • Such a technique may be employed generally in heat treatment furnaces to help reduce the total consumption of gas.
  • sintering it is known to employ a pre-heat region intermediate the sintering (or thermal treatment region) and the furnace entrance.
  • a limited flow of air into the oxidised in the pre-heat region may be tolerated to help create the necessary oxidising conditions.
  • the invention also provides a method of operating a continuous heat treatment furnace having, in sequence, an entrance, a thermal treatment region, a cooling region and an exit, work to be treated being passed through the furnace from the entrance to the exit, and the furnace being of a kind that is adapted operated conventionally by supplying non-reactive gas selected from nitrogen and argon and reducing gas to its thermal treatment region both in the direction of the entrance and in the direction of the exit, and with all the gas that passes out of the furnace leaving from the exit and entrance regions of the furnace, non-reactive gas selected from nitrogen and argon is supplied to the chamber or chambers so as to restrict ingress of air from outside the furnace through the chamber or chambers into a part of the furnace intermediate the chambers and the thermal treatment region, non-reactive gas, selected from nitrogen and argon, and reducing gas also being supplied to the furnace at chosen locations to create an atmosphere for the heat treatment, providing a plurality of curtains and/or partitions in the cooling region to define one or more chambers, and supplying non-reactive gas
  • the non-reactive gas is preferably introduced directly into the chamber or chambers.
  • non-reactive gas is preferably at such a rate and the physical obstruction that the partitions present to the flow of gas is preferably such that:
  • a horizontal furnace there are at least two chambers and where:
  • the chamber or chambers are in the cooling region near the exit end of the furnace and with the pressure in the chamber or chambers greater than atmospheric pressure the tendency for air to flow or seep into the cooling region of the furnace through the furnace exit is reduced.
  • the pressure in the chamber or chambers greater than the pressure in the rest of the cooling region and the pressure in the thermal treatment region the creation of the desired flow regimen in the furnace, with a non-flammable gas mixture leaving the furnace exit, is facilitated while enabling the total requirements for non-reactive and reducing gas to be reduced.
  • these chambers will typically intercommunicate with and be at substantially the same pressure as one another.
  • the cooling region there are at least two, and typically three or more chambers, each supplied directly with non-reactive gas.
  • a relatively high hydrogen (or other reactive gas) concentration e.g. 50% by volume or more
  • the concentration of hydrogen in the outermost chamber being such that the atmosphere therein is non-flammable.
  • Having a high hydrogen concentration in most of the cooling region assists in cooling the metal owing to the relatively high specific heat of hydrogen.
  • Such a high hydrogen concentration may be desirable if the furnace is required to treat a particularly large mass of metal per unit time, but on other occasions may be unnecessary, and, instead, it may be desirable to confine the highest hydrogen concentrations to the thermal treatment region by introducing most of the hydrogen into the thermal treatment region directly, or into a part of the cooling region near to the thermal treatment region.
  • each partition may take the form of a flap adapted to make a substantially fluid-tight seal or engagement with the metal being treated and the sides of the furnace.
  • each partition may comprise a row of members of 'fingers' pivotally mounted or hinged at the top of the furnace, with adjacent 'fingers' overlapping.
  • Such an arrangement offers a physical obstruction to the flow of gas while permitting the metal to be treated to pass therethrough.
  • Various materials may be employed to form the partitions. For example, they may be of steel or ceramic material or may be of a suitable composite or laminate.
  • the reducing gas may be hydrogen, typically supplied from a container of commercial pure hydrogen under pressure, or an ammonia cracker, or may be a hydrocarbon such as methane or propane.
  • the reducing gas may alternatively be a mixture of carbon monoxide and hydrogen generated in situ by thermal decomposition of a volatile organic compound, such as methanol. At temperatures above 700°C one mole of methanol decomposes to yield one mole of carbon monoxide and two moles of hydrogen.
  • Methanol is a preferred source of hydrogen if the work to be heat treated is oily. If there is grease on the work it may also be advantageous to introduce water into the treatment region or a pre-heat region to combat deposition of soot on the work. This may be done by passing non-reactive gas through a humidifier before it enters the treatment region. It is important that the metal itself is not oxidised and thus non-oxidised or reducing conditions (so far as the metal is concerned) are maintained substantially throughout the furnace.
  • non-reactive gas may be introduced into the furnace at one or more locations intermediate the thermal region and the inlet, preferably with a horizontal component of velocity in the direction of the inlet, so as to help prevent or limit the ingress of air into the furnace through the inlet.
  • a baffle or baffles, or arrangement of chamber with supply of non-reactive gas thereto such as may be employed in the cooling region may be used at the inlet or entry end of the furnace.
  • the reducing gas in the gas mixture passing through the inlet is burnt off as in conventional operation of a continuous heat treatment furnace.
  • composition of the atmosphere in the thermal treatment region of the furnace will be chosen inter alia in accordance with the treatment to be performed, the composition of the metal to be treated, the dew point of the fluids used to form the atmosphere, whether or not the metal to be treated comes into the furnace carrying oil in its surface and the effectiveness of the measure adopted to limit or exclude air from the furnace.
  • Typical atmospheres that can be created in the thermal treatment region for various treatment of various materials are set out in Tables 1 and 2 below (though in some instances higher hydrogen concentrations may be employed).
  • the atmosphere substantially throughout the cooling region contains a substantially lower portion of reducing gas such as hydrogen than the atmosphere in the thermal treatment region.
  • relatively high hydrogen (or other reducing gas) concentrations in a major portion of the cooling region may be required (e.g. for efficient cooling or to enable an increased throughput of work to be dealt with) and indeed the reducing gas concentration may be higher than or substantially the same as that in the thermal treatment region.
  • This example relates to the annealing of ferrous metal parts in a standard Birlex 18" mesh belt furnace.
  • the mesh belt furnace indicated by the reference 2
  • the furnace has a thermal treatment region 8 located near to the inlet 4, and a cooling region 10, intermediate the outlet 6 and the thermal treatment region 8.
  • the thermal treatment region 8 is heated by means of "glow-bar" heating elements (not shown).
  • Work to be annealed is fed on to an endless mesh belt 11 which is driven around an endless path extending through the furnace 2 from the inlet 4 to the outlet 6, the belt 11 being mounted on rollers, 12, at least one of which is driven by means of a motor (not shown).
  • work to be annealed is loaded on to the belt just in advance of the inlet 4 and is conducted through the furnace at a chosen rate until it passes through the outlet 6 where it is lifted off the belt.
  • inlets 14 Positioned underneath the mesh belt 11 in the thermal treatment region 8 are two inlets 14 through which gas can be supplied to the treatment region 8. Inlets 14 form part of the furnace before it was adapted to operate the method according to the invention.
  • the injector 18 comprises an outer pipe 22 for nitrogen and an inner 26 for methanol coaxial with the pipe 22.
  • the pipe 26 terminates within the pipe 22, a short distance above its outlet.
  • the injector 20 is substantially identical to the injector 18 having an outer nitrogen pipe 24, and an inner methanol pipe 28.
  • the injectors 18 and 20 are operable such that droplets of methanol become entrained in the nitrogen and vaporise before impinging upon the work to be annealed.
  • a directional nitrogen injector 30 comprising a pipe having perforations or apertures pointing at an angle of 45° to the vertical in the direction of the outlet 6 extends into the cooling region 10 from the roof of the furnace 2.
  • the injector 30's position in the cooling region is relatively near to the outlet 6 of the furnace.
  • Positioned intermediate injector 30 and the outlet 6 are four rows of curtains 34 depending from the roof furnace 2 and ending a sufficient distance above the mesh belt 11 to enable work to pass therethrough.
  • the curtains each comprise a multitude of closely grouped together, generally vertically depending, glass fibres which when the curtain is "closed” substantially obturate the outlet of the furnace, but which may be parted by metal passing through the furnace thereby permitting the metal to pass out of the furnace.
  • a directional nitrogen injector 32 Extending downwardly into an upper part of the cooling region 10 is a directional nitrogen injector 32 having apertures or perforations pointing at an angle of 45° to the vertical in the direction of the thermal treatment region 8.
  • the injector 32 is positioned intermediate the injector 30 and the thermal treatment region.
  • nitrogen is typically introduced into the cooling region 10 from the injectors 30 and 32 so as to purge air from the furnace.
  • the means for heating the thermal treatment region 8 are then activated so as to raise the temperature therein to a chosen treatment value.
  • Nitrogen and methanol may then be introduced into the treatment region 8 so as to create a desired atmosphere therein.
  • the methanol, introduced as liquid flows into the treatment region 8, so it vaporises with a considerable expansion in volume.
  • the nitrogen introduced into the treatment region 8 through the injectors 18 and 20 and through the inlets 14 is warmed from about ambient temperatures to the treatment temperature and also expands.
  • the nitrogen introduced into the cooling region 10 through the injector 32 has a component of velocity in the direction of the thermal treatment region 8 and its flow is arranged to be sufficient so as to inhibit considerably the flow of expanding gases out of the thermal treatment region 8 into the cooling region 10. These gases thus flow largely in the direction of the inlet 4. They pass into a flue 38 where flammable constituents are burned off. A sliding plate 40 is provided for the purposes of adjusting the flow of such gas into the flue 38.
  • the flow of gases under the plate 40 will be sufficient to prevent ingress of substantial quantities of air into the furnace through the inlet 4.
  • nitrogen may be introduced into the furnace intermediate the treatment region 8 and the inlet 4 through a nozzle or injector (not shown) having one or more outlets pointing towards inlet 4. The additional nitrogen flow thus created helps prevent ingress of air through the inlet 4.
  • the arrangement of the injector 30 and the curtains 34 substantially limits the ingress of air into the furnace through the outlet 6. If there is any flue associated with the outlet 6, similar to the flue 38, for burning-off imflammable gas, this should be sealed to prevent air flowing into the furnace therethrough.
  • Suitable nitrogen-methanol supply equipment for the use with the furnace shown in Figure 1 is illustrated in Figure 2.
  • the equipment includes a nitrogen supply pipeline 50 communicating with a source (not shown) of commercially pure nitrogen.
  • this source is a vacuum-insulated vessel containing nitrogen in its liquid state, the vessel being fitted with a vaporiser so as to vaporise liquid nitrogen.
  • the supply equipment also includes a pipeline 52 communicating with a vessel (not shown) containing liquid methanol.
  • the methanol may be supplied to the pipeline 52 by means of a pump or under the pressure of nitrogen supplied to the ullage space of the aforesaid vessel containing methanol.
  • An isolating or shut-off valve 54 is positioned in the nitrogen pipeline 50 and is operable to isolate the inlet 14, the injector 18, 20, 30 and 32 from the source of nitrogen.
  • a pressure regulator 56 is located downstream, of the valve 54 in the pipeline 50 and is operable to adjust the supply in pressure of nitrogen to pipes 58, 60, 62 and 64, communicating with the pipeline 50 downstream of the regulator 56.
  • a pipe 58 communicates with two subsidiary pipes 72 and 74, serving the injectors 30 and 32 respectively.
  • the pipe 60 communicates with the inlets 14, the pipe 62 with the nitrogen pipe 22 of the injector 18 and the pipe 64 connects the source of nitrogen to the pipe 24 of the injector 20.
  • Flow control valves 66 are located in each pipe 60, 62 and 64. In each such pipe there is provided a flow meter 68 downstream of the valve 66.
  • a flow meter is also provided in the pipe 58.
  • a pressure regulator 70 located downstream of the respective flow meter 68.
  • the pipe 58 ends in the union of the pipes 72 and 74 and flow control valves 76 and 78 are provided in the pipes 72 and 74 respectively.
  • the apparatus shown in Figure 2 has means for humidifying nitrogen supplied to the injector 20.
  • This means comprises a drum 82 containing water having an inlet 80 which is submerged beneath the water and which communicates with the pipeline 64 downstream of the valve 70.
  • the drum 82 has an outlet communicating with a pipe 86 leading to the nitrogen pipe 28 of the injector 20.
  • valve 84 is opened and all the nitrogen in the pipe 64 flows through the valve 84 and thence into the pipe 86, whereas when the valve 84 is closed, all the nitrogen entering the pipeline 64 flows through the drum 82.
  • the purpose of the humidifier will be described below.
  • the methanol pipeline 52 has first shut off or isolating valve 88, disposed therein. Downstream of the methanol pipe 88 is a filter 90 to remove any suspended solids from the methanol.
  • a pipeline 96 communicates with the pipeline 52 downstream of filter 90, the pipeline 96 communicating with the methanol pipe 26 of the injector 18.
  • a flow control valve 98 is provided in pipe 96, and downstream of the valve 98 is a flow meter 100. Downstream of the union of the pipeline 96 with the pipeline 52, is a flow control valve 92, and downstream of that a flow meter 94. Downstream of the flow meter 94, the pipeline 52 communicates with the methanol pipe 28 of the injector 20.
  • the furnace 2 Before adaption by fitting the injectors 18, 20, 30 and 32 and the curtains 34, and connecting the inlets 14 to the nitrogen (as well as shutting off any flue at the outlet end of the furnace), the furnace 2 was operated by supplying 2,000 standard cubic feet per hour (57 standard cubic metres per hour) of rich exothermically generated gas to the thermal treatment region 8 through the inlets 14 and 16. The resulting flammable gas mixture was burned off at both ends of the furnace. Ih was found that bright work could be obtained by operating the method according to the invention when the furnace was adapted as shown in Figures 1 and 2. In a tyical example, universal joint forgings were annealed at 800'C in the thermal treatment region 8 and then cooled to near ambient temperature in the cooling region 10. The supply of nitrogen and methanol to the respective fluid inlets and injectors was as follows:
  • Parts from large castings to small pressings were treated in the furnace with the nitrogen and methanol supplied to the furnace at the rates described above and at maximum thermal treatment region temperatures in the range 720 to 1060°C.
  • Figure 3 illustrates the variation in the composition of the furnace atmosphere with the location in the furnace when the treatment region 8 is operated at 970°C. It can be seen that the concentration of hydrogen in the atmosphere in the treatment region 8 was in the order of 7%, but it decreased progressively along the cooling region 10 in the direction of the outlet 6, falling to below 1% before the outlet 6 is reached. Similarly, the carbon monoxide level falls from between 3.5% and 4% in the thermal treatment region to below 1% at the end of the cooling region 10 remote from the thermal treatment region 8. There is a corresponding fall in carbon dioxide concentration from about 0.4% in the thermal treatment region 8 to below 0.1 % at the end of the cooling region 10 remote from the thermal treatment region 8 (all percentages are by volume). Thus the gas leaving the furnace through the outlet 6 was substantially free of flammable reducing gas.
  • methanol was chosen as the source of reducing gas in view of the oily condition of some of the work to be treated.
  • the injectors 18 and 20 were designed with the pipes 22 and 24 closed at their respective bottoms but with orifices in their sides.
  • methanol leaving the pipes 26 and 28 struck the closed ends of the pipes 22 and 24, breaking into droplets which were carried by the nitrogen through orifices in the pipes 22 and 24 into the treatment region 8.
  • the humidifier drum 82 was used to add water vapour to the atmosphere and thereby help prevent soot formation on the work and the furnace structure.
  • a flame curtain was provided under the mesh belt 10 at the inlet end of the furnace when treating large pressings. The purpose of this was to consume oxygen in trapped air from the underside of the pressings.
  • This example relates to the sintering of bronze on to a steel backing in a suitable continuous sintering furnace as illustrated in Figure 4.
  • a continuous furnace 200 has an entrance 202 for work to be sintered, a thermal treatment region 204 having means (not shown) for raising it to a treatment temperature, a region 206 intermediate the entrance 202 and the thermal treatment region 204, and an exit 208.
  • This inlet 212 is part of the conventional fittings of the furnace.
  • Eight injectors 214 terminate in the cooling region 210, each injector being associated with its own nitrogen supply pipeline 216 in which are disposed a flow control valve 218 and a calibrated orifice 220 downstream of the flow control valve 218.
  • the pipes are all connected to a common pipeline 222 for the supply of nitrogen.
  • a nitrogen distribution, pipe 224 terminating in the furnace.
  • the orientation of the distribution pipe 224 is adjustable so as to enable the direction at which gas issues therefrom to be varied. It is preferably set such that there is a substantial component of velocity in the direction of the exit.
  • the distributor pipe 224 has outlet orifices whose axes extend at an angle of 45° to the vertical.
  • Curtains 226 are positioned in the furnace between the injector 224 and the outlet 208.
  • the distribution pipe 224 has its own nitrogen supply pipe 228 in which is disposed a flow control valve 230 upstream of a calibrated orifice 232.
  • the pipe 228 is connected to the pipeline 222.
  • the cooling region 210 is typically cooled by an arrangement of water jackets 234.
  • Nitrogen may also be supplied to the region 206 of the furnace 200 through a distributor pipe 238 that is analogous to the distribution pipe 224.
  • the pipe 238 is positioned such that gas issuing from it has a substantial component of velocity in the direction of the inlet 202.
  • the arrangement of the pipe is such that gas leaves the pipe at an angle of 45° to the vertical.
  • the pipe 238 is associated with pipe 240 having a calibrated orifice 242 disposed therein and a flow control valve 244 upstream thereof.
  • the gas inlet 212 is connected to a gas mixing panel 246 which is in turn connected to a source of nitrogen (not shown), and a source of cracked ammonia.
  • a source of nitrogen not shown
  • a source of cracked ammonia At its inlet and outlet ends, the furnace is provided as a standard fitting with gas pipes (not shown). These pipes are sealed off. Also at the inlet and outlet ends of the furnace are flues 252. The flue at the outlet end of the furnace is sealed.
  • the operation of the furnace shown in Figure 4 is substantially similar to that shown in Figure 1.
  • Work to be sintered is advanced through the furnace 200 by means (not shown).
  • a chosen mixture of nitrogen and cracked ammonia is introduced to the thermal treatment region 204 of the furnace from the inlet pipe 212 located in the cooling region 210.
  • the injectors 214 are used to introduce nitrogen at spaced apart locations in the cooling region 210 so as to create in the cooling region a nitrogen flow that helps to prevent free flow of gas from the entrance 202 and the thermal treatment region 204 in the direction of the outlet 208.
  • the curtains 226 act as an impedance to the flow of gas out of the furnace 200 through the exit 208, and also the nitrogen directed thereat from the distributor pipe 224 to help to prevent the ingress of air into the furnace through the exit 208.
  • the nitrogen directed to the entrance 202 from the distributor pipe 238 helps to prevent ingress of air into the furnace through the inlet.
  • Nitrogen and cracked ammonia entering the thermal treatment region 204 tend to expand and by virtue of the introduction of nitrogen through the injector 214 into the cooling region 210 tend to flow out of the thermal treatment region 204 through region 206, and then into the flue 252 where the content of inflammable gas (hydrogen) is burned-off. It is to be appreciated that the effect of the production of nitrogen into the cooling zone 210 through the injectors 214 and the distributor 224 renders negligible the amount of inflammable gas in the gas leaving the furnace through the outlet 208.
  • an atmosphere containing from 20 to 30% by volume of hydrogen and a balance of nitrogen is conventionally used, this atmosphere being supplied to the furnace through the inlet 212 and the inlet 250.
  • the nitrogen flow to each of the injectors 214 and the distributor 224 may typically amount to some 400 to 500 standard cubic feet per hour, the nitrogen flow being evenly divided between the eight injectors and the distributor pipe.
  • the gas mixture supplied to the pipe 212 and thence to the thermal treatment region may typically be a mixture of 50 standard cubic feet per hour (1.42 standard cubic metres per hour) of cracked ammonia (25% nitrogen, 75% hydrogen) and up to 300 standard cubic feet per hour of nitrogen (8.5 standard cubic metres per hour).
  • Nitrogen is preferably supplied to the distributor 238 at a rate of 150 to 200 standard cubic feet per hour (4.2 to 5.7 standard cubic metres per hour).
  • This example relates to the bright annealing of ferrous or non-ferrous metal strip in an FHD mesh belt furnace.
  • a mesh belt advances strip (or other metal to be treated) from the inlet or entry 602 to the furnace to the outlet or exit 604 from the furnace.
  • the furnace has, in sequence, advancing from the entry 602 to the exit 604, an inlet region 606, a thermal treatment region 608, and a cooling region 610.
  • chambers 612, 614 and 616 defined by generally vertical partitions 618 that co-operate with the walls of the furnace to define the chambers.
  • a sliding plate 619 is provided at the exit 604 and defines a further chamber 621 with the nearest of the partitions 618 thereto.
  • a flare-off means 620 is provided in communication with the top or roof of the inlet region 606 at a location intermediate a chamber 622 in the inlet region 606 and the thermal treatment region 608.
  • the chamber 622 is defined between the walls of the furnace, a first sliding plate 626, inclined at an angle to vertical, at the entry 602, and a hinged plate 624 which may be raised or lowered to vary the size of the gap between the bottom edge of the plate 624 and the mesh belt (not shown).
  • the chambers 612, 614 and 616 each communicate with upper and lower nitrogen-supply plenum chambers 628 and 630, and the chamber 622 with analogous nitrogen-supply plenum chambers 632 and 634.
  • the furnace is also provided with a variable angle nitrogen injector 636 situated in the inlet region 606 of the furnace intermediate the plate 626 and the thermal treatment region 608.
  • a nitrogen inlet 640 to the furnace is also provided at a location in the cooling region 610 near to the thermal treatment region.
  • a variable angle hydrogen injector 638 is also provided in the cooling region outside but near to the chamber 612. The arrangement of the chambers 612, 614 and 616 is shown schematically in Figure 6.
  • the partitions 618 comprise steel plates or flaps each hinged to a support 642 depending from the roof 644 of the furnace.
  • the floor 646 of the furnace and the roof 644 are formed with spaced-apart slots 648 therein to allow nitrogen to pass into each of the chambers 612, 614 and 616 from the chambers 628 and 630.
  • the chambers 628 and 630 have nitrogen inlets 650 and 652 connectible to a source of nitrogen.
  • Baffle plates 654 and 656 are provided in the chamber to block the direct path between the inlets 650 and 652 and the respective sets of slots 648. Thus, in operation, nitrogen flows around the baffles 654 and 656 and through the slots 648, typically providing a laminar flow of gas into the furnace.
  • the partitions hang at an angle at about 10° to the vertical (with their bottom edges nearer to the exit 604 than their top edges) so as to enable some of the nitrogen to be deflected thereby and thus to be given a horizontal component of velocity in the direction of the exit.
  • each partition 618 contacts the metal strip being heat treated as it is passed through the furnace.
  • each partition 618 may be provided at its edges with sealing means (not shown) to prevent substantially all gas flow between the partition and the side walls of the furnace. There is however intercommunication between the chambers over the top edge of the partitions and through the mesh belt 658 of the furnace, but seals at such top edge can readily be provided, if desired.
  • the furnace shown in Figures 5 and 6 may be operated as follows.
  • Nitrogen is supplied to the chambers 628, 630, 632 and 634 and this is effective to flush air out of the furnace.
  • the thermal treatment region 608 of the furnace is raised to a treatment temperature by heating means (not shown) associated with the furnace.
  • Hydrogen is then supplied to the furnace through the variable angle injector 638, typically orientated so as to direct gas downwards at an angle of 20° to the vertical with a horizontal component of velocity in the direction of the inlet end of the furnace.
  • the hydrogen reacts with any residual air in the thermal treatment region and once substantially all such residual air has been removed, strip to be annealed may be advanced continuously through the furnace.
  • the furnace is typically set up with the inlets 636 and 640 closed, and the plates 624, 626 and 619 in their lowermost positions.
  • Nitrogen passes into the chambers 612, 614 and 616 from the upper and lower supply chambers 628 and 630. A pressure in the chambers 612, 614 and 616 in excess of atmospheric pressure is built up. Some nitrogen will thus flow from chamber 616 into the chamber 621 and out of the furnace through exit 604. Introduction of hydrogen into the cooling region from the injector 638 and flow of nitrogen from the chambers 616, 614 and 612 into the cooling region 610 provides a flow of a gas mixture comprising nitrogen and hydrogen into the thermal treatment region 608.
  • This directional flow is caused partly by the obstruction to flow in the opposite direction presented by the partitions 618 and the gas pressure in the chambers 612, 614 and 616, and partly by burning flammable gas issuing from the thermal treatment region 608, such flammable gas being burned in the flare-off means 620.
  • the burning helps to induce a flow in the direction of the entry 602 to the furnace).
  • the gas flows or diffuses in the direction of the thermal treatment region so it is progressively warmed (by convection from the thermal treatment region). Such warming causes the gas to expand and thus tends to create a back pressure in the cooling region 610.
  • the pressure in the cooling region 610 at a point near to the chamber 612 and intermediate the chamber 612 and the thermal treatment region 608 will be greater than atmospheric pressure and greater than the pressure in the thermal treatment region 608 itself, provided nitrogen is supplied at a suitable flow rate to the chambers 628 and 630.
  • Flammable gas mixture is burned in the flare- off means 620 as aforementioned. Nitrogen supplied to the chamber 622 from the supply chambers 632 and 634 impedes flow of hydrogen past the burn-off zone and also helps to impede flow of air into the furnace through the entrance 602.
  • Experiments Nos 1 and 2 show that relatively high concentrations of hydrogen can be obtained in the cooling and thermal treatment regions while ensuring that the gas leaving the furnace through the exit 604 is non-flammable.
  • additional nitrogen was admitted into the furnace through the inlet 640.
  • the proportion of hydrogen in the thermal treatment region was substantially less than in Experiments Nos 1 and 2 while still obtaining a relatively high proportion of hydrogen in the cooling region. This demonstrates that a generally unidirectional flow regimen from the cooling region to the thermal treatment region was obtained.
  • Experiment Nos 4 and 5 show that all of the nitrogen supplied to the chambers 612, 614 and 616 may be introduced from the upper plenum chamber 628, and that all of the nitrogen supplied to the chamber 622 may be introduced thereto from the lower plenum chamber 634.
  • the chambers near the exit end of the furnace maybe provided by means of a custom-built unit fitted to the exit end of the furnace, thereby extending the length of the furnace.
  • the method according to the present invention may be operated on continuous furnaces used for sintering and having a region in which oil and lubricant on the work being sintered is oxidised. Such region is intermediate the inlet of the furnace and the thermal treatment region. Typically, the sintering temperature in the thermal treatment region is 1100°C and the delubrication region is maintained at a temperature in the range 500 to 700°C.
  • the furnace may be provided with chambers at its entry and exit ends in the manner shown in and described with reference to Figures 5 and 6. In such a furnace a suitable flow regimen may be created by burning off gas only near the entry end with gas being supplied at the following rates.
  • Nitrogen is supplied to the chambers at the end of the cooling region remote from the thermal treatment region at a rate of from 150 to 200 cubic feet per hour (4.2 to 5.7 cubic metres per hour) and at a similar rate to the chamber at the entry end of the furnace.
  • Gas generated in an endothermic generator (typically including about 40% by volume of hydrogen) is passed into the cooling region at a location outside but near to the chambers in that region at a rate of 100 cubic feet per hour (2.8 cubic metres per hour).
  • Such endothermic gas is also introduced into the cooling region at a location near to the thermal treatment region at a rate of 250 cubic feet per hour (7.1 cubic metres per hour) and nitrogen is introduced into the same region at a rate of 350 to 400 cubic feet per hour (10 to 11.3 cubic metres per hour).

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Tunnel Furnaces (AREA)
  • Furnace Details (AREA)

Claims (9)

1. Verfahren zum Betrieb eines kontinuierlichen, waagerechten Wärmebehandlungsofens, der in Folge aufweist: einen Eintritt, einen Wärmebehandlungsschnitt, einen Kühlabschnitt und einen Austritt, wobei wärmezubehandelndes Gut durch den Ofen von dem Eintritt zu dem Austritt geführt wird und der Ofen zu einer Art gehört, welche zum konventionellen Betrieb mittels Zufuhr von reduzierendem Gas und nichtreaktionsfähigem Gas, ausgewählt unter Stickstoff und Argon, zu seinem Wärmebehandlungsabschnitt eingerichtet ist, und wobei wesentliche Gasströmungen aus dem Wärmebehandlungsabschnitt sowohl in Richtung auf den Eintritt als auch in Richtung auf den Austritt vorliegen, und wobei das gesamte Gas, das aus dem Ofen austritt, aus den Austritt- und Eintrittabschnitten des Ofens abgegeben wird, und wobei Einrichtungen vorgesehen sind, um das Eingringen von Luft in den Ofen durch den Eintritt und den Austritt einzuschränken und reduzierendes Gas in den Ofen eingeführt wird und nichtreaktionsfähiges Gas, ausgewählt unter Stickstoff und Argon, in den Ofen an einer Vielzahl von derart ausgewählten Orten, daß ein Strömungsmuster gebildet wird, in welchem Atmosphären unterschiedlicher Zusammensetzungen zueinander in den Wärmebehandlungs- und Kühlabschnitten bestehen, eingeführt wird, worin nicht-oxidierende oder reduzierende Bedingungen über die Wärmebehandlungs- und Kühlabschnitte des Ofens hergestellt werden, wobei wenigstens ein Vorhang oder eine Abtrennung in dem Kühlabschnitt am Austrittsende des Ofens vorgesehen ist und nicht- reaktionsfähiges Gas in den Ofen nahe bei diesem Vorhang oder dieser Abtrennung mit einer solchen Strömungsrate zugeführt wird, daß die Strömung des Gases aus dem Wärmebehandlungsabschnitt in den Kühlabschnitt gehemmt wird und daß Gas aus dem Wärmebehandlungsabschnitt in starkem Maße in Richtung zum Ofeneintritt strömt, wobei die Gesamtrate en Versorgungsgas zu dem Ofen geringer als bei konventionellem Betrieb des Ofens ist.
2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß reduzierendes Gas ebenfalls in den Kühlabschnitt eingeführt wird und in den Wärmebehandlungsabschnitt strömt.
3. Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß die den Ofen verlassende Gasatmosphäre nur nahe dem Eintrittsende des Ofens abgebrannt wird.
4. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß die Abtrennungen und/oder Vorhänge wenigstens eine Kammer begrenzen, die ausgelegt ist, um zu behandelndes Metall hierdurch durchtreten zu lassen, und daß nicht-reaktionsfähiges Gas in die Kammern oder wenigstens eine dieser Kammern eingeführt wird.
5. Verfahren zum Betrieb eines kontinuierlichen, waagerechten Wärmebehandlungsofens, der in Folge aufweist: einen Eintritt, einen Wärmebehandlungsabschnitt, einen Kühlabschnitt und einen Austritt, wobei wärmezubehandelndes Gut durch den Ofen von dem Eintritt zu dem Austritt geführt wird und der Ofen zu einer Art gehört, welche zum konventionellen Betrieb mittels Zufuhr von reduzierendem Gas und nichtreaktionsfähigem Gas, ausgewählt unter Stickstoff und Argon, zu seinem Wärmebehandlungsabschnitt eingerichtet ist, und wobei wesentliche Gasströmungen aus dem Wärmebehandlungsabschnitt sowohl in Richtung auf den Eintritt als auch in Richtung auf den Austritt vorliegen, und wobei das gesamte Gas, das aus dem Ofen austritt, aus den Austritt- und Eintrittabschnitten des Ofens abgegeben wird, nicht-reaktionsfähiges Gas, ausgewählt unter Stickstoff und Argon, zu der Kammer oder den Kammern zugeführt wird, um den Eintritt von Luft von der Außenseite des Ofens durch die Kammer oder die Kammern in einen Teil des Ofens zwischen den Kammern und den Wärmebehandlungsbereich einzuschränken, nicht-reaktionsfähiges Gas, ausgewählt unter Stickstoff und Argon, und reduzierendes Gas ebenfalls in den Ofen an vorgewählten Orten zur Erzeugung einer Atmosphäre für die Wärmebehandlung zugeführt wird, wobei eine Vielzahl von Vorhängen und/oder Abtrennungen in dem Kühlbereich zur Begrenzung von einer oder mehreren Kammern vorgesehen sind und nicht-reaktionsfähiges Gas direkt in eine solche Kammer mit einer solchen Strömungsrate zugeführt wird, daß die Gasströmung aus dem Wärmbehandlungsabschnitt in den Kühlabschnitt gehemmt wird und daß Gas aus dem Wärmebehandlungsabschnitt weitgehend in Richtung des Ofeneintrittes ausströmt, wobei die Gesamtrate des zu dem Ofen zugeführten Gases geringer als beim konventionellen Betrieb des Ofens ist.
6. Verfahren nach Anspruch 5, dadurch gekennzeichnet, daß
Figure imgb0010
wobei
Pc der Druck in der Kammer oder der dem Wärmebehandlungsabschnitt nächstliegenden Kammer ist;
Pu der Druck im Kühlabschnitt unmittelbar anschließend an diese Kammer oder diese Kammern und zwischen diesen Kammern und dem Wärmebehandlungsabschnitt ist; und
Pa der atmosphärische Druck ist.
7. Verfahren nach Anspruch 6, dadurch gekennzeichnet, daß wenigstens zwei Kammern vorhanden sind, und;
Figure imgb0011
wobei Pc der Druck in der Kammer nächstliegend zum Wärmebehandlungsabschnitt ist;
Pu und Pa die in Anspruch 6 angegebene Bedeutung besitzen und Pt der Druck in dem Wärmebehandlungsabschnitt ist.
8. Verfahren nach einem der Ansprüche 5 bis 7, dadurch gekennzeichnet, daß eine Wasserstoffkonzentration von größer als 50 Vol.-% in dem Teil des Kühlabschnittes zwischen dem Wärmebehandlungsabschnitt und den Kammern erzeugt wird, und daß ein nicht-entflammbares Gasgemisch das Austrittsende des Ofens verläßt.
9. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß wenigstens , eine Kammer an dem Eintrittsende des Ofens vorgesehen ist und nicht-reaktionsfähiges Gas, ausgewählt uner Stickstoff und Argon, direkt zu dieser Kammer zugeführt wird.
EP19820304867 1981-09-19 1982-09-15 Wärmebehandlung von Metallen Expired EP0075438B1 (de)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
GB8128392 1981-09-19
GB8128392 1981-09-19
GB8217338 1982-06-15
GB8217338 1982-06-15

Publications (2)

Publication Number Publication Date
EP0075438A1 EP0075438A1 (de) 1983-03-30
EP0075438B1 true EP0075438B1 (de) 1987-12-16

Family

ID=26280755

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19820304867 Expired EP0075438B1 (de) 1981-09-19 1982-09-15 Wärmebehandlung von Metallen

Country Status (6)

Country Link
EP (1) EP0075438B1 (de)
JP (1) JPH0617501B2 (de)
AU (1) AU556896B2 (de)
DE (1) DE3277843D1 (de)
ES (2) ES515780A0 (de)
GB (1) GB2108156B (de)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2583064A1 (fr) * 1985-06-05 1986-12-12 Air Liquide Procede de traitement thermique, hotte pour la mise en oeuvre de ce procede et son utilisation dans les fours de traitement thermique
EP0311030A1 (de) * 1987-10-07 1989-04-12 Linde Aktiengesellschaft Verfahren zum Glühen von Metallteilen in Durchlauföfen
FR2628753A1 (fr) * 1988-03-16 1989-09-22 Air Liquide Procede et dispositif de traitement de recuit d'articles metalliques en four horizontal
FR2628752A1 (fr) * 1988-03-16 1989-09-22 Air Liquide Procede et dispositif de traitement de recuit de bandes metalliques en four vertical
FR2629188A1 (fr) * 1988-03-22 1989-09-29 Messer Griesheim Gmbh Procede d'alimentation d'une installation de recuit verticale ou horizontale en gaz protecteur et de reaction
DE3828134A1 (de) * 1988-08-18 1990-02-22 Linde Ag Verfahren zur waermebehandlung von werkstuecken
EP0379104A1 (de) * 1989-01-17 1990-07-25 Linde Aktiengesellschaft Verfahren zum Glühen von Metallteilen unter wasserstoffreichem Schutzgas in einem Durchlaufofen
US4966632A (en) * 1988-03-16 1990-10-30 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Process for the annealing treatment of metal strips
US5798007A (en) * 1996-03-13 1998-08-25 Stein Heurtey Process and apparatus for the continuous heat treatment of a metal strip travelling in a different atmosphere
US6561799B2 (en) 1999-12-06 2003-05-13 Snecma Propulsion Solide Sealing box for a chamber for continuously treating a thin strip product, in particular for a furnace for continuously carbonizing a fiber substrate

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT395321B (de) * 1983-07-05 1992-11-25 Ebner Ind Ofenbau Verfahren zum abkuehlen von chargen in diskontinuierlich arbeitenden industrieoefen, insbesondere von stahldraht- oder - bandbunden in haubengluehoefen
JP3002518B2 (ja) * 1990-10-17 2000-01-24 株式会社日立製作所 液晶表示装置
DE4104982A1 (de) * 1991-02-19 1992-08-20 Linde Ag Durchlaufwaermebehandlungsanlage mit spezieller schutzgasabsaugung
IL119434A (en) * 1995-11-27 2000-01-31 Boc Group Inc Furnace
DE10050673C1 (de) * 2000-10-04 2002-04-18 Kohnle W Waermebehandlung Verfahren zum Anlassen von Werkstücken in einem Ofen unter einer Schutzgasatmoshäre
LU90721B1 (en) * 2001-01-25 2002-07-26 Circuit Foil Luxembourg Trading Sarl Method for producing metal foams and furnace for producing same
JP2003003211A (ja) * 2001-06-19 2003-01-08 Kanto Yakin Kogyo Co Ltd アルゴン雰囲気下での金属の連続熱処理方法
US7458991B2 (en) 2002-02-08 2008-12-02 Howmedica Osteonics Corp. Porous metallic scaffold for tissue ingrowth
BE1015109A3 (fr) * 2002-09-13 2004-10-05 Drever Internat S A Procede de traitemant thermique de bande metallique.
DE10347312B3 (de) * 2003-10-08 2005-04-14 Air Liquide Deutschland Gmbh Verfahren zur Wärmebehandlung von Eisenwerkstoffen
BRPI0702253B1 (pt) 2006-04-04 2020-02-04 Linde Ag processo de tratamento térmico de peças em um forno de tratamento térmico
DE102006015739A1 (de) * 2006-04-04 2007-10-11 Linde Ag Verfahren zur Wärmebehandlung
EP1842931B1 (de) * 2006-04-04 2014-02-19 Linde AG Verfahren zur Wärmebehandlung
FR2903121B1 (fr) * 2006-06-30 2008-09-19 D M S Sa Installation de traitement thermique en continu, destine au recuit brillant d'une bande d'acier inoxydable
CN100465302C (zh) * 2006-08-17 2009-03-04 武汉钢铁(集团)公司 三段式可控气氛热处理炉
EP3372935A1 (de) * 2017-03-08 2018-09-12 Paul Wurth S.A. Fördervorrichtung für schüttgut
FR3070976B1 (fr) * 2017-09-14 2020-02-28 Adam Pyrometrie Four verrier electrique portatif de recuisson d'objets de verre hauts, dote d'une porte selon un mouvement cinematique
CN113136482A (zh) * 2020-01-19 2021-07-20 天津阿瑞斯工业炉有限公司 一种单真空辊底式保护气氛热处理设备及其工艺
CN112029978A (zh) * 2020-08-11 2020-12-04 江苏常宝普莱森钢管有限公司 一种控制热处理炉内表面氧化保护气氛的配比方法

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE617319C (de) * 1931-05-02 1935-08-16 Benno Schilde Maschb Akt Ges Verfahren und Einrichtung zum Blankgluehen
GB429940A (en) * 1933-12-08 1935-06-11 John Lindon Pearson Improvements in or relating to annealing processes and furnaces
GB515121A (en) * 1937-05-24 1939-11-27 Wilhelm Doderer Apparatus for the treatment of materials with gases under pressure
FR55831E (fr) * 1943-02-02 1952-09-08 Perfectionnements aux procédés et dispositifs pour le revêtement d'objets en métal par des couches protectrices d'un métal différent
DE861569C (de) * 1944-02-03 1953-01-05 Accumulatoren Fabrik Ag Verfahren und Einrichtung zum Blankgluehen und Sintern, insbesondere von Metallen
GB695624A (en) * 1949-10-05 1953-08-12 Birlec Ltd Improvements in, or relating to, continuous furnaces
GB794140A (en) * 1955-01-17 1958-04-30 Metal Rolling And Tube Company Improvements relating to the heat-treatment of metal articles
US3467366A (en) * 1967-10-02 1969-09-16 Hayes Inc C I Furnace construction having atmosphere curtain
US3738025A (en) * 1972-07-31 1973-06-12 Hanson Ind Inc Ski boot having variable stiffness
US3950192A (en) * 1974-10-30 1976-04-13 Monsanto Company Continuous carburizing method
JPS5238105U (de) * 1975-09-10 1977-03-17
JPS53125210A (en) * 1977-04-07 1978-11-01 Kobe Steel Ltd Preparation of steel material having small amount of scale

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0206873A1 (de) * 1985-06-05 1986-12-30 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Wärmebehandlungsverfahren, Gasabdichtungsvorrichtung und dessen Verwendung in Wärmebehandlungsöfen
FR2583064A1 (fr) * 1985-06-05 1986-12-12 Air Liquide Procede de traitement thermique, hotte pour la mise en oeuvre de ce procede et son utilisation dans les fours de traitement thermique
EP0311030A1 (de) * 1987-10-07 1989-04-12 Linde Aktiengesellschaft Verfahren zum Glühen von Metallteilen in Durchlauföfen
US4966632A (en) * 1988-03-16 1990-10-30 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Process for the annealing treatment of metal strips
FR2628753A1 (fr) * 1988-03-16 1989-09-22 Air Liquide Procede et dispositif de traitement de recuit d'articles metalliques en four horizontal
FR2628752A1 (fr) * 1988-03-16 1989-09-22 Air Liquide Procede et dispositif de traitement de recuit de bandes metalliques en four vertical
BE1007266A3 (fr) * 1988-03-16 1995-05-09 Air Liquide Procede et dispositif de traitement de recuit de bandes metalliques.
FR2629188A1 (fr) * 1988-03-22 1989-09-29 Messer Griesheim Gmbh Procede d'alimentation d'une installation de recuit verticale ou horizontale en gaz protecteur et de reaction
DE3828134A1 (de) * 1988-08-18 1990-02-22 Linde Ag Verfahren zur waermebehandlung von werkstuecken
EP0355520A3 (en) * 1988-08-18 1990-04-18 Linde Aktiengesellschaft Method of heat treating workpieces
EP0355520A2 (de) * 1988-08-18 1990-02-28 Linde Aktiengesellschaft Verfahren zur Wärmebehandlung von Werkstücken
EP0379104A1 (de) * 1989-01-17 1990-07-25 Linde Aktiengesellschaft Verfahren zum Glühen von Metallteilen unter wasserstoffreichem Schutzgas in einem Durchlaufofen
US5798007A (en) * 1996-03-13 1998-08-25 Stein Heurtey Process and apparatus for the continuous heat treatment of a metal strip travelling in a different atmosphere
US6561799B2 (en) 1999-12-06 2003-05-13 Snecma Propulsion Solide Sealing box for a chamber for continuously treating a thin strip product, in particular for a furnace for continuously carbonizing a fiber substrate

Also Published As

Publication number Publication date
EP0075438A1 (de) 1983-03-30
ES8407573A1 (es) 1984-09-16
ES526964A0 (es) 1984-09-16
GB2108156B (en) 1986-01-15
AU8850882A (en) 1983-03-31
GB2108156A (en) 1983-05-11
AU556896B2 (en) 1986-11-27
ES8403163A1 (es) 1984-03-01
JPH0617501B2 (ja) 1994-03-09
JPH01127618A (ja) 1989-05-19
DE3277843D1 (en) 1988-01-28
ES515780A0 (es) 1984-03-01

Similar Documents

Publication Publication Date Title
EP0075438B1 (de) Wärmebehandlung von Metallen
US4340433A (en) Method of heat treating articles
JP5884748B2 (ja) 鋼帯の連続焼鈍装置および連続溶融亜鉛めっき装置
US4049473A (en) Methods for carburizing steel parts
US6126913A (en) Thermal oxidizers with improved preheating means and processes for operating same
US10792701B2 (en) Pipe coupling thermal cleaning and coating curing oven and method
JPS6124352B2 (de)
US2589811A (en) Gas atmosphere generating means for heat-treating furnaces
JP2665333B2 (ja) 連続式熱処理炉用フード
CA1151420A (en) Method and apparatus for the ignition of a solid fuel and a sinterable mixture
EP0233944B1 (de) Anlage zur kontinuierlichen behandlung von bandstahl mit einem direkt beheizten ofen
US4148946A (en) Method for maintaining a non-oxidizing atmosphere at positive pressure within the metallic strip preparation furnace of a metallic coating line during line stops
US2146760A (en) Annealing process
US3492378A (en) Method of operation of a continuous strip heating furnace
US2706110A (en) Metallurgical heating furnace
US2693952A (en) Forge furnace control
JPS58110617A (ja) 金属熱処理方法
US3399873A (en) Furnace for scaleless direct heating of metal charge destined to heattreatment
US1937812A (en) Heating furnace
US20080066834A1 (en) Direct-Fired Furnace Utilizing an Inert Gas to Protect Products Being Thermally Treated in the Furnace
US4210097A (en) Means for maintaining a non-oxidizing atmosphere at positive pressure within the metallic strip preparation furnace of a metallic coating line during line stops
EP0506043B2 (de) Brenner zur Russerzeugung und Ofen mit einem derartigen Brenner zur Russablagerung
US2240099A (en) Method of bright annealing elongated metal bodies
JPS6345358A (ja) 連続ガス浸炭方法
GB902674A (en) System for baking carbonaceous products or the like

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): BE DE FR NL SE

17P Request for examination filed

Effective date: 19830913

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): BE DE FR NL SE

ET Fr: translation filed
REF Corresponds to:

Ref document number: 3277843

Country of ref document: DE

Date of ref document: 19880128

PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

26 Opposition filed

Opponent name: LINDE AKTIENGESELLSCHAFT, WIESBADEN

Effective date: 19880916

NLR1 Nl: opposition has been filed with the epo

Opponent name: LINDE AKTIENGESELLSCHAFT

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Effective date: 19890916

PLBN Opposition rejected

Free format text: ORIGINAL CODE: 0009273

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: OPPOSITION REJECTED

27O Opposition rejected

Effective date: 19900323

NLR2 Nl: decision of opposition
EUG Se: european patent has lapsed

Ref document number: 82304867.3

Effective date: 19900521

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19950811

Year of fee payment: 14

Ref country code: FR

Payment date: 19950811

Year of fee payment: 14

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19950818

Year of fee payment: 14

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 19950824

Year of fee payment: 14

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Effective date: 19960930

Ref country code: BE

Effective date: 19960930

BERE Be: lapsed

Owner name: BOC LTD

Effective date: 19960930

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Effective date: 19970401

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 19970401

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Effective date: 19970603

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST