Classifications

• • 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
  • C21D1/76—Adjusting the composition of the atmosphere
  • C21D1/763—Adjusting the composition of the atmosphere using a catalyst

Definitions

• the invention relates to a method of heating, holding or heat treatment of metal material in an atmosphere of processing gas consisting predominantly of nitrogen and produced at, or in close vicinity to, the location where the heating, holding or heat treatment takes place.
• heat treatment is hereinafter used as a collective term embracing all the aforesaid processes.
• furnaces which may be of a multiplicity of different types and may operate batchwise or continuously.
• equipment is provided to ensure that the desired atmosphere is maintained in the furnace chamber during the heat treatment, that is, to ensure that the atmosphere is made up only of the pro cessing gas, which is controlled at least in respect of its composition.
• the processing gas is produced on the site, that is, within the plant or workshop where the heat treatment takes place.
• the equipment for the production of the processing gas is located in very close vicinity to the furnace
• processing gas consumption of 500-1000 m 3 /h at a single plant is not uncommon.
• the principal raw material for the production of the processing gas is hydrocarbon gas (liquefied petroleum gas, natural gas and the like), which is thus consumed in considerable quantities; a processing gas consumption of 700 m 3 /h corresponds to an annual consumption of liquefied petroleum gas of
• the present invention provides a possibility of drastically reducing the raw material cost for the processing gas in the cases where an installation which generates heat by the combustion of a suitable hydrocarbon fuel, such as liquefied petroleum gas or natural gas, is located at, or in close vicinity to, the location where the heat treatment takes place.
• a suitable hydrocarbon fuel such as liquefied petroleum gas or natural gas
• the principal characterizing feature of the invention is that the exhaust gases from such an installation are used as the principal raw material for the production of the processing gas.
• the invention is based on the realization of the fact that the exhaust gases of such an installation predominantly consist of nitrogen gas, that is, the predominant constituent of the processing gas.
• any of the ordinary hydrocarbon fuels such as fuel oil
• the processing gas should be virtually free of sulphur and ashes, at least the ordinary fuel oil grades must be disregarded in actual practice; the purification required by the exhaust gases produced by the combustion of such fuels renders their use uneconomical, at least if the purification is carried out by the techniques existing today.
• the installation producing the exhaust gas may be the furnace in which the heat treatment is carried out.
• the combustion of the hydrocarbon fuel used for the heating of the furnace chamber then is effected outside the furnace chamber so that the exhaust gases are kept away therefrom (indirect heating).
• the heating exhaust gases may also, or alternatively, be used for the production of processing gas for a different but neighbouring furnace requiring hydrogen-based processing gas. If the furnace producing the exhaust gas does not itself require a processing gas atmosphere, the hydrocarbon fuel may be combusted within the furnace chamber of that furnace, which may thus be directly heated.
• Fig. 1 is a diagrammatic illustration of a roller hearth furnace and an associated installation for producing a carbon-carrying processing gas for the furnace in accordance with the method of the invention.
• Fig. 2 is a diagrammatic illustration of the same furnace and an associated installation for producing a carbon-free processing gas for the furnace.
• the furnace 10 illustrated in the drawings is of a construction known per se. It is a continuous furnace and the material to be subjected to heat treatment in the furnace chamber of the furnace accordingly is continuously moved therethrough. At the ends of the closed, tunnel-like furnace chamber, gas locks 11 and 12 are provided to prevent the surrounding air from entering the furnace chamber.
• the furnace chamber is indirectly heated by a large number of radiation tubes 13 fired with liquefied petroleum gas or a similar hydrocarbon gas.
• the exhaust gases are passed from the radiation tubes into a header conduit 14. Rather than passing the exhaust gases into the surrounding atmosphere as hitherto, the exhaust gases in the present case are continuously fed from the header conduit 14 into an installation, generally designated 15, for producing a processing gas which consists essentially of nitrogen, hydrogen and carbon monoxide and which is continuously fed to the furnace chamber immediately inwardly of the discharge gas lock 12.
• the heating exhaust gases continuously flowing out from the header conduit 14 are at a temperature of 250-300oC and essentially consist of nitrogen, carbon dioxide (on the order of 10 percent by volume), oxygen (one or a few percent by volume) and water vapour (on the order of 10 percent by volume).
• the oxygen content is due to the fact that the combustion in the furnace is effected with a certain excess of air.
• the temperature of the exhaust gases is lowered to 20-30oC in a cooler 16, which may form part of a heat recovery system.
• the exhaust gases then are passed through a filter 17 in which solid particles are removed, whereupon a pump 18 feeds the exhaust gases to a drier 19, where most of the carbon dioxide and the water vapour is removed.
• a pump 18 feeds the exhaust gases to a drier 19, where most of the carbon dioxide and the water vapour is removed.
• the exhaust gases consist of one or a few percent by volume of oxygen, the balance being nitrogen (the unavoidable residues of carbon monoxide, water vapour, noble gases etc. are disregarded here).
• the oxygen content of the exhaust gases is determined by means of an oxygen content meter 20, and through an air conduit 21 having a control valve 22 controlled by the meter 20 and a flow meter 23 sufficient air is fed to the exhaust gases to impart to them a predetermined oxygen content matching the desired carbon monoxide content of the processing gas.
• the exhaust gases are then fed through a flow meter 24 to a so-called endo-generator 25.
• a controlled amount of liquefied petroleum gas is supplied through a conduit 26 including a control valve 27 and a flow meter 28; the quantity of said petroleum gas is relatively small in relation to the nitrogen content of the exhaust gases.
• thermal catalytic cracking of the petroleum gas is effected at about 950oC, the carbon forming carbon monoxide with the oxygen of the exhaust gases. Leaving the endo-generator 25 is thus a gas mixture of nitrogen (which constitutes the predominan portion of the gas mixture), carbon monoxide and nitrogen as well as traces of carbon dioxide, water vapour, hydrocarbon gas and noble gases.
• the gas mixture Downstream of the endo-generator 25 the gas mixture is cooled to a relatively low temperature (room temperature) in a cooler 29 whereupon it is fed as processing gas into a part of the furnace chamber serving as a cooling section, in which the processing gas flows in counter-current relation to the material being subjected to heat treatment.
• the amount of liquefied petroleum gas supplied through the conduit 26 is controlled by a carbon dioxide content or dew point meter 30 which is connected downstream of the cooler 29 and thus ensures the proper value of the so-called carbon potential of the processing gas.
• the processing gas continuously flowing from the furnace chamber may advantageously be used for scavenging the locks 12 and 13 in the manner described in Swedish published patent specification 364 729.
• the installation shown in Fig. 2 for producing carbon-free processing gas is generally designated 15A and identical with the installation of Fig. 1 in respect of certain elements which are therefore referenced by the same numerals in both figures.
• the installation 15A thus includes a cooler 16 connected to the header conduit 14 of the furnace 10, a filter 17, a pump 18, a drier 19, where carbon dioxide and water vapour are removed, an oxygen content meter 20 and an air conduit 21 including a control valve 22 controlled by the meter 20, and a flow meter 23.
• the installation moreover includes a flow meter 24 for the cooled, filtered and dried raw material gas admixed with oxygen up to a predetermined oxygen content of one or a few percent by volume.
• a controlled amount of so-called cracker gas is supplied through a conduit 31 including a control valve 32.
• This gas which consists of hydrogen gas and nitrogen gas, is supplied through a cooler 33 from a catalytic reactor 34 to which ammonia is fed.
• a different gas mixture of known hydrogen gas content or pure hydrogen gas may be supplied.
• the raw material gas with the admixed hydrogen gas is introduced into a so-called deoxo-reactor 35 in which the gas mixture is subjected to complete combustion by means of a noble metal catalyst.
• the combustion which raises the gas temperature to about 200°C, results in the formation of water vapour from the oxygen of the raw material gas and a portion of the hydrogen supplied through the conduit 31.
• the resulting gas mixture consisting of nitrogen, hydrogen and water vapour (and minor quantities of other gases) is fed through a cooler 36 to a drier 37, in which the water vapour is removed, and is then supplied as relatively cool processing gas into the furnace chamber as in Fig. 1.
• a meter 38 Downstream of the drier 37 a meter 38 is provided which measures the hydrogen content of the processing gas - which usually consists of 2 to 15 percent by volume of hydrogen and nitrogen as the balance - and controls the control valve 32 to bring it to pass an amount of gas matching the desired hydrogen gas content of the processi gas.
• the invention has been exemplified with particular reference to its application to a continuous furnace in which the amounts of exhaust and processing gases do not vary considerably over the time.
• the invention is also applicable to batch furnaces and hybrid forms of continuous and batch furnaces. It is also within the scope of the invention to vary the quantity of processing gas produced per unit of time in dependence on the demand of processing gas and/or the availability of the exhaust gases and, if required, to temporarily store the processing gas in a buffer storage.
• the invention is not limited to the above-mentioned metallurgical processes, that is, heating, holding or heat treatment of metal material, but also embraces within its scope other metallurgical processes which are carried out in an atmosphere of processing gas which consists essentially or predominantly of nitrogen gas and is produced at, or in close vicinity to, the location where the processes are carried out.

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Physics & Mathematics (AREA)
• Thermal Sciences (AREA)
• Crystallography & Structural Chemistry (AREA)
• Mechanical Engineering (AREA)
• Materials Engineering (AREA)
• Metallurgy (AREA)
• Organic Chemistry (AREA)
• Furnace Details (AREA)
• Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)

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• 1980
  • 1980-05-05 SE SE8003349A patent/SE8003349L/ unknown
• 1981
  • 1981-05-05 EP EP19810901121 patent/EP0052113A1/en not_active Withdrawn
  • 1981-05-05 BR BR8108584A patent/BR8108584A/pt unknown
  • 1981-05-05 WO PCT/SE1981/000134 patent/WO1981003184A1/en not_active Application Discontinuation
  • 1981-12-29 FI FI814187A patent/FI814187L/fi not_active Application Discontinuation
• 1982
  • 1982-01-04 DK DK182A patent/DK182A/da not_active Application Discontinuation

Non-Patent Citations (1)

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