US20220341021A1 - Surface hardening treatment device and surface hardening treatment method - Google Patents

Surface hardening treatment device and surface hardening treatment method Download PDF

Info

Publication number
US20220341021A1
US20220341021A1 US17/641,165 US202017641165A US2022341021A1 US 20220341021 A1 US20220341021 A1 US 20220341021A1 US 202017641165 A US202017641165 A US 202017641165A US 2022341021 A1 US2022341021 A1 US 2022341021A1
Authority
US
United States
Prior art keywords
gas
furnace
introduction
nitriding potential
ammonia
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.)
Pending
Application number
US17/641,165
Other languages
English (en)
Inventor
Yasushi Hiraoka
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.)
Parker Netsushori Kogyo KK
Original Assignee
Parker Netsushori Kogyo KK
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
Application filed by Parker Netsushori Kogyo KK filed Critical Parker Netsushori Kogyo KK
Assigned to Parker Netsushori Kogyo Co., Ltd. reassignment Parker Netsushori Kogyo Co., Ltd. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HIRAOKA, YASUSHI
Publication of US20220341021A1 publication Critical patent/US20220341021A1/en
Pending legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
    • C23C8/28—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases more than one element being applied in one step
    • C23C8/30—Carbo-nitriding
    • C23C8/32—Carbo-nitriding of ferrous surfaces
    • 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
    • C21D1/06—Surface hardening
    • 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
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
    • C23C8/28—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases more than one element being applied in one step
    • C23C8/30—Carbo-nitriding
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/80—After-treatment

Definitions

  • the present invention relates to a surface hardening treatment device and a surface hardening treatment method which can perform a surface hardening treatment, such as nitriding, nitrocarburizing, nitriding quenching (austenitic nitriding), and the like, for a work made of metal.
  • a surface hardening treatment such as nitriding, nitrocarburizing, nitriding quenching (austenitic nitriding), and the like, for a work made of metal.
  • nitriding there is a strong need for nitriding because it is a low distortion treatment.
  • a specific nitriding method there are a gas method, a salt bath method, a plasma method. and the like.
  • the gas method is comprehensively superior when considering quality, environmental properties, mass productivity, and the like.
  • Carburizing, carbonitriding or induction hardening (quenching) involved in hardening a mechanical part causes distortion, but the distortion can be improved when a nitriding treatment by a gas method (gas nitriding treatment) is used.
  • a nitrocarburizing treatment by a gas method (gas nitrocarburizing treatment) involved in carburizing is also known as a treatment of the same kind as the gas nitriding treatment.
  • the gas nitriding treatment is a process in which only nitrogen is permeated and diffused into a work, in order to harden a surface of the work.
  • an ammonia gas alone, a mixed gas of an ammonia gas and a nitrogen gas, a mixed gas of an ammonia gas and an ammonia decomposition gas (which consists of 75% hydrogen and 25% nitrogen, and is also called an AX gas), or a mixed gas of an ammonia gas an ammonia decomposition gas and a nitrogen gas is introduced into a processing furnace in order to perform a surface hardening treatment.
  • the gas nitrocarburizing treatment is a process in which carbon is secondarily permeated and diffused into a work together with nitrogen, in order to harden a surface of the work.
  • a mixed gas of an ammonia gas, a nitrogen gas and a carbon dioxide gas (CO 2 ) or a mixed gas of an ammonia gas, a nitrogen gas, a carbon dioxide gas and a carbon monoxide gas (CO) is introduced into a processing furnace in order to perform a surface hardening treatment, as a plurality of furnace introduction gases.
  • the basis of an atmosphere control in the gas nitriding treatment and in the gas nitrocarburizing treatment is to control a nitriding potential (K N ) in a furnace.
  • K N nitriding potential
  • the bending fatigue strength and/or the wear resistance of a mechanical part may be improved by selecting the ⁇ ′ phase and increasing its thickness, which can achieve a further high functionality of the mechanical part.
  • Non-Patent Document 1 a nitrocarburizing treatment is used for making positive use of the ⁇ phase which is hard, for example in order to improve the wear resistance (“Nitriding and Nitrocarburizing on Iron Materials”, second edition (2013), pages 81-86 (Dieter Liedtke et al., Agune Technical Center) Non-Patent Document 1).
  • Non-Patent Document 3 As for the method of controlling each furnace introduction gas, a method of controlling the total amount while keeping the flow rate ratio between the respective furnace introduction gases constant is well known (“Nitriding and Nitrocarburizing on Iron Materials”, second edition (2013), pages 158-163 (Dieter Liedtke et al., Agune Technical Center): Non-Patent Document 3).
  • JP-B-5629436 has disclosed a device which can perform both a first control step of controlling a total introduction amount of a plurality of furnace introduction gases while keeping a flow rate ratio between the plurality of furnace introduction gases constant and a second control step of controlling an introduction amount of each of the plurality of furnace introduction gases while changing a flow rate ratio between the plurality of furnace introduction gases (either one of the first control step and the second control step is selectively performed at a time) (JP-B-5629436: Patent Document 2).
  • the method of controlling a total introduction amount of a plurality of furnace introduction gases while keeping a flow rate ratio between the plurality of furnace introduction gases constant is advantageous in that the total used amount of the plurality of furnace introduction gases may be made smaller.
  • the controllable range of nitriding potential by means of this method is narrow.
  • the present inventor has already developed a control method that can achieve a wide controllable range of nitriding potential on the side of lower nitriding potential (for example, about 0.05 to 1.3 at 580° C.) and has obtained JP-B-6345320 (Patent Document 3).
  • an introduction amount of each of the plurality of furnace introduction gases is controlled by changing a flow rate ratio between the plurality of furnace introduction gases while keeping a total introduction amount of the plurality of furnace introduction gases constant. such that the nitriding potential in the processing furnace is brought close to the target nitriding potential.
  • the nitriding potential K N is defined by the following formula (2).
  • the partial pressure of ammonia in the furnace is represented by P NH3
  • the partial pressure of hydrogen in the furnace is represented by P H2
  • the nitriding potential K N is well known as an index representing the nitriding ability of the atmosphere in the gas nitriding furnace.
  • the thermal decomposition reaction represented by the formula (3) mainly (dominantly) occurs, and the nitriding reaction represented by the formula (1) is almost negligible quantitatively. Therefore, if the in-furnace ammonia concentration consumed in the reaction represented by the formula (3) or the hydrogen gas concentration generated in the reaction represented by the formula (3) is known, the nitriding potential can be calculated. That is to say, since 1.5 mol of hydrogen and 0.5 mol of nitrogen are generated from 1 mol of ammonia, if the in-furnace ammonia concentration is measured, the in-furnace hydrogen concentration can also be known and thus the nitriding potential can be calculated. Alternatively, if the in-furnace hydrogen concentration is measured, the in-furnace ammonia concentration can also be known, and thus the nitriding potential can also be calculated.
  • the ammonia gas that has been introduced (flown) into the gas nitriding furnace is circulated through the furnace and then discharged outside the furnace. That is to say. in the gas nitriding treatment, a fresh (new) ammonia gas is continuously flown into the furnace with respect to the existing gases in the furnace. so that the existing gases are continuously discharged out of the furnace (extruded at the supply pressure).
  • the flow rate of the ammonia gas introduced into the furnace is small, the gas residence time thereof in the furnace becomes long, so that the amount of the ammonia gas to be thermally decomposed increases, which increases the amount of the sum of the nitrogen gas and the hydrogen gas generated by the thermal decomposition reaction.
  • the flow rate of the ammonia gas introduced into the furnace is large, the amount of the ammonia gas to be discharged outside the furnace without being thermally decomposed increases, which decreases the amount of the sum of the nitrogen gas and the hydrogen gas generated by the thermal decomposition reaction.
  • the left side represents the furnace introduction gas (ammonia gas only)
  • the right side represents the in-furnace atmospheric gases (gas composition) including a part of the ammonia gas remained without being thermally decomposed, and the nitrogen gas and the hydrogen gas generated in the ratio of 1:3 by the thermal decomposition of the ammonia gas. Therefore, when the hydrogen concentration in the furnace is measured by means of a hydrogen sensor, 1.5s/(1+s) on the right side corresponds to the measured value of the hydrogen sensor, and thus the degree of the thermal decompositions of the ammonia gas introduced into the furnace can be calculated from the measured value. Thereby, the ammonia concentration in the furnace corresponding to (1 ⁇ s)/(1+s) on the right side can also be calculated. That is to say. the in-furnace hydrogen concentration and the in-furnace ammonia concentration can be known only from the measured value of the hydrogen sensor. Thus, the nitriding potential can be calculated.
  • the right side represents the in-furnace atmospheric gases (gas composition) including a part of the ammonia gas remained without being thermally decomposed, the nitrogen gas and the hydrogen gas generated in the ratio of 1:3 by the thermal decomposition of the ammonia gas, and the nitrogen gas remained as introduced on the left side (without being decomposed in the furnace).
  • gas composition gas composition
  • the degree of the thermal decomposition s of the ammonia gas introduced into the furnace can be calculated from the measured value of the hydrogen sensor.
  • the ammonia concentration in the furnace can also be calculated.
  • the nitriding potential can be calculated.
  • the in-furnace hydrogen concentration and the in-furnace ammonia concentration include two variables, i.e., the degree of the thermal decompositions of the ammonia gas introduced into the furnace and the introduction ratio x of the ammonia gas.
  • a mass flow controller MFC
  • the introduction ratio x of the ammonia gas can be continuously read out as a digital signal based on flow rate values of the respective gases. Therefore, the nitriding potential can be calculated based on the formula (5) by combining this introduction ratio x and the measured value of the hydrogen sensor.
  • the carbon supply source is a carbon monoxide gas.
  • the carbon monoxide gas may be directly introduced into the processing furnace, or may be generated in the processing furnace from a carbon dioxide gas.
  • an equilibrium reaction represented by the following formula (8) is established.
  • an amount of hydrogen (whose mole ratio is represented by w) consumed by the reactions represented by the formulas (8) and (9) is correlated to an amount of oxygen in the processing furnace.
  • the amount of hydrogen w consumed by those reactions corresponds to the value of pH 2 O. Therefore, it is possible to obtain the value of w, and thus in turn it is possible to obtain the degree of the thermal decompositions of the ammonia gas.
  • Patent Document 1 JP-A-2016-211069.
  • the present inventor has repeated diligent examination and various experiments about the gas nitrocarburizing treatment in which a plurality of furnace introduction gases including an ammonia gas and an ammonia decomposition gas are introduced into a processing furnace.
  • a control of nitriding potential which is sufficient for practical use can be achieved by changing an introduction amount of each of the plurality of furnace introduction gases except for the ammonia decomposition gas while keeping an introduction amount of the ammonia decomposition gas constant. as a control for bringing the nitriding potential in the processing furnace close to the target nitriding potential.
  • the present invention has been made based on the above findings. It is an object of the present invention to provide a surface hardening treatment device and a surface hardening treatment method which are capable of achieving a control of nitriding potential which is sufficient for practical use, in a gas nitrocarburizing treatment in which a plurality of furnace introduction gases including an ammonia gas and an ammonia decomposition gas are introduced into a processing furnace.
  • the present invention is a surface hardening treatment device for performing a gas nitrocarburizing treatment as a surface hardening treatment for a work arranged in a processing furnace by introducing a plurality of furnace introduction gases including an ammonia gas and an ammonia decomposition gas
  • the surface hardening treatment device including: an in-furnace atmospheric gas concentration detector configured to detect a hydrogen concentration or an ammonia concentration in the processing furnace; an in-furnace nitriding potential calculator configured to calculate a nitriding potential in the processing furnace based on the hydrogen concentration or the ammonia concentration detected by the in-furnace atmospheric gas concentration detector; and a gas-introduction-amount controller configured to change an introduction amount of each of the plurality of furnace introduction gases except for the ammonia decomposition gas while keeping an introduction amount of the ammonia decomposition gas constant, based on the nitriding potential in the processing furnace calculated by the in-furnace nitriding potential calculator and a target nitriding potential,
  • a control of nitriding potential of a relatively wider range (in particular, a control of nitriding potential which is relatively lower) can be achieved by changing the introduction amount of each of the plurality of furnace introduction gases except for the ammonia decomposition gas while keeping the introduction amount of the ammonia decomposition gas constant.
  • the introduction amount of the ammonia decomposition gas which is to be kept constant, has been predetermined in advance by conducting a preliminary experiment before an actual operation. This is because, in fact, the degree of the thermal decomposition of the ammonia gas may be also influenced by in-furnace environment of the furnace to be used or the like.
  • the surface hardening treatment device of the present invention further includes: an in-furnace oxygen concentration detector configured to detect an oxygen concentration in the processing furnace, wherein the in-furnace nitriding potential calculator is configured to calculate the nitriding potential in the processing furnace based on the hydrogen concentration or the ammonia concentration detected by the in-furnace atmospheric gas concentration detector and the oxygen concentration detected by the in-furnace oxygen concentration detector.
  • an in-furnace oxygen concentration detector configured to detect an oxygen concentration in the processing furnace
  • the in-furnace nitriding potential calculator is configured to calculate the nitriding potential in the processing furnace based on the hydrogen concentration or the ammonia concentration detected by the in-furnace atmospheric gas concentration detector and the oxygen concentration detected by the in-furnace oxygen concentration detector.
  • nitriding potential can be achieved by detecting the oxygen concentration in the processing furnace by the in-furnace oxygen concentration detector and using the oxygen concentration for calculating the nitriding potential in the processing furnace.
  • * * * * . cN cN ⁇ (A+x ⁇ B) wherein the introduction amount of the ammonia gas is represented by A, the introduction amount of the ammonia decomposition gas is represented by B, and a predetermined constant is represented by x.
  • the value is explained as a factor for converting the introduction amount of the ammonia decomposition gas B into the introduction amount of the ammonia gas A with regard to the amount of hydrogen.
  • the value of x does not have to be strictly 0.5. If the value of x is roughly within a range of 0.4 to 0.6, a control of nitriding potential which is sufficient for practical use can be achieved.
  • the plurality of furnace introduction gases includes a carbon dioxide gas as a carburizing gas.
  • the plurality of furnace introduction gases includes a carbon monoxide gas as a carburizing gas.
  • the plurality of furnace introduction gases includes a carbon dioxide gas and a nitrogen gas, or includes a carbon monoxide gas and a nitrogen gas.
  • the present invention can be recognized as a surface hardening treatment method. That is to say, the present invention is a surface hardening treatment method of performing a gas nitrocarburizing treatment as a surface hardening treatment for a work arranged in a processing furnace by introducing a plurality of furnace introduction gases including an ammonia gas and an ammonia decomposition gas, the surface hardening treatment method including: an in-furnace atmospheric gas concentration detecting step of detecting a hydrogen concentration or an ammonia concentration in the processing furnace: an in-furnace nitriding potential calculating step of calculating a nitriding potential in the processing furnace based on the hydrogen concentration or the ammonia concentration detected at the in-furnace atmospheric gas concentration detecting step:and a gas-introduction-amount controlling step of changing an introduction amount of each of the plurality of furnace introduction gases except for the ammonia decomposition gas while keeping an introduction amount of the ammonia decomposition gas constant, based on the nitriding potential in the
  • the present invention is a surface hardening treatment device for performing a gas nitrocarburizing treatment as a surface hardening treatment for a work arranged in a processing furnace by introducing a plurality of furnace introduction gases including an ammonia gas, an ammonia decomposition gas and a carburizing gas
  • the surface hardening treatment device including: an in-furnace atmospheric gas concentration detector configured to detect a hydrogen concentration or an ammonia concentration in the processing furnace; an in-furnace nitriding potential calculator configured to calculate a nitriding potential in the processing furnace based on the hydrogen concentration or the ammonia concentration detected by the in-furnace atmospheric gas concentration detector:and a gas-introduction-amount controller configured to change an introduction amount of each of the ammonia gas and the carburizing gas while keeping an introduction amount of the ammonia decomposition gas constant, based on the nitriding potential in the processing furnace calculated by the in-furnace nitriding potential calculator and a target nitriding
  • the feature of the above invention is to change the introduction amount of each of the ammonia gas and the carburizing gas while keeping the introduction amount of the ammonia decomposition gas constant, while an introduction amount of each of the rest of the plurality of furnace introduction gases is not conditioned. Accordingly, the scope of the above invention can clearly cover any manner in which a certain minute amount of gas (whose flow ratio is about 1% or less) is introduced to an extent that it does not substantially involve the reactions.
  • the above invention is applicable, in which an introduction amount of the main carburizing gas may be changed and an introduction amount of the other carburizing gas minutely introduced may be constant, according to which a control of nitriding potential of a relatively wider range (in particular, a control of nitriding potential which is relatively lower) can be achieved.
  • the present invention is a surface hardening treatment device for performing a gas nitrocarburizing treatment as a surface hardening treatment for a work arranged in a processing furnace by introducing a plurality of furnace introduction gases including an ammonia gas, an ammonia decomposition gas, a carburizing gas and a nitrogen gas
  • the surface hardening treatment device including: an in-furnace atmospheric gas concentration detector configured to detect a hydrogen concentration or an ammonia concentration in the processing furnace: an in-furnace nitriding potential calculator configured to calculate a nitriding potential in the processing furnace based on the hydrogen concentration or the ammonia concentration detected by the in-furnace atmospheric gas concentration detector:and a gas-introduction-amount controller configured to change an introduction amount of each of the ammonia gas, the carburizing gas and the nitrogen gas while keeping an introduction amount of the ammonia decomposition gas constant, based on the nitriding potential in the processing furnace calculated by the in-furnace nitriding potential calculator
  • the feature of the above invention is to change the introduction amount of each of the ammonia gas, the carburizing gas and the nitrogen gas while keeping the introduction amount of the ammonia decomposition gas constant, while an introduction amount of each of the rest of the plurality of furnace introduction gases is not conditioned. Accordingly, the scope of the above invention can clearly cover any manner in which a certain minute amount of gas (whose flow ratio is about 1% or less) is introduced to an extent that it does not substantially involve the reactions. For example, when two or more kinds of carburizing gases are introduced, the above invention is applicable, in which an introduction amount of the main carburizing gas may be changed and an introduction amount of the other carburizing gas minutely introduced may be constant. according to which a control of nitriding potential of a relatively wider range (in particular, a control of nitriding potential which is relatively lower) can be achieved.
  • a control of nitriding potential of a relatively wider range (in particular, a control of nitriding potential which is relatively lower) can be achieved by changing the introduction amount of each of the plurality of furnace introduction gases except for the ammonia decomposition gas while keeping the introduction amount of the ammonia decomposition gas constant.
  • FIG. 1 is a schematic view showing a surface hardening treatment device according to a first embodiment of the present invention:
  • FIG. 2 is a graph showing a control of furnace introduction gases according to an example 1-1;
  • FIG. 3 is a graph showing a control of nitriding potential according to the example 1-1:
  • FIG. 4 is a graph showing a control of furnace introduction gases according to an example 1-3;
  • FIG. 5 is a graph showing a control of nitriding potential according to the example 1-3;
  • FIG. 6 is a table comparing the examples 1-1 to 1-3 with their respective comparative examples
  • FIG. 7 is a schematic view showing a surface hardening treatment device according to a second embodiment of the present invention.
  • FIG. 8 is a graph showing a control of furnace introduction gases according to an example 2-2;
  • FIG. 9 is a graph showing a control of nitriding potential according to the example 2-2.
  • FIG. 10 is a table comparing the examples 2-1 to 2-3 with their respective comparative examples:
  • FIG. 11 is a schematic view showing a surface hardening treatment device according to a third embodiment of the present invention:
  • FIG. 12 is a graph showing a control of furnace introduction gases according to an example 3-2:
  • FIG. 13 is a graph showing a control of nitriding potential according to the example 3-2;
  • FIG. 14 is a table comparing the examples 3-1 to 3-3 with their respective comparative examples:
  • FIG. 15 is a schematic view showing a surface hardening treatment device according to a fourth embodiment of the present invention:
  • FIG. 16 is a table comparing the examples 4-1 to 4-3 with their respective comparative examples
  • FIG. 17 is a schematic view showing a surface hardening treatment device according to a fifth embodiment of the present invention:and
  • FIG. 18 is a table comparing the examples 5-1 to 5-3 with their respective comparative examples.
  • FIG. 1 is a schematic view showing a surface hardening treatment device according to an embodiment of the present invention.
  • the surface hardening treatment device 1 of the present embodiment is a surface hardening treatment device for performing a gas nitrocarburizing treatment as a surface hardening treatment for a work S arranged in a processing furnace 2 by introducing an ammonia gas, an ammonia decomposition gas and a carbon dioxide gas into the processing furnace 2 .
  • the ammonia decomposition gas is a gas called AX gas, and is a mixed gas composed of nitrogen and hydrogen in a ratio of 1:3.
  • the work S is made of metal.
  • the work S is a steel part or a mold.
  • the processing furnace 2 of the surface hardening treatment device 1 of the present embodiment includes: a stirring fan 8 , a stirring-fan drive motor 9 , a in-furnace temperature measuring device 10 , a furnace body heater 11 , an atmospheric gas concentration detector 3 , a nitriding potential adjustor 4 , a temperature adjustor 5 , a programmable logic controller 31 , a recorder 6 , and a furnace introduction gas supplier 20 .
  • the stirring fan 8 is disposed in the processing furnace 2 and configured to rotate in the processing furnace 2 in order to stir atmospheric gases in the processing furnace 2 .
  • the stirring-fan drive motor 9 is connected to the stirring fan 8 and configured to cause the stirring fan 8 to rotate at an arbitrary rotation speed.
  • the in-furnace temperature measuring device 10 includes a thermocouple and is configured to measure a temperature of the in-furnace gases existing in the processing furnace 2 . In addition, after measuring the temperature of the in-furnace gases, the in-furnace temperature measuring device 10 is configured to output an information signal including the measured temperature (in-furnace temperature signal) to the temperature adjustor 5 and the recorder 6 .
  • the atmospheric gas concentration detector 3 is composed of: a sensor capable of detecting a hydrogen concentration or an ammonia concentration in the processing furnace 2 as an in-furnace atmospheric gas concentration; and an oxygen sensor capable of detecting an oxygen concentration in the processing furnace 2 as an in-furnace oxygen concentration.
  • a main body of each of the above sensors communicates with an inside of the processing furnace 2 via an atmospheric gas pipe 12 .
  • the atmospheric gas pipe 12 is formed as a single-line path that directly communicates the sensors' main bodies of the atmospheric gas concentration detector 3 and the processing furnace 2 .
  • An on-off valve 17 is provided in the middle of the atmospheric gas pipe 12 . and configured to be controlled by an on-off valve controller 16 .
  • the atmospheric gas concentration detector 3 is configured to output an information signal including the detected concentrations to the nitriding potential adjustor 4 and the recorder 6 .
  • the recorder 6 includes a CPU and a storage medium such as a memory. Based on the signals outputted from the in-furnace temperature measurement device 10 and the atmospheric gas concentration detector 3 , the recorder 6 is configured to record the temperature and/or the atmospheric gas concentration and the oxygen concentration in the processing furnace 2 , for example in correspondence with the date and time when the surface hardening treatment is performed.
  • the nitriding potential adjuster 4 includes an in-furnace nitriding potential calculator 13 and a gas flow rate output adjustor 30 .
  • the programmable logic controller 31 includes a gas introduction controller 14 and a parameter setting device 15 .
  • the in-furnace nitriding potential calculator 13 is configured to calculate a nitriding potential in the processing furnace 2 based on the hydrogen concentration or the ammonia concentration and the oxygen concentration detected by the atmospheric gas concentration detector 3 .
  • calculation formulas for the nitriding potential are programmed dependent on the actual furnace introduction gases in accordance with the same theory as the above formulas (5) to (9), and incorporated in the in-furnace nitriding potential calculator 13 , so that the nitriding potential is calculated from the value of the in-furnace atmospheric gas concentration and the value of the oxygen concentration.
  • the parameter setting device 15 is composed of a touch panel, for example. Through the parameter setting device 15 , the target nitriding potential, the processing temperature, the processing time, the introduction amount of the ammonia decomposition gas, the predetermined constant x, the factor of proportionality c1, and so on can be set and inputted for the same work. In addition, through the parameter setting device 15 , setting parameter values for a PID control method can be set and inputted for each different value of the target nitriding potential. Specifically, “a proportional gain”, “an integral gain or an integration time”, and “a differential gain or a differentiation time” for the PID control method can be set and inputted for each different value of the target nitriding potential. The set and inputted setting parameter values are transferred to the gas flow rate output adjustor 30 .
  • the gas flow rate output adjustor 30 is configured to perform the PID control method in which respective gas introduction amounts of the ammonia gas and the carbon dioxide gas among the three kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value. More specifically, in the present PID control method, the nitriding potential in the processing furnace 2 is brought close to the target nitriding potential by changing the introduction amount of the ammonia gas and the introduction amount of the carbon dioxide gas while keeping the introduction amount of the ammonia decomposition gas constant. In addition, in the present PID control method, the setting parameter values that have been transferred from the parameter setting device 15 are used.
  • a state of the processing furnace a state of a furnace wall and/or a jig
  • a temperature condition of the processing furnace and (3) a state of the work (type and/or the number of parts) are the same, it is possible to obtain in advance candidate values for the setting parameter values (4) for each different value of the target nitriding potential, by an auto-tuning function that the nitriding potential adjustor 4 has in itself.
  • a “UT75A” manufactured by Yokogawa Electric Co., Ltd. (a high-functional digital indicating controller, http://www.yokogawa.co.jp/ns/cis/utup/utadvanced/ns-ut75a-01-ja.htm) or the like can be used.
  • the setting parameter values (a set of “the proportional gain”, “the integral gain or the integration time” and “the derivative gain or the derivative time”) obtained as the candidate values can be recorded in some manner, and then can be manually inputted to the parameter setting device 15 .
  • the setting parameter values obtained as the candidate values can be stored in some storage device in a manner associated with the target nitriding potential, and then can be automatically read out by the parameter setting device 15 based on the set and inputted value of the target nitriding potential.
  • the gas flow rate output adjustor 30 is configured to determine an introduction amount of the ammonia decomposition gas, which is kept constant, and respective initial introduction amounts of the ammonia gas and of the carbon dioxide gas, which are subsequently changed. It is preferable to perform pilot processes to obtain in advance candidate values for these introduction amounts, so that the obtained values can be automatically read out by the parameter setting device 15 from some storage device or can be manually inputted to the parameter setting device 15 .
  • the output values from the gas flow rate output adjustor 30 are transferred to the gas introduction amount controller 14 .
  • the gas introduction amount controller 14 is configured to transmit a control signal to a first supply amount controller 22 for the ammonia gas.
  • the furnace introduction gas supplier 20 of the present embodiment includes a first furnace introduction gas supplier 21 for the ammonia gas, the first supply amount controller 22 , a first supply valve 23 and a first flow meter 24 .
  • the furnace introduction gas supplier 20 of the present embodiment includes a second furnace introduction gas supplier 25 for the ammonia decomposition gas (AX gas), a second supply amount controller 26 , a second supply valve 27 and a second flow meter 28 .
  • the furnace introduction gas supplier 20 of the present embodiment includes a third furnace introduction gas supplier 61 for the carbon dioxide gas, a third supply amount controller 62 , a third supply valve 63 and a third flow meter 64 .
  • the ammonia gas, the ammonia decomposition gas and the carbon dioxide gas are mixed in a furnace introduction gas pipe 29 before entering the processing furnace 2 .
  • the first furnace introduction gas supplier 21 is formed by, for example, a tank filled with a first furnace introduction gas (in this example, the ammonia gas).
  • the first supply amount controller 22 is formed by a mass flow controller (which can finely change a flow rate within a short time period), and is interposed between the first furnace introduction gas supplier 21 and the first supply valve 23 .
  • An opening degree of the first supply amount controller 22 changes according to the control signal outputted from the gas introduction amount controller 14 .
  • the first supply amount controller 22 is configured to detect a supply amount from the first furnace introduction gas supplier 21 to the first supply valve 23 , and output an information signal including the detected supply amount to the gas introduction amount controller 14 and the recorder 6 . This information signal can be used for correction or the like of the control performed by the gas introduction amount controller 14 .
  • the first supply valve 23 is formed by an electromagnetic valve configured to switch between opened and closed states according to a control signal outputted from the gas introduction amount controller 14 , and is interposed between the first supply amount controller 22 and the first flow meter 24 .
  • the first flow meter 24 is formed by, for example, a mechanical flow meter such as a flow-type flow meter, and is interposed between the first supply valve 23 and the furnace introduction gas pipe 29 .
  • the first flow meter 24 detects a supply amount from the first supply valve 23 to the furnace introduction gas pipe 29 .
  • the supply amount detected by the first flow meter 24 can be provided for an operators visual confirmation.
  • the second furnace introduction gas supplier 25 is formed by, for example, a tank filled with a second furnace introduction gas (in this example, the ammonia decomposition gas).
  • the second supply amount controller 26 is formed by a mass flow controller (which can finely change a flow rate within a short time period), and is interposed between the second furnace introduction gas supplier 25 and the second supply valve 27 .
  • An opening degree of the second supply amount controller 26 changes according to the control signal outputted from the gas introduction amount controller 14 .
  • the second supply amount controller 26 is configured to detect a supply amount from the second furnace introduction gas supplier 25 to the second supply valve 27 , and output an information signal including the detected supply amount to the gas introduction amount controller 14 and the recorder 6 . This information signal can be used for correction or the like of the control performed by the gas introduction amount controller 14 .
  • the second supply valve 27 is formed by an electromagnetic valve configured to switch between opened and closed states according to a control signal outputted from the gas introduction amount controller 14 , and is interposed between the second supply amount controller 26 and the second flow meter 28 .
  • the second flow meter 28 is formed by, for example, a mechanical flow meter such as a flow-type flow meter, and is interposed between the second supply valve 27 and the furnace introduction gas pipe 29 .
  • the second flow meter 28 detects a supply amount from the second supply valve 27 to the furnace introduction gas pipe 29 .
  • the supply amount detected by the second flow meter 28 can be provided for an operator's visual confirmation.
  • the introduction amount of the ammonia decomposition gas is not changed finely.
  • the second supply amount controller 26 may be omitted, and a flow rate (an opening degree) of the second flow meter 28 may be manually adjusted correspondingly to the control signal outputted from the gas introduction amount controller 14 .
  • the third furnace introduction gas supplier 61 is formed by, for example, a tank filled with a third furnace introduction gas (in this example, the carbon dioxide gas).
  • the third supply amount controller 62 is formed by a mass flow controller (which can finely change a flow rate within a short time period), and is interposed between the third furnace introduction gas supplier 61 and the third supply valve 63 .
  • An opening degree of the third supply amount controller 62 changes according to the control signal outputted from the gas introduction amount controller 14 .
  • the third supply amount controller 62 is configured to detect a supply amount from the third furnace introduction gas supplier 61 to the third supply valve 63 , and output an information signal including the detected supply amount to the gas introduction amount controller 14 and the recorder 6 . This information signal can be used for correction or the like of the control performed by the gas introduction amount controller 14 .
  • the third supply valve 63 is formed by an electromagnetic valve configured to switch between opened and closed states according to a control signal outputted from the gas introduction amount controller 14 , and is interposed between the third supply amount controller 62 and the third flow meter 64 .
  • the third flow meter 64 is formed by, for example, a mechanical flow meter such as a flow-type flow meter, and is interposed between the third supply valve 63 and the furnace introduction gas pipe 29 .
  • the third flow meter 64 detects a supply amount from the third supply valve 63 to the furnace introduction gas pipe 29 .
  • the supply amount detected by the third flow meter 64 can be provided for an operator's visual confirmation.
  • a work S to be processed is put into the processing furnace 2 , and then the processing furnace 2 starts to be heated.
  • a pit furnace having a size of ⁇ 700 ⁇ 1000 was used as the processing furnace 2
  • 570° C. was adopted as the temperature to be heated
  • a steel material having a surface area of 4 m 2 was used as the work S.
  • the ammonia gas, the ammonia decomposition gas and the carbon dioxide gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 13 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 19 [l/min]
  • the initial introduction amount of the carbon dioxide gas was set to 1.03 [l/min]
  • These initial introduction amounts can be set and inputted by the parameter setting device 15 .
  • the stirring fan drive motor 9 is driven and thus the stirring fan 8 rotates to stir the atmospheric gases in the processing furnace 2 .
  • the on-off valve controller 16 closes the on-off valve 17 .
  • a treatment for activating a steel surface to make it easy for nitrogen to enter may be performed.
  • a hydrogen chloride gas and/or a hydrogen cyanide gas or the like may be generated in the furnace. These gases may deteriorate the atmospheric gas concentration detector (sensors) 3 , and thus it is effective to keep the on-off valve 17 closed.
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs art information in signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (0.6 in this example: see FIG. 3 ) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the so atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas and the carbon dioxide gas among the three kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas and the introduction amount of the carbon dioxide gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant) and the third supply amount controller 62 for the carbon dioxide gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.6) with extremely high precision since a timing of about 30 minutes after starting the treatment.
  • recording of the respective gas introduction amounts and the nitriding potential was stopped at a timing of about 190 minutes after starting the treatment.
  • an example 1-2 in which the surface hardening treatment device 1 according to the present embodiment is used and the target nitriding potential is set to 0.4.
  • a pit furnace having a size of ⁇ 700 ⁇ 1000 was used as the processing furnace 2 , 570° C. was adopted as the temperature to be heated, and a steel material having a surface area of 4 m 2 was used as the work S.
  • the ammonia gas, the ammonia decomposition gas and the carbon dioxide gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 5.5 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 25 [l/min]
  • the initial introduction amount of the carbon dioxide gas was set to 0.95 [l/min]
  • These initial introduction amounts can be set and inputted by the parameter setting device 15 .
  • the stirring fan drive motor 9 is driven and thus the stirring fan 8 rotates to stir the atmospheric gases in the processing furnace 2 .
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (0.4 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 ,
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas and the carbon dioxide gas among the three kinds of furnace introduction gases are input values, the nitriding potential calculated in by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas and the introduction amount of the carbon dioxide gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant) and the third supply amount controller 62 for the carbon dioxide gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.4) with extremely high precision since a timing of about 30 minutes after starting the treatment.
  • an example 1-3 in which the surface hardening treatment device 1 according to the present embodiment is used and the target nitriding potential is set to 0.2.
  • a pit furnace having a size of ⁇ 700 ⁇ 1000 was used as the processing furnace 2 , 570° C. was adopted as the temperature to be heated, and a steel material having a surface area of 4 m 2 was used as the work S.
  • the ammonia gas, the ammonia decomposition gas and the carbon dioxide gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 2 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 29 [l/min]
  • the initial introduction amount of the carbon dioxide gas was set to 0.87 [l/min]
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (0.2 in this example: see FIG. 5 ) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas and the carbon dioxide gas among the three kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas and the introduction amount of the carbon dioxide gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant) and the third supply amount controller 62 for the carbon dioxide gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.2) with extremely high precision since a timing of about 30 minutes after starting the treatment.
  • recording of the respective gas introduction amounts and the nitriding potential was stopped at a timing of about 160 minutes after starting the treatment.
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculated the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performed the PID control method in which the respective gas introduction amounts of the ammonia gas and the carbon dioxide gas were input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 was an output value, and the target nitriding potential (the set nitriding potential) was a target value.
  • the nitriding potential in the processing furnace 2 was brought close to the target nitriding potential, by changing the total introduction amount of the ammonia gas and the carbon dioxide gas while keeping the ratio of the introduction amounts of the ammonia gas and the carbon dioxide gas constant.
  • the nitriding potential could not be stably controlled.
  • FIG. 6 A table of the above results is shown as FIG. 6 .
  • a third furnace introduction gas supplier 61 ′ is formed by a tank filled with not a carbon dioxide gas but a carbon monoxide gas.
  • the other structure of the second embodiment is substantially the same as that of the first embodiment explained with reference to FIG. 1 .
  • FIG. 7 the same parts as those of the first embodiment are shown by the same reference numerals, and detailed explanation thereof is omitted.
  • the ammonia gas, the ammonia decomposition gas and the carbon monoxide gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 5.5 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 19 [l/min]
  • the initial introduction amount of the carbon monoxide gas was set to 0.2 [l/min]
  • These initial introduction amounts can be set and inputted by the parameter setting device 15 .
  • the stirring fan drive motor 9 is driven and thus the stirring fan 8 rotates to stir the atmospheric gases in the processing furnace 2 .
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (0.6 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas and the carbon monoxide gas among the three kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas and the introduction amount of the carbon monoxide gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant) and the third supply amount controller 62 for the carbon monoxide gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.6) with extremely high precision since a timing of about 20 minutes after starting the treatment.
  • an example 2-2 in which the surface hardening treatment device according to the second embodiment is used and the target nitriding potential is set to 0.4.
  • a pit furnace having a size of ⁇ 700 ⁇ 1000 was used as the processing furnace 2 , 570° C. was adopted as the temperature to be heated, and a steel material having a surface area of 4 m 2 was used as the work S.
  • the ammonia gas, the ammonia decomposition gas and the carbon monoxide gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 3 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 25 [l/min]
  • the initial introduction amount of the carbon monoxide gas was set to 0.15 [l/min].
  • c1 0.01 was set.
  • These initial introduction amounts can be set and inputted by the parameter setting device 15 .
  • the stirring fan drive motor 9 is driven and thus the stirring fan 8 rotates to stir the atmospheric gases in the processing furnace 2 .
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 so and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (0.4 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas and the carbon monoxide gas among the three kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas and the introduction amount of the carbon monoxide gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.4) with extremely high precision since a timing of about 20 minutes after starting the treatment.
  • the ammonia gas, the ammonia decomposition gas and the carbon monoxide gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 1 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 29 [l/min]
  • the initial introduction amount of the carbon monoxide gas was set to 0.15 [l/min].
  • c1 0.01 was set.
  • These initial introduction amounts can be set and inputted by the parameter setting device 15 .
  • the stirring fan drive motor 9 is driven and thus the stirring fan 8 rotates to stir the atmospheric gases in the processing furnace 2 .
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (0.3 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas and the carbon monoxide gas among the three kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas and the introduction amount of the carbon monoxide gas as a result of the PID control method.
  • the gas in introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant) and the third supply amount controller 62 for the carbon monoxide gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.2) with extremely high precision since a timing of about 30 minutes after starting the treatment.
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculated the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performed the PID control method in which the respective gas introduction amounts of the ammonia gas and the carbon monoxide gas were input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 was an output value, and the target nitriding potential (the set nitriding potential) was a target value.
  • the nitriding potential in the processing furnace 2 was brought close to the target nitriding potential, by changing the total introduction amount of the ammonia gas and the carbon monoxide gas while keeping the ratio of the introduction amounts of the ammonia gas and the carbon monoxide gas constant.
  • the nitriding potential could not be stably controlled.
  • FIG. 10 A table of the above results is shown as FIG. 10 .
  • a furnace introduction gas supplier 20 ′ of a third embodiment further includes a fourth furnace introduction gas supplier 71 for nitrogen gas, a fourth supply amount controller 72 , a fourth supply valve 73 and a fourth flow meter 74 .
  • the fourth furnace introduction gas supplier 71 is formed by, for example, a tank filled with a fourth furnace introduction gas (in this example, nitrogen gas).
  • the fourth supply amount controller 72 is formed by a mass flow controller (which can finely change a flow rate within a short time period), and is interposed between the fourth furnace introduction gas supplier 71 and the fourth supply valve 73 .
  • An opening degree of the fourth supply amount controller 72 changes according to the control signal outputted from the gas introduction amount controller 14 .
  • the fourth supply amount controller 72 is configured to detect a supply amount from the fourth furnace introduction gas supplier 71 to the fourth supply valve 73 , and output an information signal including the detected supply amount to the gas introduction amount controller 14 and the recorder 6 . This information signal can be used for correction or the like of the control performed by the gas introduction amount controller 14 .
  • the fourth supply valve 73 is formed by an electromagnetic valve configured to switch between opened and closed states according to a control signal outputted from the gas introduction amount controller 14 , and is interposed between the fourth supply amount controller 72 and the fourth flow meter 74 .
  • the fourth flow meter 74 is formed by, for example, a mechanical flow meter such as a flow-type flow meter, and is interposed between the fourth supply valve 73 and the furnace introduction gas pipe 29 .
  • the fourth flow meter 74 detects a supply amount from the fourth supply valve 73 to the furnace introduction gas pipe 29 .
  • the supply amount detected by the fourth flow meter 74 can be provided for an operator's visual confirmation.
  • the other structure of the third embodiment is substantially the same as that of the first embodiment explained with reference to FIG. 1 .
  • FIG. 11 the same parts as those of the first embodiment are shown by the same reference numerals, and detailed explanation thereof is omitted.
  • the ammonia gas, the ammonia decomposition gas, the carbon dioxide gas and the nitrogen gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 ′ according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 13 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 19 [l/min]
  • the initial introduction amount of the carbon dioxide gas was set to 2.2 [l/min]
  • the initial introduction amount of the nitrogen gas was set to 20 [l/min]
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (1.0 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the Pill control method in which the respective gas introduction amounts of the ammonia gas, the carbon dioxide gas and the nitrogen gas among the four kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas, the introduction amount of the carbon dioxide gas and the introduction amount of the nitrogen gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant), the third supply amount controller 62 for the carbon dioxide gas and the fourth supply amount controller 72 for the nitrogen gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (1.0) with extremely high precision since a timing of about 20 minutes after starting the treatment.
  • an example 3-2 in which the surface hardening treatment device according to the third embodiment is used and the target nitriding potential is set to 0.6.
  • a pit furnace having a size of ⁇ 700 ⁇ 1000 was used as the processing furnace 2 , 570° C. was adopted as the temperature to be heated, and a steel material having a surface area of 4 m 2 was used as the work S.
  • the ammonia gas, the ammonia decomposition gas, the carbon dioxide gas and the nitrogen gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 ′ according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 8 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 25 [l/min]
  • the initial introduction amount of the carbon dioxide gas was set to 2 [l/min]
  • the initial introduction amount of the nitrogen gas was set to 18.5 [l/min]
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (0.6 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PO control method in which the respective gas introduction amounts of the ammonia gas, the carbon dioxide gas and the nitrogen gas among the four kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas, the introduction amount of the carbon dioxide gas and the introduction amount of the nitrogen gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant), the third supply amount controller 62 for the carbon dioxide gas and the fourth supply amount controller 72 for the nitrogen gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.6) with extremely high precision since a timing of about 30 minutes after starting the treatment.
  • the ammonia gas, the ammonia decomposition gas, the carbon dioxide gas and the nitrogen gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 ′ according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 3 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 29 [l/min]
  • the initial introduction amount of the carbon dioxide gas was set to 1.8 [l/min]
  • the initial introduction amount of the nitrogen gas was set to 15.8 [l/min]
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (0.2 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas, the carbon dioxide gas and the nitrogen gas among the four kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas, the introduction amount of the carbon dioxide gas and the introduction amount of the nitrogen gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant), the third supply amount controller 62 for the carbon dioxide gas and the fourth supply amount controller 72 for the nitrogen gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.2) with extremely high precision since a timing of about 40 minutes after starting the treatment.
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculated the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performed the PID control method in which the respective gas introduction amounts of the ammonia gas, the nitrogen gas and the carbon dioxide gas were input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 was an output value, and the target nitriding potential (the set nitriding potential) was a target value.
  • the nitriding potential in the processing furnace 2 was brought close to the target nitriding potential, by changing the total introduction amount of the ammonia gas, the nitrogen gas and the carbon dioxide gas while keeping the ratio of the introduction amounts of the ammonia gas, the nitrogen gas and the carbon dioxide gas constant.
  • the nitriding potential could not be stably controlled.
  • FIG. 14 A table of the above results is shown as FIG. 14 .
  • a third furnace introduction gas supplier 61 ′ is formed by a tank filled with not a carbon dioxide gas but a carbon monoxide gas.
  • the other structure of the fourth embodiment is substantially the same as that of the third embodiment explained with reference to FIG. 11 .
  • FIG. 15 the same parts as those of the third embodiment are shown by the same reference numerals, and detailed explanation thereof is omitted.
  • the ammonia gas, the ammonia decomposition gas, the carbon monoxide gas and the nitrogen gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 ′ according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 13 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 19 [l/min]
  • the initial introduction amount of the carbon monoxide gas was set to 0.9 [l/min]
  • the initial introduction amount of the nitrogen gas was set to 20 [l/min]
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (1.0 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas, the carbon monoxide gas and the nitrogen gas among the four kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas, the introduction amount of the carbon monoxide gas and the introduction amount of the nitrogen gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant), the third supply amount controller 62 for the carbon monoxide gas and the fourth supply amount controller 72 for the nitrogen gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (1.0) with extremely high precision since a timing of about 30 minutes after starting the treatment.
  • the ammonia gas, the ammonia decomposition gas, the carbon monoxide gas and the nitrogen gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 ′ according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 8 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 25 [l/min]
  • the initial introduction amount of the carbon monoxide gas was set to 0.8 [l/min]
  • the initial introduction amount of the nitrogen gas was set to 19.7 [l/min]
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (0.6 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas, the carbon monoxide gas and the nitrogen gas among the four kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas, the introduction amount of the carbon monoxide gas and the introduction amount of the nitrogen gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant), the third supply amount controller 62 for the carbon monoxide gas and the fourth supply amount controller 72 for the nitrogen gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.6) with extremely high precision since a timing of about 40 minutes after starting the treatment.
  • an example 4-3 in which the surface hardening treatment device according to the fourth embodiment is used and the target nitriding potential is set to 0.2.
  • a pit furnace having a size of ⁇ 700 ⁇ 1000 was used as the processing furnace 2 , 570° C. was adopted as the temperature to be heated, and a steel material having a surface area of 4 m 2 was used as the work S.
  • the ammonia gas, the ammonia decomposition gas, the carbon monoxide gas and the nitrogen gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 ′ according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 3 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 29 [l/min]
  • the initial introduction amount of the carbon monoxide gas was set to 0.7 [l/min]
  • the initial introduction amount of the nitrogen gas was set to 16 [l/min]
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (0.2 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas, the carbon monoxide gas and the nitrogen gas among the four kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas, the introduction amount of the carbon monoxide gas and the introduction amount of the nitrogen gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant), the third supply amount controller 62 for the carbon monoxide gas and the fourth supply amount controller 72 for the nitrogen gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.2) with extremely high precision since a timing of about 40 minutes after starting the treatment.
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculated the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal.
  • the gas flow rate output adjustor 30 performed the PID control method in which the respective gas introduction amounts of the ammonia gas, the nitrogen gas and the carbon monoxide gas were input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 was an output value, and the target nitriding potential (the set nitriding potential) was a target value, More specifically, in the present PID control method, the nitriding potential in the processing furnace 2 was brought close to the target nitriding potential, by changing the total introduction amount of the ammonia gas, the nitrogen gas and the carbon monoxide gas while keeping the ratio of the introduction amounts of the ammonia gas, the nitrogen gas and the carbon monoxide gas constant. However, in the above comparative examples, the nitriding potential could not be stably controlled.
  • FIG. 16 A table of the above results is shown as FIG. 16 .
  • a furnace introduction gas supplier 20 ′′ of a fifth embodiment further includes a fifth furnace introduction gas supplier 81 for carbon dioxide gas, a fifth supply amount controller 82 , a fifth supply valve 83 and a fifth flow meter 84 , in addition to the furnace introduction gas supplier 20 ′ of the fourth embodiment.
  • the fifth furnace introduction gas supplier 81 is formed by, for example, a tank filled with a fifth furnace introduction gas (in this example, carbon dioxide gas).
  • a fifth furnace introduction gas in this example, carbon dioxide gas
  • the fifth supply amount controller 82 is formed by a mass flow controller (which can finely change a flow rate within a short time period), and is interposed between the fifth furnace introduction gas supplier 81 and the fifth supply valve 83 .
  • An opening degree of the fifth supply amount controller 82 changes according to the control signal outputted from the gas introduction amount controller 14 .
  • the fifth supply amount controller 82 is configured to detect a supply amount from the fifth furnace introduction gas supplier 81 to the fifth supply valve 83 , and output an information signal including the detected supply amount to the gas introduction amount controller 14 and the recorder 6 . This information signal can be used for correction or the like of the control performed by the gas introduction amount controller 14 .
  • the fifth supply valve 83 is formed by an electromagnetic valve configured to switch between opened and closed states according to a control signal outputted from the gas introduction amount controller 14 , and is interposed between the fifth supply amount controller 82 and the fifth flow meter 84 .
  • the fifth flow meter 84 is formed by, for example, a mechanical flow meter such as a flow-type flow meter, and is interposed between the fifth supply valve 83 and the furnace introduction gas pipe 29 .
  • the fifth flow meter 84 detects a supply amount from the fifth supply valve 83 to the furnace introduction gas pipe 29 , The supply amount detected by the fifth flow meter 84 can be provided for an operator's visual confirmation.
  • the other structure of the fifth embodiment is substantially the same as that of the fourth embodiment explained with reference to FIG. 15 .
  • FIG. 17 the same parts as those of the fourth embodiment are shown by the same reference numerals, and detailed explanation thereof is omitted.
  • the ammonia gas, the ammonia decomposition gas, the carbon monoxide gas, the nitrogen gas and the carbon dioxide gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 ′′ according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 13 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 19 [l/min]
  • the initial introduction amount of the carbon monoxide gas was set to 0.45 [l/min]
  • the initial introduction amount of the nitrogen gas was set to 21 [l/min]
  • the initial introduction amount of the carbon dioxide gas was set to 0.9 [l/min]
  • c3 0.04.
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (1.0 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas, the carbon monoxide gas, the nitrogen gas and the carbon dioxide gas among the five kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas, the introduction amount of the carbon monoxide gas, the introduction amount of the nitrogen gas and the introduction amount of the carbon dioxide gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant), the third supply amount controller 62 for the carbon monoxide gas, the fourth supply amount controller 72 for the nitrogen gas and the fifth supply amount controller 82 for the carbon dioxide gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (1.0) with extremely high precision since a timing of about 30 minutes after starting the treatment.
  • an example 5-2 in which the surface hardening treatment device according to the fifth embodiment is used and the target nitriding potential is set to 0.6.
  • a pit furnace having a size of ⁇ 700 ⁇ 1000 was used as the processing furnace 2 , 570° C. was adopted as the temperature to be heated, and a steel material having a surface area of 4 m 2 was used as the work S.
  • the ammonia gas, the ammonia decomposition gas, the carbon monoxide gas, the nitrogen gas and the carbon dioxide gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 ′′ according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 12 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 25 [l/min]
  • the initial introduction amount of the carbon monoxide gas was set to 0.5 [l/min]
  • the initial introduction amount of the nitrogen gas was set to 23 [l/min]
  • the initial introduction amount of the carbon dioxide gas was set to 1.0 [l/min].
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state),
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (1.0 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PIC control method in which the respective gas introduction amounts of the ammonia gas, the carbon monoxide gas, the nitrogen gas and the carbon dioxide gas among the five kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas, the introduction amount of the carbon monoxide gas, the introduction amount of the nitrogen gas and the introduction amount of the carbon dioxide gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant), the third supply amount controller 62 for the carbon monoxide gas, the fourth supply amount controller 72 for the nitrogen gas and the fifth supply amount controller 82 for the carbon dioxide gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.6) with extremely high precision since a timing of about 40 minutes after starting the treatment.
  • the ammonia gas, the ammonia decomposition gas, the carbon monoxide gas, the nitrogen gas and the carbon dioxide gas are introduced into the processing furnace 2 from the furnace introduction gas supplier 20 ′′ according to their respective initial introduction amounts.
  • the initial introduction amount of the ammonia gas was set to 3 [l/min]
  • the initial introduction amount of the ammonia decomposition gas was set to 29 [l/min]
  • the initial introduction amount of the carbon monoxide gas was set to 0.3 [l/min]
  • the initial introduction amount of the nitrogen gas was set to 16 [l/min]
  • the initial introduction amount of the carbon dioxide gas was set to 0.6 [l/min]
  • c3 0.04.
  • These initial introduction amounts can be set and inputted by the parameter setting device 15 .
  • the stirring fan drive motor 9 is driven and thus the stirring fan 8 rotates to stir the atmospheric gases in the processing furnace 2 .
  • the on-off valve controller 16 closes the on-off valve 17 .
  • the in-furnace temperature measurement device 10 measures a temperature of the in-furnace gases, and outputs an information signal including the measured temperature to the nitriding potential adjustor 4 and the recorder 6 .
  • the nitriding potential adjustor 4 judges whether the state in the processing furnace 2 is still during the temperature rising step or already after the temperature rising step has been completed (a stable state).
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates an in-furnace nitriding potential (which is initially an extremely high value (since no hydrogen gas exists in the furnace), but decreases as decomposition of the ammonia gas (generation of the hydrogen gas) proceeds) and judges whether the calculated value has dropped lower than the sum of the target nitriding potential (1.0 in this example) and a standard margin.
  • This standard margin can also be set and inputted by the parameter setting device 15 , and is for example 0.1.
  • the nitriding potential adjustor 4 starts to control an introduction amount of each of the furnace introduction gases via the gas introduction amount controller 14 .
  • the on-off valve controller 16 opens the on-off valve 17 .
  • the processing furnace 2 and the atmospheric gas concentration detector 3 communicate with each other, and then the atmospheric gas concentration detector 3 detects an in-furnace hydrogen concentration or an in-furnace ammonia concentration, and detects an in-furnace oxygen concentration.
  • the detected hydrogen concentration signal or ammonia concentration signal and the detected oxygen concentration signal are outputted to the nitriding potential adjustor 4 and the recorder 6 .
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculates the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performs the PID control method in which the respective gas introduction amounts of the ammonia gas, the carbon monoxide gas, the nitrogen gas and the carbon dioxide gas among the five kinds of furnace introduction gases are input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 is an output value, and the target nitriding potential (the set nitriding potential) is a target value.
  • the setting parameter values that have been set and inputted by the parameter setting device 15 are used.
  • the setting parameter values may be different depending on values of the target nitriding potential.
  • the gas introduction amount controller 14 controls the introduction amount of the ammonia gas, the introduction amount of the carbon monoxide gas, the introduction amount of the nitrogen gas and the introduction amount of the carbon dioxide gas as a result of the PID control method.
  • the gas introduction amount controller 14 transmits control signals to the first supply amount controller 22 for the ammonia gas, the second supply amount controller 26 for the ammonia decomposition gas (whose flow rate is constant), the third supply amount controller 62 for the carbon monoxide gas, the fourth supply amount controller 72 for the nitrogen gas and the fifth supply amount controller 82 for the carbon dioxide gas, in order to realize the respective determined introduction amounts of the furnace introduction gases.
  • the in-furnace nitriding potential can be stably controlled in the vicinity of the target nitriding potential.
  • the surface hardening treatment of the work S can be performed with extremely high quality.
  • a feedback control is performed with a sampling rate of about several hundred milliseconds, and the introduction amount of the ammonia gas is increased and decreased within a range of about 3 ml ( ⁇ 1.5 ml), so that the nitriding potential can be controlled to the target nitriding potential (0.2) with extremely high precision since a timing of about 40 minutes after starting the treatment.
  • the in-furnace nitriding potential calculator 13 of the nitriding potential adjustor 4 calculated the in-furnace nitriding potential based on the inputted hydrogen concentration signal or ammonia concentration signal and the inputted oxygen concentration signal. Then, the gas flow rate output adjustor 30 performed the PID control method in which the respective gas introduction amounts of the ammonia gas, the nitrogen gas, the carbon monoxide gas and the carbon dioxide gas were input values, the nitriding potential calculated by the in-furnace nitriding potential calculator 13 was an output value, and the target nitriding potential (the set nitriding potential) was a target value.
  • the nitriding potential in the processing furnace 2 was brought close to the target nitriding potential, by changing the total introduction amount of the ammonia gas, the nitrogen gas, the carbon monoxide gas and the carbon dioxide gas while keeping the ratio of the introduction amounts of the ammonia gas, the nitrogen gas, the carbon monoxide gas and the carbon dioxide gas constant.
  • the nitriding potential could not be stably controlled.
  • FIG. 18 A table of the above results is shown as FIG. 18 .

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)
US17/641,165 2019-10-11 2020-10-09 Surface hardening treatment device and surface hardening treatment method Pending US20220341021A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2019187310 2019-10-11
JP2019-187310 2019-10-11
PCT/JP2020/038315 WO2021070938A1 (fr) 2019-10-11 2020-10-09 Appareil de durcissement de surface et procédé de durcissement de surface

Publications (1)

Publication Number Publication Date
US20220341021A1 true US20220341021A1 (en) 2022-10-27

Family

ID=75438231

Family Applications (1)

Application Number Title Priority Date Filing Date
US17/641,165 Pending US20220341021A1 (en) 2019-10-11 2020-10-09 Surface hardening treatment device and surface hardening treatment method

Country Status (8)

Country Link
US (1) US20220341021A1 (fr)
EP (1) EP4043606A4 (fr)
JP (1) JPWO2021070938A1 (fr)
KR (1) KR20220057601A (fr)
CN (1) CN114829668A (fr)
MX (1) MX2022002518A (fr)
TW (1) TW202124731A (fr)
WO (1) WO2021070938A1 (fr)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6345320B1 (ja) * 2017-07-07 2018-06-20 パーカー熱処理工業株式会社 表面硬化処理装置及び表面硬化処理方法

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53115110A (en) 1977-03-18 1978-10-07 Nippon Telegr & Teleph Corp <Ntt> Light-combination type current switch scanning system
JPS57193398A (en) 1981-05-25 1982-11-27 Pentel Kk Nose knock type propelling pencil
NL9300901A (nl) * 1993-05-26 1994-12-16 Skf Ind Trading & Dev Werkwijze voor het carbonitreren van staal.
JP5883727B2 (ja) * 2012-06-01 2016-03-15 株式会社日本テクノ ガス窒化及びガス軟窒化方法
JP6552209B2 (ja) * 2015-02-10 2019-07-31 サンコール株式会社 金属製ばねの製造方法及び製造装置
JP6636829B2 (ja) 2015-05-12 2020-01-29 パーカー熱処理工業株式会社 窒化鋼部材及び窒化鋼部材の製造方法
JP2021042398A (ja) * 2017-12-27 2021-03-18 パーカー熱処理工業株式会社 窒化鋼部材並びに窒化鋼部材の製造方法及び製造装置
JP7094540B2 (ja) * 2018-04-26 2022-07-04 パーカー熱処理工業株式会社 窒化鋼部材並びに窒化鋼部材の製造方法及び製造装置
JP6503122B1 (ja) * 2018-08-17 2019-04-17 パーカー熱処理工業株式会社 表面硬化処理装置及び表面硬化処理方法

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6345320B1 (ja) * 2017-07-07 2018-06-20 パーカー熱処理工業株式会社 表面硬化処理装置及び表面硬化処理方法

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Machine Translation of JP-6345320-B1, retrieved April 1, 2024. *

Also Published As

Publication number Publication date
TW202124731A (zh) 2021-07-01
EP4043606A1 (fr) 2022-08-17
CN114829668A (zh) 2022-07-29
EP4043606A4 (fr) 2023-06-14
JPWO2021070938A1 (fr) 2021-04-15
MX2022002518A (es) 2022-04-01
WO2021070938A1 (fr) 2021-04-15
KR20220057601A (ko) 2022-05-09

Similar Documents

Publication Publication Date Title
US11155891B2 (en) Surface hardening treatment device and surface hardening treatment method
US11781209B2 (en) Surface hardening treatment device and surface hardening treatment method
JP5883727B2 (ja) ガス窒化及びガス軟窒化方法
US8157561B2 (en) System for controlling atmosphere gas inside furnace
US4175986A (en) Inert carrier gas heat treating control process
KR100512187B1 (ko) 열처리로의 분위기 제어방법 및 장치
US20220341021A1 (en) Surface hardening treatment device and surface hardening treatment method
EP0024106B1 (fr) Procédé de traitement thermique de métaux ferreux
EP0859067B1 (fr) Methode et appareillage pour contrôler l&#39;atmosphère d&#39;un four de traitement thermique
WO2022215526A1 (fr) Appareil et procédé de traitement de durcissement de surface
JP4092215B2 (ja) 熱処理炉の雰囲気制御装置
JP2019116687A (ja) 窒化処理装置、および、窒化処理方法
JPS6059060A (ja) 浸炭窒化の炉気制御方法

Legal Events

Date Code Title Description
AS Assignment

Owner name: PARKER NETSUSHORI KOGYO CO., LTD., JAPAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:HIRAOKA, YASUSHI;REEL/FRAME:059194/0056

Effective date: 20220210

STPP Information on status: patent application and granting procedure in general

Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED