JP3117704B2 - Cooling method using fluidized bed - Google Patents
Cooling method using fluidized bedInfo
- Publication number
- JP3117704B2 JP3117704B2 JP02298395A JP29839590A JP3117704B2 JP 3117704 B2 JP3117704 B2 JP 3117704B2 JP 02298395 A JP02298395 A JP 02298395A JP 29839590 A JP29839590 A JP 29839590A JP 3117704 B2 JP3117704 B2 JP 3117704B2
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- Japan
- Prior art keywords
- fluidized bed
- gas
- cooling
- fluidized
- bed
- 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.)
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- Heat Treatments In General, Especially Conveying And Cooling (AREA)
- Furnace Details (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) この発明は、流動層炉の流動層中に処理品を埋没させ
ることにより行われる冷却処理方法に関し、鋼や鋳鉄の
冷却焼入、特にオーステンパ処理を効率よく行う方法に
関する。Description: TECHNICAL FIELD The present invention relates to a cooling treatment method performed by burying a treated product in a fluidized bed of a fluidized bed furnace, and relates to cooling and quenching of steel or cast iron, particularly, austempering. The present invention relates to a method for performing processing efficiently.
(従来の技術) 一般にオーステンパ処理は鋼や鋳鉄等の処理品をオー
ステナイト域まで加熱し、それをパーライト変態を阻止
するように急冷した後、250〜400℃程度の温度に所定時
間(約2時間)保持する熱処理法をいう。この保持中に
基地組織がベイナイト化して強度、靱性を向上させるこ
とを狙っている。(Conventional technology) Generally, in austempering, a treated product such as steel or cast iron is heated to an austenite region and rapidly cooled so as to prevent pearlite transformation, and then heated to a temperature of about 250 to 400 ° C for a predetermined time (about 2 hours). ) Hold heat treatment method. During this holding, it aims at improving the strength and toughness by turning the base structure into bainite.
前述したようなオーステンパ処理の冷却工程および高
温保持工程に流動層炉を適用することは公知である。従
来の流動層炉では冷却処理の全期にわたって流動層が形
成されており、流動媒体にアルミナ粉末、流動ガスにN2
ガスを用いるのが一般的であった。It is known to apply a fluidized-bed furnace to the cooling step and the high-temperature holding step of the austempering described above. In the conventional fluidized-bed furnace and the fluidized bed is formed over the full term of the cooling process, the alumina powder to the fluidized medium, N 2 to the fluidized gas
It was common to use gas.
流動層を用いた冷却によるオーステンパ処理は、流動
層炉内で処理品全体にわたって均一な温度分布が得られ
易いということから、処理品の各部が均一に行われると
いう冷却特性を有している。しかし、従来のN2ガスを流
動ガスとして用いた流動層では冷却能が小さいため、例
えば肉部が厚い鋳造部品のオーステンパ処理を行う場合
には、内部までベイナイト組織を得ることが困難であっ
た。The austempering treatment by cooling using a fluidized bed has a cooling characteristic that each part of the treated product is uniformly performed because a uniform temperature distribution is easily obtained throughout the treated product in the fluidized bed furnace. However, in a fluidized bed using a conventional N 2 gas as a fluidized gas, the cooling capacity is small, so that when performing austempering of a cast part having a thick wall, for example, it was difficult to obtain a bainite structure up to the inside. .
そこで、本発明者は、先にHeガスがN2ガスに比較して
はるかに大きな熱伝導度を有することに注目し、流動ガ
スとして従来のN2ガスの代わりにHeガスを用いることに
より冷却能を高めた流動層を用いたオーステンパ処理方
法及び装置を提案した。The present inventor has cooled by He gas earlier noted to have a much greater thermal conductivity compared to N 2 gas, a He gas instead of the conventional N 2 gas as a fluidizing gas An austempering method and apparatus using a fluidized bed with enhanced performance was proposed.
(発明が解決しようとする課題) ところが、このようなHeガス流動による流動層では、
冷却能が高い反面、流動層との接触部が過度に冷却され
る現象が見られ冷却時に処理品の表面と内部とで大きな
温度差が生じることが判明した。第1図(a)(b)に
は、流動層と処理品との温度分布の測定結果が示されて
いるが、(a)のHeガス流動の場合は、(b)のN2ガス
流動の場合に比べて処理品表面と内部との温度差が顕著
であることがわかる。また、Heガス流動の場合の冷却曲
線についてみると、第2図に示されるように、処理品表
面の温度はHeガスの高い冷却能によって急速に低下する
が、内部の温度は遅れて低下していくために、2つの曲
線は冷却の進行につれて大きく離れて行く。2つの曲線
が最も離れたところが、表面と内部の温度差が最大とな
るところである。このような大きな温度差は熱応力によ
る歪の発生を招き、特に、処理品の形状により各部で肉
厚にバラツキがある場合に、変形等をもたらす原因とな
る。(Problems to be solved by the invention) However, in such a fluidized bed by He gas flow,
Although the cooling capacity was high, a phenomenon in which the contact portion with the fluidized bed was excessively cooled was observed, and it was found that a large temperature difference occurred between the surface and the inside of the processed product during cooling. FIGS. 1 (a) and 1 (b) show the measurement results of the temperature distribution between the fluidized bed and the processed product. In the case of (a) He gas flow, (b) N 2 gas flow It can be seen that the temperature difference between the surface of the processed product and the inside is more remarkable than in the case of Looking at the cooling curve in the case of He gas flow, as shown in Fig. 2, the temperature of the treated product surface rapidly decreases due to the high cooling power of He gas, but the internal temperature decreases with a delay. In order to proceed, the two curves are far apart as cooling proceeds. The point where the two curves are farthest from each other is where the temperature difference between the surface and the inside is maximum. Such a large temperature difference causes distortion due to thermal stress, and particularly causes deformation when the thickness of each part varies depending on the shape of the processed product.
したがって、本発明は、Heガスを流動ガスに用いた高
効率の熱処理方法において、処理品表面と内部との温度
差による歪の発生を防ぐことを目的とする。Accordingly, an object of the present invention is to prevent the occurrence of distortion due to a temperature difference between the surface of a processed product and the inside in a highly efficient heat treatment method using He gas as a flowing gas.
(課題を解決するための手段) 前記目的を達成するために、第1発明による流動層を
用いる冷却処理方法は、流動層炉の流動層中に処理品を
埋没させることにより行われる流動層を用いた冷却処理
方法において、流動層の流動ガスにHeガスを用いるとと
もに、この流動ガスを間欠的に複数回流動層内に流入さ
せ、流動層内において流動層と固定層とを交互に形成さ
せながら処理品を処理するようにしたことを特徴とする
ものである。(Means for Solving the Problems) In order to achieve the above object, a cooling method using a fluidized bed according to the first invention is a method for cooling a fluidized bed performed by burying a processed product in a fluidized bed of a fluidized bed furnace. In the cooling treatment method used, He gas was used as the fluidized gas in the fluidized bed, and this fluidized gas was intermittently flowed into the fluidized bed a plurality of times to alternately form the fluidized bed and the fixed bed in the fluidized bed. It is characterized in that the processed product is processed while processing.
また、第2発明による流動層を用いる処理方法は、処
理品をオーステナイト領域の温度域まで加熱した後に、
流動層炉の流動層中に埋設させることにより行われる流
動層を用いた冷却処理方法において、流動層の流動ガス
にHeガスを用いるとともに、この流動ガスを間欠的に複
数回流動層内に流入させ、流動層内において流動層と固
定層とを交互に形成させながら処理品を冷却することに
より、フェライトおよびパーライトの生成を抑制しなが
らベイナイト生成温度域まで冷却し、その後Heガスの流
入を停止して固定層中で所定時間保持することにより、
処理品の基地組織をベイナイト組織化することを特徴と
するものである。Further, in the processing method using the fluidized bed according to the second invention, after the processed product is heated to a temperature range of an austenite region,
In a cooling treatment method using a fluidized bed performed by embedding in a fluidized bed of a fluidized bed furnace, He gas is used as the fluidized gas in the fluidized bed, and this fluidized gas is intermittently flown into the fluidized bed several times. By cooling the treated product while alternately forming a fluidized bed and a fixed bed in the fluidized bed, cooling to the bainite formation temperature range while suppressing the production of ferrite and pearlite, then stopping the flow of He gas By holding for a predetermined time in the fixed layer,
It is characterized in that the base structure of the processed product is bainite-structured.
さらに、第3発明による流動層を用いる冷却処理方法
は、処理品をオーステナイト領域の温度域まで加熱した
後に、流動層炉の流動層中に埋設させることにより行わ
れる流動層を用いた冷却処理方法において、流動層の流
動ガスにHeガスを用いるとともに、この流動ガスを間欠
的に複数回流動層内に流入させ、流動層内において流動
層と固定層とを交互に形成させながら処理品を冷却する
ことにより、フェライトおよびパーライトの生成を抑制
しながらベイナイト生成温度域まで冷却し、その後Na2
ガス流動に切り替えることにより、処理品の基地組織を
ベイナイト組織化することを特徴とするものである。Further, the cooling treatment method using a fluidized bed according to the third invention is a cooling treatment method using a fluidized bed performed by heating a treated product to a temperature range of an austenite region and then burying the treated product in a fluidized bed of a fluidized bed furnace. He gas is used as the fluidized gas in the fluidized bed, and the fluidized gas is intermittently flowed into the fluidized bed several times, and the processed product is cooled while alternately forming the fluidized bed and the fixed bed in the fluidized bed. by, cooled to the bainite formation temperature range while suppressing the formation of ferrite and pearlite, then Na 2
It is characterized in that the base structure of the processed product is made bainite by switching to gas flow.
(作 用) 高温状態にある処理品の冷却処理を行う場合、Heガス
流動による流動層内において、処理品の表面温度は急速
に低下する。すなわち、Heガスの熱伝導度が大きいため
に、処理品表面から急激に熱が奪われて行く。このよう
なHeガス流動の状態では、処理品表面からの外部への熱
放出速度の方が、処理品内部から表面への熱伝導速度よ
りも大きく、処理品内部と表面とで著しい温度差が生じ
る。Heガスを止めて流動層から固定層の状態に変化させ
ると、熱放出速度は一気に低下し、逆に、処理品内部で
の熱の移動の方が相対的に大きくなるために、表面温度
は一時的に上昇する。その結果、処理品内部と表面との
温度差は実質的に解消され、処理品全体の温度はほぼ均
一化する。このようなHeガスの間欠的な流動を繰り返し
て、流動層と固定層とが交互に形成されるようにしなが
ら冷却処理を行うと、処理品表面の温度は段階的に低下
し、しかも内部との温度差は小さく抑えられることにな
る。(Operation) When performing cooling treatment of a processed product in a high temperature state, the surface temperature of the processed product rapidly decreases in a fluidized bed due to He gas flow. That is, since the thermal conductivity of the He gas is large, heat is rapidly removed from the surface of the processed product. In such a state of He gas flow, the rate of heat release from the surface of the processed product to the outside is greater than the rate of heat conduction from the inside of the processed product to the surface, and there is a remarkable temperature difference between the inside of the processed product and the surface. Occurs. When He gas is stopped and the state changes from a fluidized bed to a fixed bed, the heat release rate decreases at a stretch, and conversely, the heat transfer inside the treated product becomes relatively large, so the surface temperature becomes Rise temporarily. As a result, the temperature difference between the inside of the processed product and the surface is substantially eliminated, and the temperature of the entire processed product is substantially uniform. When the cooling process is performed while repeating the intermittent flow of the He gas so that the fluidized bed and the fixed bed are alternately formed, the temperature of the surface of the processed product decreases step by step, and furthermore, Is kept small.
したがって、本発明に係わる熱処理方法を適用したオ
ーステンパ処理では、第3図のような冷却曲線が得られ
る (発明の効果) Heガスを間欠的に流して流動層と固定層とを交互に形
成させることにより、Heガスが流動する流動層による高
い冷却効果と、固定層による緩徐でかつ均一な冷却効果
の両方が得られる。本発明に係わる方法をオーステンパ
処理の冷却工程に適用した場合、Heガスが示す高い冷却
効果が間欠的に付加されることによりN2ガス流動によっ
ては困難であったφ20mm程度の肉厚部品で非合金FCD材
からなる部品についても、内部までベイナイト化されて
オーステンパ処理を行うことが可能になった。また、均
一な冷却効果により、処理品の低歪化が実現できるよう
になった。Therefore, in the austempering treatment to which the heat treatment method according to the present invention is applied, a cooling curve as shown in FIG. 3 is obtained. (Effect of the Invention) He gas is intermittently flowed to alternately form a fluidized bed and a fixed bed. Thus, both a high cooling effect by the fluidized bed in which the He gas flows and a slow and uniform cooling effect by the fixed bed can be obtained. When the method according to the present invention is applied to the cooling process of the austempering process, the high cooling effect exhibited by the He gas is intermittently added, so that it is difficult to use a thick part of about φ20 mm, which is difficult by the N 2 gas flow. Parts made of alloy FCD material have also been bainitized to the inside, making it possible to perform austempering. In addition, the uniform cooling effect can reduce the distortion of the processed product.
本発明に係わる処理方法は、前記したようなオーステ
ンパ処理や焼入における冷却処理工程のみならず、各種
加熱後処理等熱処理方法に適用した場合にも、同様に高
い処理効率のもとに均一な熱処理を実施可能にする。The processing method according to the present invention is not limited to the above-described cooling process in the austempering process or quenching, but also when applied to a heat treatment method such as various post-heating processes, the uniformity is similarly high under a high processing efficiency. Enables heat treatment.
(実施例) 次に、本発明の具体的な一実施例を図面を参照しつつ
詳細に説明する。(Example) Next, a specific example of the present invention will be described in detail with reference to the drawings.
第4図に本発明に係わる方法を実施するための装置の
一例が示されている。第4図において、流動層炉1内に
は、800〜900℃に加熱された球状黒鉛鋳鉄製部材を処理
品2として装入する。また、80メッシュ程度の粒径のア
ルミナ粉11を装入しておく。次に、バルブ3、4、5を
開きHeガスボンベ8からターボファン10により加速した
Heガスを配管9を通して流動層炉1内に導入する。な
お、バルブ3は適当なHe供給量に達した後に閉じる。ま
た、バルブ4は数秒〜数10秒毎に開閉され、このバルブ
4が開いている間、Heガスが流動層炉内に流される。He
ガスが導入されると、流動層炉内では、分散板12からHe
ガスが吹き上げられ、アルミナ粉11が流動することによ
り流動層が形成される。この流動層の熱交換作用により
処理品2が冷却される。熱交換によりあたためられたHe
ガスはフィルタ14を通って流動層炉1の上方から排出さ
れ、熱交換器15によって冷却される。それから配管9を
通り再びターボファン10によって加速されて流動層炉1
に導入される。このように流動層形成中はHeガスを循環
させて処理品2を約250〜400℃のベイナイト変態温度ま
で処理品2の表面および内部の温度差を僅少としつつ冷
却する。一方、バルブ4が閉止されることによりHeガス
の流動が停止すると、アルミナ粉11は流動層炉1の下部
に沈降し、間欠的に固定層が形成される。必要に応じて
ヒータ16により流動層炉1内を所定恒温温度に調節する
ことによりこのベイナイト変態温度を保持し、流動層炉
中においてベイナイト変態を行わせることも可能となっ
ている。流動層または固定層の間欠形成による冷却処理
経過後、バルブ3、4を閉じバルブ6を開け(バルブ7
は閉じたままである。)ポンプ17によりHeガスを流動層
炉1内から抜き出して貯蔵タンク18に貯蔵する。貯蔵完
了後はまたバルブ6を閉じる。ベイナイト変態が終了し
た球状黒鉛鋳鉄部材としての処理品2は炉外へ取り出し
て放冷される。FIG. 4 shows an example of an apparatus for performing the method according to the present invention. In FIG. 4, a spheroidal graphite cast iron member heated to 800 to 900 ° C. is charged as a processed product 2 into a fluidized bed furnace 1. Also, alumina powder 11 having a particle size of about 80 mesh is charged. Next, the valves 3, 4 and 5 were opened, and the gas was accelerated from the He gas cylinder 8 by the turbo fan 10.
He gas is introduced into the fluidized bed furnace 1 through a pipe 9. Note that the valve 3 is closed after reaching an appropriate He supply amount. The valve 4 is opened and closed every few seconds to several tens of seconds, and while the valve 4 is open, He gas flows into the fluidized bed furnace. He
When the gas is introduced, in the fluidized bed furnace, He
The gas is blown up and the alumina powder 11 flows to form a fluidized bed. The processed product 2 is cooled by the heat exchange action of the fluidized bed. He warmed up by heat exchange
The gas is discharged from above the fluidized-bed furnace 1 through the filter 14 and cooled by the heat exchanger 15. Then, the fluidized bed furnace 1 is accelerated again by the turbofan 10 through the pipe 9.
Will be introduced. During the formation of the fluidized bed, the He gas is circulated to cool the treated product 2 to a bainite transformation temperature of about 250 to 400 ° C. while minimizing the temperature difference between the surface and the inside of the treated product 2. On the other hand, when the flow of the He gas is stopped by closing the valve 4, the alumina powder 11 sinks to the lower part of the fluidized bed furnace 1, and a fixed bed is formed intermittently. If necessary, the bainite transformation temperature is maintained by adjusting the inside of the fluidized bed furnace 1 to a predetermined constant temperature by the heater 16, and bainite transformation can be performed in the fluidized bed furnace. After the cooling process due to the intermittent formation of the fluidized bed or the fixed bed, the valves 3 and 4 are closed and the valve 6 is opened (the valve 7
Remains closed. 2) He gas is extracted from the fluidized bed furnace 1 by the pump 17 and stored in the storage tank 18. After the storage is completed, the valve 6 is closed again. The treated product 2 as a spheroidal graphite cast iron member after the bainite transformation is taken out of the furnace and allowed to cool.
別の処理品2をオーステンパ処理するために再びこの
流動層炉1装置を使用する際には、処理品2を装入後、
バルブ7、4、5を開け、コンプレッサ19により貯蔵タ
ンク18から排出されたHeガスを加圧して流動層炉1に送
り出す。そして前述の操作を繰り返して行う。この際He
ガスの流動が不足であればバルブ3を開けてHeガスを追
加供給すればよい。When the fluidized bed furnace 1 is used again for austempering another treated product 2, after the treated product 2 is charged,
The valves 7, 4 and 5 are opened, and the He gas discharged from the storage tank 18 by the compressor 19 is pressurized and sent to the fluidized bed furnace 1. Then, the above operation is repeated. At this time, He
If the gas flow is insufficient, the valve 3 may be opened to supply additional He gas.
次に、前記したような装置を用いて実際にオーステン
パ処理を行った具体例について説明する。Next, a specific example in which an austempering process is actually performed using the above-described apparatus will be described.
第5図は、オーステンパ処理に使用した部品の形状を
示す図である。この部品は球状黒鉛鋳鉄から成り、外径
φ90mm、内径φ30mmである。この部品を、Heガスの間欠
送気条件を、5秒流動層→5秒固定層→5秒流動層→5
秒固定層→10秒流動層→10秒固定層→10秒流動層→10秒
固定層となるようにして冷却処理を行った。この処理に
おける冷却状態を、第5図に示される処理品2表面部と
肉厚中心部について測定し、それぞれの冷却曲線を第6
図に示す。なお、図中F.Pはフェライト・パーライトの
略号である。このようなHeガス間欠流動の結果処理品表
面と肉厚中心部との温度差は最も大きなところでも150
℃以下で、処理品にも熱偏差による歪がほとんど無く、
中心部までベイナイト相が得られた。FIG. 5 is a diagram showing the shape of a part used in the austempering process. This part is made of spheroidal graphite cast iron and has an outer diameter of 90 mm and an inner diameter of 30 mm. This part was changed to a He gas intermittent air supply condition of 5 seconds fluidized bed → 5 seconds fixed bed → 5 seconds fluidized bed → 5 seconds.
The cooling treatment was performed in such a manner that the second fixed bed → 10 second fluidized bed → 10 second fixed bed → 10 second fluidized bed → 10 second fixed bed. The cooling state in this processing was measured for the surface portion and the center of the thickness of the processed product 2 shown in FIG.
Shown in the figure. In the drawing, FP is an abbreviation for ferrite / pearlite. As a result of such intermittent He gas flow, the temperature difference between the surface of the treated product and the center of the wall thickness is 150
Below ℃, the processed product has almost no distortion due to thermal deviation,
A bainite phase was obtained up to the center.
比較のために、同じ部品について、従来のN2ガス流動
による非間欠流動層を用いた冷却処理と、連続したHeガ
ス流動による非間欠流動層を用いた冷却処理とをそれぞ
れ行った。それぞれの処理において得られた処理品表面
部と肉厚中心部の冷却曲線とを第7図に示す。For comparison, the same component was subjected to a conventional cooling process using a non-intermittent fluidized bed with N 2 gas flow and a cooling process using a non-intermittent fluidized bed with continuous He gas flow. FIG. 7 shows the surface of the treated product and the cooling curve at the center of the wall thickness obtained in each treatment.
第7図からわかるように、従来のN2ガス流動による冷
却処理では、処理品表面部と肉厚中心部との温度差は少
ないが、中心部では冷却曲線がフェライト・パーライト
ノーズに触れるため、完全なベイナイト組織が得られな
かった。As can be seen from FIG. 7, in the conventional cooling treatment using N 2 gas flow, although the temperature difference between the surface of the treated product and the center of the wall thickness is small, the cooling curve at the center touches the ferrite / pearlite nose. No complete bainite structure was obtained.
また、連続したHeガス流動による冷却処理の場合に
は、肉厚中心部まで一様なベイナイト相が得られたが、
処理品表面部と肉厚中心部との温度差が最も大きなとこ
ろでは200℃以上あって、歪の発生が予想された。In the case of cooling treatment by continuous He gas flow, a uniform bainite phase was obtained up to the center of the wall thickness.
Where the temperature difference between the surface of the treated product and the center of the wall thickness was the largest, the temperature was 200 ° C. or more, and the occurrence of distortion was expected.
前述した実施例では、流動ガスにHeガスのみを用いた
が、冷却処理の前半、すなわち、冷却処理の開始期ない
しベイナイト相生成温度範囲のような急冷が必要な段階
でのみHeガスを用い、後半のフェライト・パーライト域
を過ぎた時点、すなわちMS点近傍ではN2ガス流動に変
え、あるいは流動ガスを止めて固定層にすることによ
り、冷却速度を遅くして歪の防止をより確実なものとす
ることもできる。In the above-described embodiment, only He gas was used as the flowing gas.However, the first half of the cooling process, that is, He gas only at the stage where rapid cooling is required, such as the beginning of the cooling process or the bainite phase formation temperature range, time past the ferrite-pearlite area of the second half, i.e. changed to the N 2 gas flow under M S point near, or by the fixed layer to stop the flowing gas, more reliable prevention of distortion at slow cooling rate It can also be.
第1図(a)(b)は処理品の温度分布を示す図、第2
図および第3図は従来例および本発明の比較を示すもの
で第2図は従来のオーステンパ処理の冷却曲線を示すグ
ラフ、第3図は本発明に係わる方法によるオーステンパ
処理の冷却曲線を示すグラフ、第4図は本発明に係わる
方法を実施するための具体的装置の一例を示す構成図、
第5図は本発明の実施例に用いた処理品の斜視図、第6
図は実施例のオーステンパ処理の冷却曲線を示すグラ
フ、および第7図は比較例のオーステンパ処理の冷却曲
線を示すグラフである。 1……流動層炉 2……処理品(球状黒鉛鋳鉄) 3〜7……バルブ、8……Heガスボンベ 9……配管 10、24……ターボファン 11……アルミナ粉、12……分散板 14……フィルタ、15……熱交換器 16……ヒータ、17……ポンプ 18……貯蔵タンク、19……コンプレッサFIGS. 1 (a) and 1 (b) show the temperature distribution of the processed product, and FIG.
FIG. 3 and FIG. 3 show a comparison between the conventional example and the present invention. FIG. 2 is a graph showing a cooling curve of the conventional austempering, and FIG. 3 is a graph showing a cooling curve of the austempering by the method according to the present invention. FIG. 4 is a block diagram showing an example of a specific apparatus for performing the method according to the present invention;
FIG. 5 is a perspective view of a processed product used in the embodiment of the present invention, and FIG.
FIG. 7 is a graph showing a cooling curve of the austempering process of the embodiment, and FIG. 7 is a graph showing a cooling curve of the austempering process of the comparative example. 1 Fluidized bed furnace 2 Processed product (spheroidal graphite cast iron) 3 to 7 Valve 8 He gas cylinder 9 Pipe 10 24 Turbo fan 11 Alumina powder 12 Dispersion plate 14 ... Filter, 15 ... Heat exchanger 16 ... Heater, 17 ... Pump 18 ... Storage tank, 19 ... Compressor
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C21D 1/00 125 C21D 1/18 C21D 1/53 C21D 5/00 ──────────────────────────────────────────────────続 き Continuation of the front page (58) Field surveyed (Int. Cl. 7 , DB name) C21D 1/00 125 C21D 1/18 C21D 1/53 C21D 5/00
Claims (3)
ことにより行われる流動層を用いた冷却処理方法におい
て、流動層の流動ガスにHeガスを用いるとともに、この
流動ガスを間欠的に複数回流動層内に流入させ、流動層
内において流動層と固定層とを交互に形成させながら処
理品を処理するようにしたことを特徴とする流動層を用
いた冷却処理方法。In a cooling method using a fluidized bed performed by embedding a treated product in a fluidized bed of a fluidized bed furnace, a He gas is used as a fluidized gas in the fluidized bed, and the fluidized gas is intermittently used. A cooling process using a fluidized bed, wherein the treated product is processed while flowing into the fluidized bed a plurality of times and the fluidized bed and the fixed bed are alternately formed in the fluidized bed.
加熱した後に、流動層炉の流動層中に埋設させることに
より行われる流動層を用いた冷却処理方法において、流
動層の流動ガスにHeガスを用いるとともに、この流動ガ
スを間欠的に複数回流動層内に流入させ、流動層内にお
いて流動層と固定層とを交互に形成させながら処理品を
冷却することにより、フェライトおよびパーライトの生
成を抑制しながらベイナイト生成温度域まで冷却し、そ
の後Heガスの流入を停止して固定層中で所定時間保持す
ることにより、処理品の基地組織をベイナイト組織化す
ることを特徴とする流動層を用いた冷却処理方法。2. A cooling method using a fluidized bed, which comprises heating a treated product to a temperature range of an austenite region and then burying the treated product in a fluidized bed of a fluidized bed furnace. The fluidized gas is intermittently flowed into the fluidized bed several times, and the processed product is cooled while forming the fluidized bed and the fixed bed alternately in the fluidized bed, thereby producing ferrite and pearlite. The fluidized bed is characterized by cooling to the bainite generation temperature range while suppressing the flow of He gas, and then stopping the inflow of He gas and maintaining the fixed structure in the fixed bed for a predetermined time to form the matrix structure of the treated product into bainite. Cooling treatment method.
加熱した後に、流動層炉の流動層中に埋設させることに
より行われる流動層を用いた冷却処理方法において、流
動層の流動ガスにHeガスを用いるとともに、この流動ガ
スを間欠的に複数回流動層内に流入させ、流動層内にお
いて流動層と固定層とを交互に形成させながら処理品を
冷却することにより、フェライトおよびパーライトの生
成を抑制しながらベイナイト生成温度域まで冷却し、そ
の後N2ガス流動に切り替えることにより、処理品の基地
組織をベイナイト組織化することを特徴とする流動層を
用いた冷却処理方法。3. A cooling treatment method using a fluidized bed performed by heating a treated product to a temperature range of an austenite region and then burying the treated product in a fluidized bed of a fluidized bed furnace. The fluidized gas is intermittently flowed into the fluidized bed several times, and the processed product is cooled while forming the fluidized bed and the fixed bed alternately in the fluidized bed, thereby producing ferrite and pearlite. A cooling method using a fluidized bed, characterized in that the base structure of the processed product is bainite-structured by cooling to a bainite generation temperature region while suppressing the temperature and then switching to a N 2 gas flow.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP02298395A JP3117704B2 (en) | 1990-11-02 | 1990-11-02 | Cooling method using fluidized bed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP02298395A JP3117704B2 (en) | 1990-11-02 | 1990-11-02 | Cooling method using fluidized bed |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04173916A JPH04173916A (en) | 1992-06-22 |
| JP3117704B2 true JP3117704B2 (en) | 2000-12-18 |
Family
ID=17859149
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP02298395A Expired - Fee Related JP3117704B2 (en) | 1990-11-02 | 1990-11-02 | Cooling method using fluidized bed |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3117704B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6502499B2 (en) | 2000-09-26 | 2003-01-07 | Hitachi Construction Machinery Co., Ltd. | Hydraulic recovery system for construction machine and construction machine using the same |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6385900B2 (en) * | 2015-07-16 | 2018-09-05 | 中外炉工業株式会社 | Steel strip cooling device |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6043410B2 (en) | 2010-04-14 | 2016-12-14 | 株式会社半導体エネルギー研究所 | Display device and electronic device |
| JP6253567B2 (en) | 2014-11-17 | 2017-12-27 | ヤンマー株式会社 | Work vehicle moving system |
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1990
- 1990-11-02 JP JP02298395A patent/JP3117704B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6043410B2 (en) | 2010-04-14 | 2016-12-14 | 株式会社半導体エネルギー研究所 | Display device and electronic device |
| JP6253567B2 (en) | 2014-11-17 | 2017-12-27 | ヤンマー株式会社 | Work vehicle moving system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6502499B2 (en) | 2000-09-26 | 2003-01-07 | Hitachi Construction Machinery Co., Ltd. | Hydraulic recovery system for construction machine and construction machine using the same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04173916A (en) | 1992-06-22 |
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