JPH07258750A - Fluidized bed patenting heat treatment device and method using the same - Google Patents

Fluidized bed patenting heat treatment device and method using the same

Info

Publication number
JPH07258750A
JPH07258750A JP7288594A JP7288594A JPH07258750A JP H07258750 A JPH07258750 A JP H07258750A JP 7288594 A JP7288594 A JP 7288594A JP 7288594 A JP7288594 A JP 7288594A JP H07258750 A JPH07258750 A JP H07258750A
Authority
JP
Japan
Prior art keywords
fluidized bed
heat treatment
sand
gas
guide
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.)
Granted
Application number
JP7288594A
Other languages
Japanese (ja)
Other versions
JP3377288B2 (en
Inventor
Hiroshi Oba
浩 大羽
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP07288594A priority Critical patent/JP3377288B2/en
Publication of JPH07258750A publication Critical patent/JPH07258750A/en
Application granted granted Critical
Publication of JP3377288B2 publication Critical patent/JP3377288B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To prevent the flow-out of sand for fluidized medium by providing conical introducing guide parts having a specific taper on the inlet side and the outlet side of the introducing pipes for guiding a steel wire to be heat treated and arranging plural gas nozzles at the bending edge parts in the inside of the guide part while directing a fluidized bed body. CONSTITUTION:The introducing pipes 4 for guiding the steel wire 3 to be heat treated into sand 5 in a chamber 7 are provided on the inlet side and the outlet side of the fluidized bed patenting heat treatment device. The conical introducing guide part 9 having 30-40 deg. taper is arranged in each introducing pipe 4, and the gas nozzles 1 are arranged in the plural positions at the bending edge parts in the inside of the guide part 9 while directing the fluidized bed body. The fluidized sand 5 piled on a dispersing plate 6 is fluidized and floated up by feeding pressurized gas 8 into the chamber 7 and the steel wire 3 to be heat treated, is guided with the introducing pipe 4 to execute the patenting treatment through the sand 5. At this time, the gas having 0.05-0.075kg/cm<2> pressure is spouted from the gas nozzles 1 arranged in the guide part 9 to prevent the flow-out of the sand 5.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】流動層を用いた連続熱処理ライン
で熱処理を行う鋼線の通線方法に関するものであり、詳
しくは作業環境上問題となる砂の流出防止に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for passing a steel wire in which heat treatment is performed in a continuous heat treatment line using a fluidized bed, and more particularly to prevention of outflow of sand which is a problem in the working environment.

【0002】[0002]

【従来の技術】鋼線の恒温変態熱処理は、一般的に鉛を
用いたパテンティングが行われるが、近年の環境改善の
動向から細径においては鉛から流動層パテンティングに
移りかわりつつある。一方、流動層熱処理に使用される
砂はジルコンおよびアルミナの微粒子が多く用いられて
いる。流動層熱処理はこの微粒子の飛散および熱処理中
の流出が作業環境上問題となるほかランニングコストに
も影響が大きい。このため、従来の技術では流出した砂
を保留タンクに集め、そのタンクから熱処理炉に補給す
る方法が用いられている。しかしながらこの方法では、
補給タンクの設置および補給タンクから熱処理炉へ輸送
する設備が必要となり、設備費、ランニングコストおよ
び設置スペースの点で問題が残されていた。また、大気
中への飛散が完全に防止できないため、設備の周囲に砂
が堆積して、作業環境を著しく害するなどの問題が生じ
ている。
2. Description of the Related Art In the isothermal transformation heat treatment of steel wire, generally, patenting using lead is carried out. However, due to the recent trend of environmental improvement, in the small diameter, lead is being replaced by fluidized bed patenting. On the other hand, the sand used for the fluidized bed heat treatment is often made of zircon and alumina fine particles. In the fluidized bed heat treatment, the scattering of fine particles and the outflow during the heat treatment pose a problem in the working environment and also have a great influence on the running cost. Therefore, in the conventional technique, a method is used in which the outflowing sand is collected in a holding tank and the heat treatment furnace is replenished from the tank. However, with this method,
Installation of a replenishment tank and equipment for transporting from the replenishment tank to the heat treatment furnace were required, and there were problems in terms of equipment cost, running cost, and installation space. Further, since it is not possible to completely prevent scattering into the atmosphere, there is a problem that sand is accumulated around the equipment and the working environment is significantly damaged.

【0003】[0003]

【発明が解決しようとする課題】本発明はこのような流
動媒体の砂の流出を防止し、作業環境の確保を可能とし
たものである。
DISCLOSURE OF THE INVENTION The present invention prevents the outflow of sand in such a fluid medium and makes it possible to secure a working environment.

【0004】[0004]

【課題を解決するための手段】すなわち、本発明は上記
課題を解決するためになされたもので、その要旨とする
ところは、パスラインが水平な連続式の流動層熱処理装
置において、入り側および出側誘導管テーパー角度30
〜40°の錐体状誘導案内部を設け、該案内部に内側曲
がりの縁部を形成し、該縁部の複数個所にガスノズルを
流動層本体向きに指向させて設置したことを特徴とする
流動層パテンティング熱処理装置及び同装置において誘
導管案内部が四角錐体状を呈し、且つ、縁部に4個のガ
スノズルを設置したことを特徴とする流動層パテンティ
ング熱処理装置並びに流動層パテンティング熱処理装置
において、誘導管案内部に設けたガスノズルから、圧力
0.05〜0.075kg/cm2 の範囲でガスを噴射
し、砂の流出を防止することを特徴とする流動層パテン
ティング熱処理方法にある。
That is, the present invention has been made to solve the above-mentioned problems, and the gist of the present invention is to provide a continuous fluidized bed heat treatment apparatus having a horizontal pass line in the inlet side and Outlet guide tube taper angle 30
It is characterized in that a cone-shaped guide guide portion of -40 ° is provided, an inner curved edge portion is formed in the guide portion, and gas nozzles are installed at a plurality of positions of the edge portion so as to be oriented toward the fluidized bed main body. Fluidized bed patenting heat treatment equipment and fluidized bed patenting heat treatment equipment and fluidized bed patenting characterized in that the guide tube guiding portion in the equipment has a quadrangular pyramid shape and four gas nozzles are installed at the edges. In the heat treatment apparatus, a fluidized bed patenting heat treatment method characterized in that gas is injected at a pressure of 0.05 to 0.075 kg / cm 2 from a gas nozzle provided in the guide portion of the induction pipe to prevent sand from flowing out. It is in.

【0005】[0005]

【作用及び実施例】図1に本発明装置の被熱処理鋼線の
入り側部を示す。なお、出側部も同様な構成になってい
る。図2に誘導案内部の詳細を示したが図2aは側面図
であり、図2bはその正面図である。流動層パテンティ
ング熱処理装置において、被熱処理鋼線3を案内する誘
導管4は該熱処理装置の入り側および出側部に設置され
ている。この誘導管4の夫々にテーパー角度30〜40
°の錐体状誘導案内部4を設け、該案内部に内側曲がり
の縁部10を形成し、該縁部の複数個所にガスノズル1
を流動層本体向きに指向させて設置する。また誘導管案
内部9は好ましくは四角錐体状を呈し、且つ、縁部10
に設置するガスノズル1は被熱処理鋼線3を取り囲むよ
う上下、左右に4個設けるのが好ましい。このような構
成をとる本装置でチャンバー室7内に送られた圧送気体
8(空気又は窒素ガス)は、分散板6上に堆積する流動
層用サンド5を流動浮遊させる。一方被熱処理鋼線3は
誘導管4により案内され、流動浮遊中のサンド5内を通
過しパテンティング処理される。なお2は通常の熱処理
中でのサンドラインを示す。
OPERATION AND EXAMPLES FIG. 1 shows the entrance side of the heat-treated steel wire of the device of the present invention. Note that the outlet side has the same configuration. 2 shows the details of the guide portion, but FIG. 2a is a side view and FIG. 2b is a front view thereof. In the fluidized bed patenting heat treatment apparatus, the guide tubes 4 for guiding the steel wire 3 to be heat treated are installed on the inlet side and the outlet side of the heat treatment apparatus. Each of the guide tubes 4 has a taper angle of 30-40.
Is provided with a cone-shaped guide guide portion 4 having an angle of 10 °, and an inner curved edge portion 10 is formed in the guide portion.
Is installed so as to face the fluidized bed body. The guide tube guide portion 9 preferably has a shape of a quadrangular pyramid, and the edge portion 10
It is preferable that four gas nozzles 1 are installed in the vertical and horizontal directions so as to surround the steel wire 3 to be heat treated. The pressure-fed gas 8 (air or nitrogen gas) sent into the chamber 7 in the present apparatus having such a configuration causes the fluidized bed sand 5 deposited on the dispersion plate 6 to flow and float. On the other hand, the heat-treated steel wire 3 is guided by the guide tube 4, passes through the sand 5 in which the fluid is suspended, and is patented. In addition, 2 shows a sand line during a normal heat treatment.

【0006】連続式の流動層熱処理の場合、被熱処理鋼
線3が通過するパスラインよりも熱処理中のサンドライ
ン2を高くしなければ安定した熱処理を施すことは出来
ない。従って、誘導管案内部にガス噴射ノズル1がない
場合、誘導管4の端部から砂が流出する。このため、熱
処理中のサンドレベルが変化し、最終的にはパスライン
近傍まで高さが低下し、熱処理のばらつきを呈すること
になる。これを防止するために、本発明者が系統的な防
止策を検討した結果、誘導管案内部でのガス噴射ノズル
が有効であることを見い出したものである。
In the case of continuous fluidized bed heat treatment, stable heat treatment cannot be performed unless the sand line 2 during heat treatment is higher than the pass line through which the steel wire 3 to be heat treated passes. Therefore, when the guide pipe guide portion does not have the gas injection nozzle 1, sand flows out from the end portion of the guide pipe 4. For this reason, the sand level changes during the heat treatment, and finally the height decreases to the vicinity of the pass line, which causes variations in the heat treatment. In order to prevent this, the present inventor has studied systematic preventive measures, and as a result, found that the gas injection nozzle in the guide tube guide section is effective.

【0007】以下に本発明を詳細に述べる。誘導管端部
に取り付ける誘導案内部及び縁部は、誘導管から流出す
る砂を押し戻すために誘導管端部からガスを効率良く吹
き込むためのものである。誘導案内部のテーパは、小さ
すぎると、噴出するガス圧力によっては、誘導管内部の
砂を熱処理装置内に押し戻してしまう。このことによ
り、熱処理内の温度が降下して所定の熱処理雰囲気温度
を確保するのが困難となる。また、逆にテーパが大きす
ぎると、噴出ガスに乱流が激しく生じて、端部の出口か
ら砂が飛散するため流出防止効果が期待できない。以上
のことから、誘導管端部に取り付けるテーパー部は、3
0°〜40°が望ましい。
The present invention will be described in detail below. The guide portion and the edge portion attached to the end portion of the guide pipe are for efficiently blowing gas from the end portion of the guide pipe in order to push back the sand flowing out from the guide pipe. If the taper of the guide portion is too small, the sand inside the guide tube will be pushed back into the heat treatment apparatus depending on the pressure of the gas to be ejected. As a result, the temperature inside the heat treatment drops, making it difficult to secure a predetermined heat treatment atmosphere temperature. On the contrary, if the taper is too large, turbulent flow is generated in the jetted gas, and the sand is scattered from the outlet of the end portion, so that the outflow preventing effect cannot be expected. From the above, the taper part attached to the end of the guide tube is 3
0 ° to 40 ° is desirable.

【0008】また、誘導案内部の形状は、特に限定する
ものではないが、噴出するガスが乱流の発生しにくい四
角錐体状が望ましく、その際のガス噴出ノズル数は、例
えば、上下の2個、あるいは、左右の2個だけでは、乱
流を発生する可能性か高く、ガス噴射ノズル数は、4個
が望ましい。更に、ノズルの取り付け角度は、やはり、
乱流発生防止の観点から四角錘の底面に直角に取り付け
るのが望ましい。
Further, the shape of the guide portion is not particularly limited, but it is desirable that the ejected gas has a quadrangular pyramid shape in which turbulent flow is less likely to occur, and the number of gas ejection nozzles at that time is, for example, There is a high possibility that a turbulent flow will be generated with only two, or two on the left and right, and four gas injection nozzles are desirable. Furthermore, the mounting angle of the nozzle is
From the viewpoint of preventing turbulence, it is desirable to mount it at a right angle to the bottom surface of the square pyramid.

【0009】次に、ガスの噴射圧力について述べる。ガ
スの噴射圧力は、小さすぎると、砂の流出防止効果がな
く、逆に圧力が高すぎると、誘導管内の砂を熱処理炉側
に押し出すため、熱処理炉内の温度コントロールが不安
定となり、安定した熱処理を施すことが困難となる。以
上のことから、噴射ガス圧力は、0.05〜0.075
kg/cm2 が望ましい。
Next, the gas injection pressure will be described. If the gas injection pressure is too low, there is no sand outflow prevention effect, and if the pressure is too high, the sand in the induction tube is pushed out to the heat treatment furnace side, making temperature control in the heat treatment furnace unstable and stable. It becomes difficult to perform the heat treatment. From the above, the injection gas pressure is 0.05 to 0.075.
kg / cm 2 is desirable.

【0010】(実施例)5.5mmの線材を伸線加工に
より1.8mmの鋼線としたのち、流動層熱処理を行な
った。オーステナイト化温度は950℃一定で加熱時間
を60secとした。熱処理温度は540℃一定とし
た。用いた流動層の媒体はアルミナサンド(#120)
を使用した。熱処理中に流出する砂の量は誘導管端部の
直下に受皿を設置して、この中に溜った量を測定した。
(Example) A wire of 5.5 mm was drawn into a steel wire of 1.8 mm by wire drawing, and then a fluidized bed heat treatment was performed. The austenitizing temperature was constant at 950 ° C. and the heating time was 60 seconds. The heat treatment temperature was kept constant at 540 ° C. The fluidized bed medium used was alumina sand (# 120).
It was used. The amount of sand flowing out during the heat treatment was measured by setting a pan directly below the end of the guide tube and accumulating in the pan.

【0011】[0011]

【表1】 [Table 1]

【0012】表1に実施例を示す。No1〜8が本発明
法である。比較法としてNo9〜16を示す。比較法N
o9〜11は、本発明法と比較してテーパー角度がはず
れているため、砂の流出が多い。No12,13は、ノ
ズル個数が少ないため、砂の流出が多い。No14,1
5は、エアーノズルの噴射圧力が本発明法の限定範囲を
越えている。このため、砂の流出が多い。また、No1
6は、テーパーおよびエアーノズルなしの水準であり、
最も砂の流出が多い。一方、本発明法であるNo1〜8
はすべて0.11/hrであり、砂流出防止に対して効
果が大きいことが判る。これらは適正なテーパー角度お
よび適正なエアーノズルの噴射圧力とノズル配置の適正
化によって初めて砂の流出防止効果が現れることを示し
ている。
Examples are shown in Table 1. Nos. 1 to 8 are the method of the present invention. No. 9 to 16 are shown as comparative methods. Comparison method N
In Nos. 9 to 11, the taper angle is deviated from that of the method of the present invention, and thus the sand flows out a lot. In Nos. 12 and 13, since the number of nozzles is small, the outflow of sand is large. No14, 1
In No. 5, the injection pressure of the air nozzle exceeds the limit range of the method of the present invention. For this reason, sand often flows out. Also, No1
6 is the level without taper and air nozzle,
Most sand flows out. On the other hand, Nos. 1 to 8 of the present invention method
Is 0.11 / hr, and it can be seen that the effect is great for preventing sand outflow. These show that the effect of preventing the outflow of sand appears only after the proper taper angle, the proper injection pressure of the air nozzle, and the proper nozzle arrangement.

【0013】[0013]

【発明の効果】本発明により、連続式流動層熱処理にお
ける砂の流出が防止でき、安定した熱処理を施すことが
できるほか、安全上および作業環境の保全にもその効果
を発揮できる。
INDUSTRIAL APPLICABILITY According to the present invention, sand can be prevented from flowing out in the continuous fluidized bed heat treatment, stable heat treatment can be performed, and its effect can be exerted for safety and maintenance of working environment.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の砂の流出装置の概略を示す図。FIG. 1 is a diagram showing an outline of a sand outflow device of the present invention.

【図2】誘導案内部の詳細を示す図。FIG. 2 is a diagram showing details of a guide unit.

【符号の説明】[Explanation of symbols]

1 ガスノズル 2 熱処理中のサンドライン 3 被熱処理鋼線 4 誘導管 5 流動層用サンド 6 分散板 7 チヤンバー室 8 圧送気体 9 誘導案内部 10 縁部 1 gas nozzle 2 sand line during heat treatment 3 steel wire to be heat-treated 4 induction pipe 5 sand for fluidized bed 6 dispersion plate 7 chamber chamber 8 pumped gas 9 induction guide part 10 edge part

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 パスラインが水平な連続式の流動層熱処
理装置において、入り側および出側誘導管部にテーパー
角度30〜40°の錐体状誘導案内部を設け、該案内部
に内側曲がりの縁部を形成し、該縁部の複数個所にガス
ノズルを流動層本体向きに指向させて設置したことを特
徴とする流動層パテンティング熱処理装置。
1. A continuous type fluidized bed heat treatment apparatus having a horizontal pass line, wherein the inlet side and outlet side guide pipes are provided with cone-shaped guide guides having a taper angle of 30 to 40 °, and the guides are bent inward. The fluidized bed patenting heat treatment apparatus is characterized in that the gas nozzles are formed at a plurality of locations on the edges and the gas nozzles are oriented toward the fluidized bed body.
【請求項2】 誘導管案内部が四角錐体状を呈し、且
つ、縁部に4個のガスノズルを設置したことを特徴とす
る請求項1記載の流動層パテンティング熱処理装置。
2. The fluidized bed patenting heat treatment apparatus according to claim 1, wherein the guide tube guide portion has a shape of a quadrangular pyramid, and four gas nozzles are installed at an edge portion.
【請求項3】 請求項1および請求項2記載の流動層パ
テンティング熱処理装置において、誘導管案内部に設け
たガスノズルから、圧力0.05〜0.075kg/c
2 の範囲でガスを噴射し、砂の流出を防止することを
特徴とする流動層パテンティング熱処理方法。
3. The fluidized bed patenting heat treatment apparatus according to claim 1 or 2, wherein the pressure is 0.05 to 0.075 kg / c from a gas nozzle provided in the guide tube guide portion.
A fluidized bed patenting heat treatment method characterized in that a gas is sprayed in a range of m 2 to prevent sand from flowing out.
JP07288594A 1994-03-18 1994-03-18 Fluidized bed patenting heat treatment apparatus and fluidized bed patenting heat treatment method using the same Expired - Fee Related JP3377288B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP07288594A JP3377288B2 (en) 1994-03-18 1994-03-18 Fluidized bed patenting heat treatment apparatus and fluidized bed patenting heat treatment method using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP07288594A JP3377288B2 (en) 1994-03-18 1994-03-18 Fluidized bed patenting heat treatment apparatus and fluidized bed patenting heat treatment method using the same

Publications (2)

Publication Number Publication Date
JPH07258750A true JPH07258750A (en) 1995-10-09
JP3377288B2 JP3377288B2 (en) 2003-02-17

Family

ID=13502245

Family Applications (1)

Application Number Title Priority Date Filing Date
JP07288594A Expired - Fee Related JP3377288B2 (en) 1994-03-18 1994-03-18 Fluidized bed patenting heat treatment apparatus and fluidized bed patenting heat treatment method using the same

Country Status (1)

Country Link
JP (1) JP3377288B2 (en)

Also Published As

Publication number Publication date
JP3377288B2 (en) 2003-02-17

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