JPS6054254A - Automatic spraying device for powder in continuous casting - Google Patents

Automatic spraying device for powder in continuous casting

Info

Publication number
JPS6054254A
JPS6054254A JP16246083A JP16246083A JPS6054254A JP S6054254 A JPS6054254 A JP S6054254A JP 16246083 A JP16246083 A JP 16246083A JP 16246083 A JP16246083 A JP 16246083A JP S6054254 A JPS6054254 A JP S6054254A
Authority
JP
Japan
Prior art keywords
powder
pipe
mold
nozzle
fed
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
JP16246083A
Other languages
Japanese (ja)
Other versions
JPH0470109B2 (en
Inventor
Haruo Oguro
大黒 治男
Toshihiro Iwasaki
岩崎 年博
Takaaki Hirokane
広兼 隆昭
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 JP16246083A priority Critical patent/JPS6054254A/en
Publication of JPS6054254A publication Critical patent/JPS6054254A/en
Publication of JPH0470109B2 publication Critical patent/JPH0470109B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/10Supplying or treating molten metal
    • B22D11/108Feeding additives, powders, or the like

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Continuous Casting (AREA)

Abstract

PURPOSE:To provide a titled device which can feed powder at a constant rate and spray uniformly the powder in a mold with a small amt. of a carrier gas with the device for spraying the powder pneumatically by providing successively a means for feeding the powder, a means for transporting the powder in suspension and a spraying nozzle. CONSTITUTION:The inside of a tank 1 is pressurized and a stop valve 3 is repeatedly opened and closed at set timings. Powder is filled approximately in a storage tank 43 by one time of such opening. The powder is discharged through a discharge port 47 and is dispersed by a conical-shaped projecting part 45, by which the powder is dropped in a dispersed state through plural holes 46. The powder in the mid-way of falling is forcibly fed in a feed pipe 5 by the pressure gas injected from an injector 7A and is fed in a suspended state. If the pipe 5 is long and the pressure drop in the pipe 5 is large, the powder is additionally fed by an injector 7B. The powder transported in suspension in the above-mentioned way is sprayed uniformly in a casting mold 10 from a spray nozzle 8 provided with plural holes or slits in the longitudinal direction of the tubular body which is provided successively to the terminal of the pipe 5 and is closed at one end.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は連続鋳造設備におけるモールド内に。[Detailed description of the invention] [Industrial application field] The present invention is applied in a mold in continuous casting equipment.

パウダーを気体によシ定量供送し自動的に均一散布する
ためのパウダー自動散布装置に関するものである。
This invention relates to an automatic powder dispersion device for supplying a fixed amount of powder using gas and automatically distributing it uniformly.

〔従来技pドj〕[Conventional technique pdoj]

現在製鉄業界では世界的に連続鋳造機の導入が進んでい
る。連続鋳造においては、スラブやブルーム等の鋳片を
形成するモールド内の溶鋼表面に。
Continuous casting machines are currently being introduced worldwide in the steel industry. In continuous casting, on the surface of molten steel in the mold that forms slabs such as slabs and blooms.

オツシレーションと併せ鋳片−モールド銅板間の潤滑、
及び不純物除去、保温等を目的にパウダーを供給散布す
ることが不可欠である。従来方法ではモールド内湯面上
へ人手によシ供給−散布してオシ、この場会、散布量は
人の勘によっていたため個人差がおり、:lfI切な潤
滑が常に行えるとは限らなかった。また高熱および、a
ウダー粉塵発生によシ作業環境が悪いという問題があっ
た。他方最近人手Vこよらず自動的に散布することも試
みられておシ、公知な方式としてスズリングフィーダー
等による機械輸送−散布方式が知られており、これが主
流となっている。しかし、本方式は供給散布フィーダー
をタンディツシュ−モールド間の狭スペースに設置する
必要があり、フィーダーの必要大きさから決まる設置ス
ペースの限界及びフレキシビリティ−のなさから、特に
小断面サイズには不適であシ、さらにモールド周辺の作
業性が悪い、熱的問題から装置の信頼性が低い等の間誼
があった。また気送方式も試みられたが、該方式では、
粉塵発生およびコストの点から気送ガスの小量化を図り
、プラグ輸送形態をとるがパウダーは粉粒状の為給送経
路内の接触抵抗が大きく、配管内詰りゃ、圧縮ガスが断
続的にノズルよ、!7噴出し。
In addition to oscillation, lubrication between slab and molded copper plate,
It is also essential to supply and spray powder for the purpose of removing impurities, keeping heat, etc. In the conventional method, lubricant was manually supplied and sprinkled onto the surface of the hot water inside the mold, and the amount of spraying was based on human intuition, which resulted in individual differences, and it was not always possible to provide adequate lubrication. Also high fever and a
There was a problem that the working environment was poor due to the generation of powder dust. On the other hand, attempts have recently been made to automatically spread the powder without requiring manual intervention, and a known method is a mechanical transportation/dispersion method using a slurry feeder or the like, which has become the mainstream. However, this method requires the dispersion feeder to be installed in a narrow space between the tundish and mold, making it particularly unsuitable for small cross-sectional sizes due to the limited installation space determined by the required size of the feeder and lack of flexibility. There were problems such as poor workability around the reeds and the mold, and low reliability of the equipment due to thermal problems. A pneumatic method was also tried, but with this method,
In order to reduce the amount of pneumatic gas from the viewpoint of dust generation and cost, a plug transportation method is used, but since the powder is in the form of powder particles, the contact resistance in the feeding route is large, and if the piping becomes clogged, the compressed gas will intermittently flow through the nozzle. Yo,! 7 squirts.

モールド内パウダーを巻き上がらせ粉塵を発生する等の
為、モールド内へのパウダー散布には致っておらず、現
在は気送のフレキシビリティを活用し、−次側のパウダ
ー輸送に採用されているのみテ、散布ハスプリングフィ
ーダーによっている。
This method has not been used for dispersing powder inside the mold because it stirs up the powder inside the mold and generates dust, but it is currently being used to transport powder to the next side by taking advantage of the flexibility of pneumatic conveyance. They are only fed by a spring feeder.

〔発明の目的〕[Purpose of the invention]

本発明はこれら、諸間肩を解決するため浮遊輸送形態を
とる気送方式により、小量のキャリヤガスで顆粒パウダ
ーの定量給送−モールド内への均一散布を可能としたも
ので、簡易且つフレキシビリディ、コンパクト性を有す
る装置構成によって自動で適確且り信顆性の高いパウダ
ー散布を粉塵を発生させることな、<、作業住良〈実施
しうる装置を提供するものである。
In order to solve these issues, the present invention utilizes a pneumatic conveyance system that uses a floating transport system to enable fixed-quantity feeding and uniform dispersion of granular powder into the mold using a small amount of carrier gas, making it simple and easy to use. The purpose of the present invention is to provide a device that can perform automatic, accurate, and highly reliable powder dispersion without generating dust, and with a flexible and compact device configuration.

〔発明の構成〕 本発明は、貯留したパウダーを所定量送シ出すためのパ
ウダー給送手段と、送シ出されたパウダーを鋳型まで輸
送するためのパウダー浮遊輸送手段と、輸送されたパウ
ダーを鋳型内湯面上に散布するための散布ノズルとで構
成されている。
[Structure of the Invention] The present invention provides a powder feeding means for delivering a predetermined amount of stored powder, a powder floating transport means for transporting the delivered powder to a mold, and a powder floating transport means for transporting the delivered powder to a mold. It consists of a spray nozzle for spraying onto the surface of the mold.

〔実施例〕〔Example〕

まずノミウダー給送手段について説明する。 First, the powder feeding means will be explained.

第1図は、本発明実施例装置の全体図〔(A)はブルー
ム、ビレット用、(B)はスラブ用〕を示し、1はN2
吹込により吸湿を防ぐ程度に密閉されたタンクで、内部
にパウダー12が収容され、上部にN2の導管2が接続
され、タンク内上方よりタンク1円のパウダーに水分を
取り除いたN2ガスを流すとともに、パウダーの糊量を
防ぐ為タンク内下方からも噴出させている。またタンク
1にはロードセル6を設け、パウダーの使用量を把握可
能にしている。タンク1の下部には所要量のパウダーを
継続して排出し、給送するための開閉ノ々ルブ3、エジ
ェクター4が接続されている。
FIG. 1 shows an overall view of the apparatus according to the present invention [(A) is for blooms and billets, (B) is for slabs], and 1 is for N2
It is a tank that is sealed to the extent that moisture absorption is prevented by blowing, and a powder 12 is stored inside, and an N2 conduit 2 is connected to the top, and N2 gas from which water has been removed is flowed from above into the powder of 1 yen in the tank. , In order to prevent the amount of powder from becoming sticky, it is also ejected from the bottom of the tank. Additionally, a load cell 6 is installed in the tank 1, making it possible to grasp the amount of powder used. Connected to the lower part of the tank 1 are an opening/closing knob 3 and an ejector 4 for continuously discharging and feeding a required amount of powder.

第2図は開閉ノ々ルブ3及びエジェクター4の詳細断面
図を示し、開閉ノ々ルブ3はパウダーの通路31と該通
路と枠体32との間に配設された弁33によって形成さ
れた気密室34および1核気密室に圧力気体を送るため
の導管35および第1図のタイマー36からの信号を受
けて開閉する三方電磁弁37と三方電磁弁38を備えて
いる。
FIG. 2 shows a detailed sectional view of the opening/closing knob 3 and the ejector 4, and the opening/closing knob 3 is formed by a powder passage 31 and a valve 33 disposed between the passage and the frame 32. It is equipped with a conduit 35 for sending pressurized gas to the airtight chamber 34 and one nuclear airtight chamber, and a three-way solenoid valve 37 and a three-way solenoid valve 38 that open and close in response to a signal from a timer 36 shown in FIG.

開閉ノ々ルブ3の作動は三方電磁弁37を入方向へ開、
三方電磁弁38を閉にすると各気密室34に圧力気体が
導入され各弁33が図中破線で示す如く圧接し通路31
が閉鎖する。三方電磁弁37を8方向へ開、三方電磁弁
38を開にすると気密室34内の圧力気体が外方へ吸引
され弁33が開く。エジェクター4は保持体41に装着
されたパウダーの分散部材42と該保持体41の上部に
螺会装着されたパウダーの貯溜槽43と、該保持体41
の下部に装着されたインジェクター内管71を備えてい
る。分散部材42は′W、3図〔(A)は拡大断面図、
(B)は平面図〕のように中央部に錐状突起部45が突
設され、該錐状朶起部の周りに複数の貫通孔46を備え
ている。錐状突起部45の頂部45aは排出口47の下
端乃至はこれより下方に位i推している。48は貯溜槽
43を保持体41に固定するための締付ナツト、49は
保持体41内部への外気の侵入を防止するためのOIJ
ソングある。
The opening/closing knob 3 is operated by opening the three-way solenoid valve 37 in the incoming direction.
When the three-way solenoid valve 38 is closed, pressurized gas is introduced into each airtight chamber 34, and each valve 33 is pressed against the passage 31 as shown by the broken line in the figure.
will be closed. When the three-way solenoid valve 37 is opened in eight directions and the three-way solenoid valve 38 is opened, the pressure gas in the airtight chamber 34 is sucked outward and the valve 33 is opened. The ejector 4 includes a powder dispersion member 42 attached to a holder 41, a powder reservoir 43 screwed to the upper part of the holder 41, and a powder reservoir 43 attached to the upper part of the holder 41.
It is equipped with an injector inner tube 71 attached to the lower part of the injector. The dispersion member 42 is 'W, Figure 3 [(A) is an enlarged sectional view,
(B) is a plan view], a conical protrusion 45 is protruded from the center, and a plurality of through holes 46 are provided around the conical protrusion. The top 45a of the conical projection 45 is located at or below the lower end of the discharge port 47. 48 is a tightening nut for fixing the storage tank 43 to the holding body 41, and 49 is an OIJ for preventing outside air from entering inside the holding body 41.
There's a song.

次にパウダー浮遊輸送手段について説明する。Next, the powder floating transportation means will be explained.

第1図において、5はエジェクター4に接続されたパウ
ダーの給送管、7A、7Bは給送管5内を通過中あるい
はエジェクター4を通過したパウダーを追送するための
インジェクターである。
In FIG. 1, 5 is a powder feeding pipe connected to the ejector 4, and 7A and 7B are injectors for feeding powder that is passing through the feeding pipe 5 or has passed through the ejector 4.

第4図はインジェクター7A、7Bの詳細図を示し、7
1は内管、72は外管、73は外管72に設けられた圧
力気体の導入管であり、外管72の内径は導管73に向
って拡大されておシ、該拡大部に内管71が挿入され、
該内管71を囲繞して圧力気体の通路74が形成され、
該通路74の先端部に圧力気体の噴出口としてのリング
状のノズル75が形成されている。なお内管71と外管
72の内径はほぼ同一である。
FIG. 4 shows a detailed diagram of the injectors 7A and 7B.
1 is an inner pipe, 72 is an outer pipe, and 73 is a pressure gas introduction pipe provided in the outer pipe 72. 71 is inserted,
A pressure gas passage 74 is formed surrounding the inner tube 71;
A ring-shaped nozzle 75 is formed at the tip of the passage 74 as a pressurized gas outlet. Note that the inner diameters of the inner tube 71 and the outer tube 72 are approximately the same.

導入管73から供給された圧力気体はリング状ノズル7
5から噴出し、この噴出により内管71内のパウダー1
2は外管72へ追送される。リング状ノズル75から噴
出した圧力気体は外管7゛2の内面に沿う気流となって
圧送されるため外管72内を送られるパウダーは気流に
包囲されながら送られ、外管内面と殆んど接触せず、該
内向との接触抵抗が非常に小さい。このためパウダーの
給送速度低下を最少限に抑えて給送することができ、ま
た外管72、給送管5の摩耗を防止できる。
Pressure gas supplied from the introduction pipe 73 passes through the ring-shaped nozzle 7
The powder 1 in the inner tube 71 is
2 is further sent to the outer tube 72. The pressurized gas ejected from the ring-shaped nozzle 75 is forced into an airflow along the inner surface of the outer tube 7゛2, so the powder sent inside the outer tube 72 is sent while being surrounded by the airflow, and is almost completely connected to the inner surface of the outer tube. There is no contact with the inward direction, and the contact resistance with the inward direction is very small. Therefore, the powder can be fed while minimizing a decrease in the powder feeding speed, and wear of the outer tube 72 and the feeding tube 5 can be prevented.

次に散布ノズルについて説明する。Next, the spray nozzle will be explained.

81はノズル本体、82は本体の長手方向に多数開口し
た排出口であシ、このような散布ノズル8が、前述のよ
うに第1図に示す通シ、注入ノズル11を囲んでかつ湯
面中央部に配置されている。
Reference numeral 81 denotes a nozzle main body, and reference numeral 82 indicates a number of discharge ports opening in the longitudinal direction of the main body.As mentioned above, such a dispersion nozzle 8 surrounds the through hole and injection nozzle 11 shown in FIG. It is located in the center.

パウダーは排出口82から長手方向に均等に排出され、
湯面中央部に落下し徐々に溶解しながら鋳型lOの内面
に向って均等に移動し鋳型縁に到達するまでに完全に溶
解して鋳片表面に供給される。
The powder is evenly discharged from the discharge port 82 in the longitudinal direction,
It falls to the center of the hot water surface and gradually melts while moving evenly toward the inner surface of the mold 10, and by the time it reaches the mold edge, it is completely melted and supplied to the surface of the slab.

このようにパウダーは湯面中央部にかつ連続的に散布さ
れるため鋳型縁においてパウダーの溶解に変動がなく、
完全に溶解したパウダーを常時供給可能である。
In this way, the powder is dispersed continuously at the center of the mold surface, so there is no fluctuation in powder dissolution at the mold edge.
Completely dissolved powder can be supplied at all times.

多孔ノズルでは、第7図(〜に示す如く、吐出流速1湾
/3以内にすると各ノズルより同量のパウダーが真下に
散布され、鋳型湯面上に均一散布される。
With multi-hole nozzles, if the discharge flow rate is within 1/3 bay, the same amount of powder will be sprayed directly below from each nozzle, as shown in Figure 7 (-), and will be uniformly spread over the mold surface.

従ってスラブ鋳片はもちろんのこと小断面サイズあるい
は異型鋳片に適したノズルといえる。
Therefore, it can be said that this nozzle is suitable not only for slab slabs but also for small cross-sectional sizes or irregularly shaped slabs.

第6図は散布ノズル(スリットノズル)の他の例を示す
拡大詳細図〔(A)は平面図、(B)は側面図〕で、8
1はノズル本体、82はスリット状に開口した排出口で
ある。本例のスリットノズルでは第7図@)K示す如く
、ノ々ウダー送り方向に傾斜して排出されるため小断面
サイズの鋳型には不都合な点があるが、スラブなど大断
面や長大な断面の鋳型に適用可能でLbシ、パウダーを
ノズル前方に散布できるため、ノズルの近設が困難な注
入ノズル周シを主体にして散布する場合は好都合である
FIG. 6 is an enlarged detailed view showing another example of a dispersion nozzle (slit nozzle) [(A) is a plan view, (B) is a side view], and 8
1 is a nozzle main body, and 82 is a slit-shaped discharge port. With the slit nozzle of this example, as shown in Fig. 7 @)K, the nozzle is ejected at an angle in the nozzle feed direction, which is inconvenient for molds with small cross-section sizes, but It can be applied to molds such as Lb, and the powder can be sprayed in front of the nozzle, so it is convenient when spraying mainly around the injection nozzle where it is difficult to install the nozzle close to it.

尚、第1図中、9は圧力調整器、lOは鋳型、11は注
入ノズルであシ湯面上中央部に配置されている。
In FIG. 1, 9 is a pressure regulator, 10 is a mold, and 11 is an injection nozzle, which are arranged at the center above the hot water surface.

本例では第1図の装置が注入ノズル11を囲むように設
けられている。
In this example, the apparatus shown in FIG. 1 is provided so as to surround the injection nozzle 11.

次に一連の作動を説明する。1ず鋳型10内に供給しよ
うとするパウダーの単位時間当りの量に基いてタイマー
36に開閉バルブ3の開閉タイミング、すなわち三方電
磁弁37.三方電磁弁3Bの開閉タイミングを設定し、
また貯溜(!!i3は所望量のパウダーを排出可能な口
径の排出口47を有したものを装着しておく。次に圧力
気体の)々ルブ13を開くとともにタイマー36のスイ
ッチ(図示せず)を入れると、タンクl内が力11圧さ
れるとともに開閉バルブ3が設定タイミングで開閉を繰
り返す。開閉バルブ1回の開放によシ貯溜槽43内にパ
ウダーがほぼ充満される。貯溜槽43内のパウダーは排
出口47から排出され錐状突起部45によって分散され
て複数の貫通孔46から分散状態で落下する。この落下
途中のパウダーはインジェクター7Aから噴出している
圧力気体によって給送管5内全圧送される。ノソウダー
は給送管内を浮遊状態で送られるが管長が長く、管内圧
損が大きい場合、給送管5内のパウダーはインジェクタ
ー7Bによって追込される。インジェクター7Bでは管
内周全面を管内面J妥さ方向に沿って流れる気流によっ
て、パウダーがこの気流に引き込まれ、浮遊輸送される
。このため・ξウダーを低速で送ることができ、散布ノ
ズル8から鋳型lO内に均等に散布される。貯溜槽43
内が空になると同時に開閉7′8′ルブ3が所定時間開
き前記同様にして貯溜槽43にパウダーが満され以下同
様(でシてパウダーが自動的に給送散布される、また貯
?*(4”!’I43にパウダーを満す手段として、タ
ンク1.開閉〕々ルゾ3の組付せによるものを示したが
、貯溜槽43を空にしないように供介、釘可能な手段で
あれば他の公知手段を採用可能である。
Next, a series of operations will be explained. First, the timer 36 determines the opening/closing timing of the opening/closing valve 3 based on the amount of powder to be supplied into the mold 10 per unit time, that is, the three-way solenoid valve 37. Set the opening and closing timing of the three-way solenoid valve 3B,
In addition, the reservoir (!!i3) is equipped with a discharge port 47 having a diameter capable of discharging the desired amount of powder.Next, open the pressure gas valve 13 and switch the timer 36 (not shown). ), the pressure inside the tank 1 is increased to 11, and the opening/closing valve 3 repeats opening and closing at the set timing. By opening the on-off valve once, the storage tank 43 is almost filled with powder. The powder in the storage tank 43 is discharged from the discharge port 47, dispersed by the conical protrusion 45, and falls from the plurality of through holes 46 in a dispersed state. This falling powder is completely pumped into the feed pipe 5 by the pressure gas jetting out from the injector 7A. The powder is sent in a floating state inside the feeding pipe, but if the pipe length is long and the pressure loss inside the pipe is large, the powder inside the feeding pipe 5 is driven in by the injector 7B. In the injector 7B, the powder is drawn into the airflow that flows along the entire inner circumference of the tube along the direction of the inner surface of the tube and is transported floatingly. Therefore, ξ powder can be sent at a low speed and is evenly sprayed from the spray nozzle 8 into the mold lO. Storage tank 43
At the same time as the inside is emptied, the opening/closing valve 3 opens for a predetermined period of time and the storage tank 43 is filled with powder in the same manner as described above. (4"!'I43 is filled with powder by assembling tank 1, opening/closing] and luzo 3, but in order to prevent the reservoir tank 43 from emptying, a means that can be inserted or nailed is used. If necessary, other known means can be used.

また給送管への圧力気体の噴出は、第8図のように給送
管5に圧力気体の噴出口6−1を設けたものでもまた錐
状突起部45は角錐等地の錐状体でもよい。なお分散部
材42におけるパウダーの流れをよくするには第3図(
A)に示す角度θを約200〜60°の範囲となるよう
に形成したり、あるいは貫通孔46を下床がりに形成す
るなどの方法がある。
In addition, the pressure gas can be ejected into the feed pipe by providing a pressure gas ejection port 6-1 in the feed pipe 5 as shown in FIG. But that's fine. In order to improve the flow of powder in the dispersing member 42, see FIG.
There are methods such as forming the angle θ shown in A) to be in the range of about 200 to 60 degrees, or forming the through hole 46 in the lower floor.

第9図、第10図はパウダー給送手段の他の実施例を示
し、第9図は貯溜槽43の上方にタンク1を直結し、開
閉ノ々ルブ3を省略したものである。
9 and 10 show other embodiments of the powder feeding means, in which the tank 1 is directly connected above the storage tank 43 and the opening/closing knob 3 is omitted.

開閉、sルプ3はその動作によジノぞウダーに衝撃を与
え詰シを防止する作用があるが、第1図に示した円盤1
4.圧力気体噴出管15によるパウダーの詰シ防止作用
を増すことにより省略tiJ’能である。
The opening and closing of the disk 3 has the effect of applying a shock to the cylinder and preventing jamming due to its operation, but the disk 1 shown in Fig. 1
4. This can be omitted by increasing the action of the pressure gas ejection pipe 15 to prevent clogging of powder.

第10図は、エジェクター4を省略し開閉バルブ3とイ
ンジェクター70とを直結したものである。
In FIG. 10, the ejector 4 is omitted and the on-off valve 3 and the injector 70 are directly connected.

この場合パウダー給送量の調節は開閉パルプ3の作動タ
イミングによって行う。
In this case, the amount of powder fed is adjusted by the timing of operation of the opening/closing pulp 3.

〔発明の効果〕〔Effect of the invention〕

従来、パウダー、特に顆粒状のパウダー全満足に給送散
布することができないため鋳造時の供給は殆んど人手に
よっており、適切量の供給ができずこのため鋳型内面と
鋳片間の潤滑不良に基づく鋳片表面欠陥がしばしば発生
していたが本発明により上記問題が解決できるとともに
給送管の摩耗を抑えることができ、また、高温、粉塵を
伴なう過酷な鋳造作業からも解放し得るものであシ鋳片
品質と作業環境の改善に格段の効果が得られるものであ
る。
Conventionally, powder, especially granular powder, could not be completely fed and dispersed, so most of the feeding during casting was done manually, and it was not possible to feed the appropriate amount, resulting in poor lubrication between the inside of the mold and the slab. However, the present invention can solve the above problems, suppress the wear of the feed pipe, and relieve the harsh casting work that involves high temperatures and dust. This will have a significant effect on improving the quality of slabs and the working environment.

また構成が簡電であるため故障の心配がなく、保守も容
易であシ、さらにはコンパクトであるたた作業の支障と
なることもなくスラブ鋳片はもちろんのこと小断面ある
いは異型鋳片の場合に更に効力を発揮するとともに最近
の自動化、機械化の有力な手段となりえるものである。
In addition, since the configuration is simple, there is no need to worry about breakdowns, and maintenance is easy.Furthermore, it is compact and does not interfere with folding work, so it can be used not only for slab slabs but also for small cross-section or irregular shaped slabs. In addition to being more effective in some cases, it can also become a powerful means of automation and mechanization in recent years.

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

第1図(A) 、 (B)は本発明か濃を実施するため
の輪置例を示す全体断面図、第2図は第1図の部分詳細
断面図、第3図は第2図の部分詳細図で、(A)は断面
図、(B)は平面図、第4図は第1図の部分詳細断面図
、第5図は散布ノズルの一例を示し、(A)は平面図、
(B)は(〜の八−入断面図、第6図は数曲ノズルの他
の例を示し、(A)は平]m図、(B)は側面図、を示
す断面図、第9図、第10図はパウダー給送手段の他の
実施例を示す断面図である。 図中。 14′iタンク、2は導管、3は開閉ノ々ルブ、4はエ
ジェクター、42は分散部材、43は貯溜槽、45は錐
状突起部、46は貫通孔、47は排出口、5はパウダー
給送管、6はノ々イブレータ−17N。 7Bはインジェクター、8はパウダー散布ノズル、10
は鋳型、11は注入ノズル、12はノミラグ−。 61は噴出口、75はリング状ノズル。 代理人 弁理士 秋 沢 政 光 他2名 第3図(A) 名3図(B) 84図 箔50(A) /8 第7図(A) 躬7図(B) 第8開 名ly図
Figures 1 (A) and (B) are overall cross-sectional views showing an example of rotation for carrying out the present invention, Figure 2 is a partial detailed cross-sectional view of Figure 1, and Figure 3 is a cross-sectional view of Figure 2. 4 is a partial detailed sectional view of FIG. 1; FIG. 5 is an example of a dispersion nozzle; (A) is a plan view;
(B) is a cross-sectional view of (~), FIG. Figure 10 is a sectional view showing another embodiment of the powder feeding means. 43 is a storage tank, 45 is a conical protrusion, 46 is a through hole, 47 is a discharge port, 5 is a powder feeding pipe, 6 is a nobbler 17N, 7B is an injector, 8 is a powder dispersion nozzle, 10
1 is a mold, 11 is an injection nozzle, and 12 is a chisel rag. 61 is a spout, and 75 is a ring-shaped nozzle. Agent Patent attorney Masamitsu Akizawa and 2 others Figure 3 (A) Figure 3 (B) Figure 84 Haku 50 (A) /8 Figure 7 (A) Figure 7 (B) Figure 8

Claims (1)

【特許請求の範囲】[Claims] (1) パウダーの給送手段及び浮遊輸送手段と、該浮
遊輸送手段に連なる給送管の終端に、−唱が閉塞された
管体の長手方向に複数の孔またはスリットを備えた散布
ノズルを連設したことを特徴とする連続鋳造におけるパ
ウダー自動散布装置。
(1) Powder feeding means and floating transportation means, and a dispersion nozzle equipped with a plurality of holes or slits in the longitudinal direction of the tube with the pipe closed at the end of the feeding pipe connected to the floating transportation means. An automatic powder dispersion device for continuous casting, which is characterized by being installed in series.
JP16246083A 1983-09-03 1983-09-03 Automatic spraying device for powder in continuous casting Granted JPS6054254A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16246083A JPS6054254A (en) 1983-09-03 1983-09-03 Automatic spraying device for powder in continuous casting

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16246083A JPS6054254A (en) 1983-09-03 1983-09-03 Automatic spraying device for powder in continuous casting

Publications (2)

Publication Number Publication Date
JPS6054254A true JPS6054254A (en) 1985-03-28
JPH0470109B2 JPH0470109B2 (en) 1992-11-10

Family

ID=15755034

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16246083A Granted JPS6054254A (en) 1983-09-03 1983-09-03 Automatic spraying device for powder in continuous casting

Country Status (1)

Country Link
JP (1) JPS6054254A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6449349U (en) * 1987-09-14 1989-03-27
JPH0454551U (en) * 1990-09-10 1992-05-11
KR100831350B1 (en) 2006-11-28 2008-05-21 주식회사 포스코 Apparatus for supplying flux

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5114208U (en) * 1974-07-16 1976-02-02
JPS5725448A (en) * 1980-07-22 1982-02-10 Teijin Ltd High bulky knitted fabric

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5114208U (en) * 1974-07-16 1976-02-02
JPS5725448A (en) * 1980-07-22 1982-02-10 Teijin Ltd High bulky knitted fabric

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6449349U (en) * 1987-09-14 1989-03-27
JPH0222120Y2 (en) * 1987-09-14 1990-06-14
JPH0454551U (en) * 1990-09-10 1992-05-11
KR100831350B1 (en) 2006-11-28 2008-05-21 주식회사 포스코 Apparatus for supplying flux

Also Published As

Publication number Publication date
JPH0470109B2 (en) 1992-11-10

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