JPH08206878A - Production of fused flux for welding and apparatus therefor - Google Patents

Production of fused flux for welding and apparatus therefor

Info

Publication number
JPH08206878A
JPH08206878A JP1371795A JP1371795A JPH08206878A JP H08206878 A JPH08206878 A JP H08206878A JP 1371795 A JP1371795 A JP 1371795A JP 1371795 A JP1371795 A JP 1371795A JP H08206878 A JPH08206878 A JP H08206878A
Authority
JP
Japan
Prior art keywords
water
flux
welding
trough
bulk density
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
JP1371795A
Other languages
Japanese (ja)
Other versions
JP3350268B2 (en
Inventor
Takashi Nukaga
孝 額賀
Kiyobumi Konishi
清文 小西
Hiroyuki Fujii
浩之 藤井
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 Welding and Engineering Co Ltd
Original Assignee
Nippon Steel Welding and Engineering Co Ltd
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 Welding and Engineering Co Ltd filed Critical Nippon Steel Welding and Engineering Co Ltd
Priority to JP01371795A priority Critical patent/JP3350268B2/en
Publication of JPH08206878A publication Critical patent/JPH08206878A/en
Application granted granted Critical
Publication of JP3350268B2 publication Critical patent/JP3350268B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Disintegrating Or Milling (AREA)
  • Nonmetallic Welding Materials (AREA)

Abstract

PURPOSE: To provide a process for producing a fused flux for welding capable of producing a fused flux having from a low bulk density to a high bulk density at a uniform shape and bulk density with the same apparatus and an apparatus therefor. CONSTITUTION: This process for producing the fused flux for welding and the apparatus therefor comprise cooling and pulverizing the fused flux 8 charged at the front of the injection hole of an injector disposed at one end of a cylindrical trough 1 by jet water 6 injected from this injection hole and discharging the pulverized flux from the trough. The fused flux is cooled and pulverized by adjusting the pressure of the jet water 6 and the temp. of transporting water 16 according to the desired shape and the bulk density.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、溶接用溶融型フラック
スの製造方法および装置に係り、さらに詳しくは、所望
の形状および嵩密度の溶接用溶融型フラックスを製造す
る技術に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for producing a molten flux for welding, and more particularly to a technique for producing a molten flux for welding having a desired shape and bulk density.

【0002】[0002]

【従来の技術】溶融フラックスを冷却し粉砕して粒状フ
ラックスを製造する方法の1つにジェット水砕法と呼ば
れている方法があり、この方法が適用されている装置を
図4と図5に示す。図4は従来の水砕装置を示す概略
図、図5は図4のb−b′断面図である。
2. Description of the Related Art A method called a jet water granulation method is one of the methods for producing a granular flux by cooling and crushing a molten flux, and an apparatus to which this method is applied is shown in FIGS. Show. FIG. 4 is a schematic view showing a conventional water granulator, and FIG. 5 is a sectional view taken along the line bb 'of FIG.

【0003】これらの図において、2はトラフ1の一端
に設けたジェット水噴射装置、10はトラフ1の他端の
排出口、5は圧力水供給パイプ、4はノズルボックス3
の前側に設けたスリット式噴射孔、7は水流調整板、6
は水流調整板より案内されて出てきたジェット水であ
る。8は溶融フラックス(以下、溶湯という。)。9は
溶湯を投入する投入口、11は排出された水と粒状フラ
ックスの混合物である。
In these figures, 2 is a jet water injection device provided at one end of the trough 1, 10 is a discharge port at the other end of the trough 5, 5 is a pressure water supply pipe, and 4 is a nozzle box 3.
Slit type injection hole provided on the front side of the, 7 is a water flow adjusting plate, 6
Is jet water that is guided out from the water flow adjusting plate. Reference numeral 8 is a molten flux (hereinafter referred to as molten metal). Reference numeral 9 is a charging port for charging molten metal, and 11 is a mixture of discharged water and granular flux.

【0004】この装置において電気炉等で溶解した溶湯
8を電気炉から直接に、又は一旦取り鍋に受け、あるい
はタンデッシュを通して、トラフ1内の噴射装置2の噴
射孔4の前方に投入すると、投入された溶湯8は水平
に、又は傾斜して設置してある噴射孔4からのジェット
水6に衝突し冷却され、かつ砕かれ、そしてトラフ1内
を水とともに排出口10から排出される。このような従
来の水砕装置では、例えば水圧2〜5kg/m2 の圧力水
が用いられ嵩密度が0.8〜2.0g/cm3 と比較的重
い軽石状、及びガラス状のフラックスが製造される。
In this apparatus, when the molten metal 8 melted in an electric furnace or the like is thrown directly from the electric furnace, once received in a ladle, or through a tundish, in front of the injection hole 4 of the injection device 2 in the trough 1, the injection is performed. The molten metal 8 collides with the jet water 6 from the injection hole 4 installed horizontally or inclined, is cooled and crushed, and is discharged from the discharge port 10 together with water in the trough 1. In such a conventional water granulator, for example, pressure water having a water pressure of 2 to 5 kg / m 2 is used, and a bulky density of 0.8 to 2.0 g / cm 3 and relatively heavy pumiceous and glassy fluxes are generated. Manufactured.

【0005】しかし、従来の水砕装置を使った製造方法
では、ジェット水噴出口がスリット式の孔であるので、
噴出口から出たジェット水は左右方向の水流が一定せ
ず、溶湯全体に均一な水圧で当たることがないので形状
に差が出たり、嵩密度が不均一になる。
However, in the conventional manufacturing method using the water granulator, since the jet water jet port is a slit type hole,
The jet water discharged from the jet outlet does not have a constant water flow in the left-right direction and does not hit the entire melt with a uniform water pressure, resulting in a difference in shape and non-uniform bulk density.

【0006】電気炉などからトラフ1の投入口9へ投入
された溶湯は、出湯初期の温度が1500℃〜1600
℃、終期の温度が1300℃〜1500℃と低くなる。
水砕されたフラックスは高温時に嵩密度が低くなり低温
時は、嵩密度が高くなるのでトラフ1の排出口10から
排出された水砕フラックスは嵩密度が不均一となる。
The temperature of the molten metal charged into the trough 1 through the inlet 9 from an electric furnace has an initial temperature of 1500 ° C. to 1600 ° C.
C, the temperature at the end of the period becomes as low as 1300 ° C to 1500 ° C.
The granulated flux has a low bulk density at a high temperature and a high bulk density at a low temperature, so that the granulated flux discharged from the discharge port 10 of the trough 1 has a non-uniform bulk density.

【0007】又、フラックスの粒子を大きくしようとし
て、水圧を低くするとトラフ内に高温のフラックスが溜
まり、水蒸気爆発を誘発することがあり、フラックス粒
子を大きくすることが困難である。
Further, if the water pressure is lowered to increase the size of the flux particles, a high temperature flux may be accumulated in the trough to induce a steam explosion, and it is difficult to increase the size of the flux particles.

【0008】よって、目標とする形状及び嵩密度が異な
る溶融型フラックスを製造するごとに、例えば針状フラ
ックス(ガラス状で針状フラックスが多く比較的嵩密度
が低いもの)の場合は、前記ジェット水砕方法、軽石状
フラックスの場合は特開昭56−84348号公報に記
載の水槽表面に加圧水を放出しながら溶融フラックスを
投入する方法、及びガラス状フラックスの場合は水槽内
の水を撹拌しながら溶融フラックスを投入する方法等と
に冷却粉砕方法を変える必要があった。
Therefore, each time a molten flux having a different target shape and bulk density is produced, for example, in the case of a needle-like flux (a glass-like flux with many needle-like fluxes and a relatively low bulk density), the jet Water granulation method, in the case of pumice-like flux, a method of charging molten flux while releasing pressurized water to the surface of the water tank described in JP-A-56-84348, and in the case of glassy flux, stirring water in the water tank. However, it was necessary to change the cooling and pulverizing method to a method of introducing molten flux.

【0009】[0009]

【発明が解決しようとする課題】このような技術の現状
にかんがみ、本発明は嵩密度が0.4〜2.0g/cm3
という低い嵩密度から高い嵩密度まで、また、針状、ガ
ラス状、及び、軽石状フラックスと形状の異なる溶融型
フラックスを、同一の設備で、形状、嵩密度のバラツキ
が少ない溶融型フラックスを製造する装置、及び、方法
を提供するものである。
In view of the current state of the art, the present invention has a bulk density of 0.4 to 2.0 g / cm 3.
From low bulk density to high bulk density, in addition to needle-shaped, glass-shaped, and pumice-shaped flux, melt type flux with different shape is manufactured with the same equipment, with less variation in shape and bulk density. Apparatus and method.

【0010】[0010]

【課題を解決するための手段】本発明の要旨とするとこ
ろは、円筒形トラフの一端に設けた噴射装置の噴射孔前
方に投入された溶融型フラックスを、該噴射孔から噴射
したジェット水で冷却粉砕してトラフから排出する溶接
用溶融型フラックスの製造方法において、所望の形状お
よび嵩密度に応じてジェット水の圧力および搬送水の水
温を調節して冷却粉砕することを特徴とする溶接用フラ
ックスの製造方法であり、また、円筒形トラフの一端に
設けた噴射装置の噴射孔前方に投入された溶融型フラッ
クスを、該噴射孔から噴射したジェット水で冷却粉砕し
てトラフから排出する溶接用溶融型フラックスの製造装
置において、水の圧力調節装置にこれと連設したジェッ
ト水噴射装置を設け、該噴射装置にはジェット水噴射孔
が水平方向に丸孔で上下左右に間隔を有して複数列設け
てあり、かつ噴射孔の下部に温度調節装置と連設された
半円状の搬送水口を設けてなることを特徴とする溶接用
フラックスの製造装置である。
SUMMARY OF THE INVENTION The gist of the present invention is that a molten flux injected in front of an injection hole of an injection device provided at one end of a cylindrical trough is jet water injected from the injection hole. In a method for producing a molten flux for welding, which is cooled and pulverized and discharged from a trough, the welding is characterized by cooling and pulverizing by adjusting the pressure of jet water and the temperature of carrier water according to the desired shape and bulk density. Welding method for producing a flux, in which molten-type flux injected in front of an injection hole of an injection device provided at one end of a cylindrical trough is cooled and pulverized by jet water injected from the injection hole and discharged from the trough In a manufacturing apparatus for molten flux for jet, a water pressure adjusting device is provided with a jet water injection device connected to the water pressure adjusting device, and the jet water injection hole has a horizontal hole in a horizontal direction. A welding flux manufacturing apparatus characterized in that a plurality of rows are provided at intervals in the vertical and horizontal directions, and a semicircular carrier water port connected to a temperature control device is provided below the injection hole. is there.

【0011】[0011]

【作用】まず、図面により本発明のフラックス製造装置
について説明する。図1は本願発明装置の主要部を示す
側面図、図2は図1のa−a′断面図、図3は本発明装
置の概要を示す図である。
First, the flux producing apparatus of the present invention will be described with reference to the drawings. 1 is a side view showing the main part of the device of the present invention, FIG. 2 is a sectional view taken along the line aa 'in FIG. 1, and FIG. 3 is a diagram showing an outline of the device of the present invention.

【0012】図1に示すフラックス製造装置の主要部は
円筒形のトラフ1とトラフ1の一端に設けたジェット水
噴射装置2とからなり、ジェット水噴射装置2はノズル
板13の上部に設けた噴射孔14、噴射孔14の下辺か
ら前方に向かって延出している水流調整板7とさらに水
流調整板7の下部に設けた搬送水口15とからなってい
る。噴射孔14は水平方向に丸孔で上下、左右に間隔を
有して複数列設けてあり、噴射孔14の下部には温度調
節装置(図示しない)と連設されたは半円状の搬送水口
15を開口している。
The main part of the flux producing apparatus shown in FIG. 1 comprises a cylindrical trough 1 and a jet water jetting device 2 provided at one end of the trough 1. The jet water jetting device 2 is provided above a nozzle plate 13. It is composed of an injection hole 14, a water flow adjusting plate 7 extending forward from the lower side of the injection hole 14, and a carrier water port 15 provided below the water flow adjusting plate 7. The injection holes 14 are horizontally circular holes and are provided in a plurality of rows at intervals vertically and horizontally. Below the injection holes 14, a temperature control device (not shown) is connected to form a semicircular conveyance. The water port 15 is opened.

【0013】溶解炉12から溶湯8が投入口9を経て投
入され、噴射装置2のノズル板13上部の噴射孔14か
ら噴射されたジェット水6に衝突して冷却され粉砕され
る。粉砕されたフラックスはトラフ1内を搬送水口15
から送られる搬送水16と共にトラフ1先端の排水口1
0から水砕フラックス11として排出され、受槽21か
らコンベア22を経て次工程へ送られる。図中17は圧
力装置であって、供給水を加圧する。18は水量装置、
19は水温計装置、20は搬送水パイプである。
Molten metal 8 is poured from a melting furnace 12 through a charging port 9, collides with jet water 6 sprayed from a spray hole 14 in an upper portion of a nozzle plate 13 of a spraying device 2, and is cooled and crushed. The crushed flux is carried in the trough 1 by the water port 15
Drain port 1 at the tip of trough 1 together with carrier water 16 sent from
It is discharged as a granulated flux 11 from 0, and is sent to the next step from the receiving tank 21 via the conveyor 22. Reference numeral 17 in the figure is a pressure device for pressurizing the supply water. 18 is a water quantity device,
Reference numeral 19 is a water temperature measuring device, and 20 is a carrier water pipe.

【0014】本発明のフラックス製造方法および装置に
よれば、ジェット水圧力調節装置2が設けてあるので、
ジェット水の圧力の調節で各種形状のフラックスの製造
が可能である。ジェット水噴射孔14が丸孔で上下左右
に隔てて複数列設けてあるので、上下左右ともジェット
水流が一定となり投入された溶湯8全体にジェット水が
均一に当たり、同一の形状で嵩密度の均一なフラックス
11を製造できる。
According to the flux manufacturing method and apparatus of the present invention, since the jet water pressure adjusting device 2 is provided,
It is possible to manufacture flux of various shapes by adjusting the pressure of jet water. Since the jet water injection holes 14 are circular holes and are provided in a plurality of rows separated vertically and horizontally, the jet water flow is constant both vertically and horizontally, and the jet water is uniformly applied to the entire molten metal 8 that has been injected, and the same shape and a uniform bulk density. It is possible to manufacture a different flux 11.

【0015】ジェット水噴射孔14の下部には搬送水口
15が設けてあるので、トラフ1内のフラックス11は
排出口10へ排出されトラフ内に溜まることがないので
水蒸気爆発の危険がない。また、搬送水は水温の調節が
可能であり、出湯温度に応じて搬送水温度を調節するこ
とにより、同一の形状で嵩密度の均一なフラックスを製
造できる。なお、搬送水の流量も目標とするフラックス
形状および嵩密度に応じて調節すればさらに均一なフラ
ックスが得られる。
Since the carrier water port 15 is provided below the jet water injection hole 14, the flux 11 in the trough 1 is not discharged to the discharge port 10 and accumulated in the trough, so that there is no danger of steam explosion. Further, the temperature of the carrier water can be adjusted, and by adjusting the temperature of the carrier water according to the hot water discharge temperature, a flux having the same shape and a uniform bulk density can be produced. A more uniform flux can be obtained by adjusting the flow rate of the carrier water according to the target flux shape and bulk density.

【0016】本発明の溶接用フラックス製造装置として
は、トラフ径300〜800mm、丸孔径5〜12mmで上
下左右のとなりあう間隔20〜40mm、丸孔列数4〜8
列、丸孔数40〜70個であり、半円状の搬送水口はト
ラフ底部から50〜200mm、ジェット水圧力0.5〜
8kg/cm2 、搬送水温度調節範囲常温〜90℃であるこ
とが好ましい。
The welding flux producing apparatus of the present invention has a trough diameter of 300 to 800 mm, a round hole diameter of 5 to 12 mm, and an interval of 20 to 40 mm in which the vertical and horizontal directions are aligned, and the number of round hole rows is 4 to 8.
Rows, the number of round holes is 40 to 70, the semicircular carrier water port is 50 to 200 mm from the trough bottom, and the jet water pressure is 0.5 to
It is preferable that the temperature range of the carrier water is 8 kg / cm 2 , and the temperature range of the carrier water is from room temperature to 90 ° C.

【0017】次に、本発明の方法および装置によるフラ
ックス形状および嵩密度のコントロールの例を示すと、
針状フラックスで嵩密度1.1〜1.7g/cm3 の場合
はジェット水圧力を高くし、ガラス状フラックスで嵩密
度1.3〜2.0g/cm3 の場合はジェット水圧力を低
くし搬送水量を多く水温は低くする。軽石状フラックス
で嵩密度が非常に低い0.4〜0.8g/cm3 の場合は
ジェット水の圧力は低圧とし搬送水の水温は出湯温度の
低下とともに高くする。同じく軽石状フラックスで嵩密
度が0.8〜1.3g/cm3 の場合はジェット水の圧力
を中圧とし搬送水と水温は出湯温度の低下とともに高く
する。
Next, an example of controlling the flux shape and bulk density by the method and apparatus of the present invention will be described.
When the needle-like flux has a bulk density of 1.1 to 1.7 g / cm 3 , the jet water pressure is increased. When the glassy flux has a bulk density of 1.3 to 2.0 g / cm 3 , the jet water pressure is lowered. Increase the amount of water to be carried and lower the water temperature. In the case of pumice-like flux with a very low bulk density of 0.4 to 0.8 g / cm 3 , the jet water pressure is low and the temperature of the carrier water is increased as the tapping temperature decreases. Similarly, in the case of pumice-like flux with a bulk density of 0.8 to 1.3 g / cm 3 , the pressure of jet water is set to medium pressure, and the temperature of the carrier water and the water temperature are increased as the tapping temperature decreases.

【0018】[0018]

【実施例】以下実施例により本発明をさらに詳細に説明
する。まず、表1に示す目標組成、形状および目標嵩密
度のフラックスを各種原材料を配合して電気炉で溶解
し、図1および図4に示す装置で目標の形状および嵩密
度となるように各3000kg試作した。それらの結果を
表2に示す。
The present invention will be described in more detail with reference to the following examples. First, various fluxes having the target composition, shape and target bulk density shown in Table 1 are mixed with various raw materials and melted in an electric furnace, and 3000 kg of each is prepared by the apparatus shown in FIGS. 1 and 4 so that the target shape and bulk density are obtained. I made a prototype. Table 2 shows the results.

【0019】なお、実施例に用いた図1の装置は、トラ
フ径400mm、丸孔径8mm、丸孔の上下左右のとなり合
う間隔30mm、丸孔の列6列、丸孔数50個で半円状の
搬送水口はトラフ底部から90mmとし、図4の装置はト
ラフ径400mm、スリット式噴射孔幅10mmでスリット
は3列設けた。
The apparatus shown in FIG. 1 used in the embodiment is a semicircle with a trough diameter of 400 mm, a round hole diameter of 8 mm, a gap of 30 mm between the upper, lower, left and right of the round holes, 6 rows of round holes, and 50 round holes. The shape of the water transfer port is 90 mm from the bottom of the trough, and the apparatus of FIG. 4 has a trough diameter of 400 mm, a slit type injection hole width of 10 mm and three rows of slits.

【0020】[0020]

【表1】 [Table 1]

【0021】[0021]

【表2】 [Table 2]

【0022】表2において、No.1〜4が本発明による
溶融型フラックスの製造例、No.5〜8が比較例であ
る。本発明によるNo.1〜4は、フラックスの目標形
状、嵩密度および湯温に合わせてジェット水圧力と搬送
水温度を調節してあるので、それぞれ目標とする形状お
よび均一な嵩密度のフラックスが得られており極めて満
足な結果であった。
In Table 2, No. Nos. 1 to 4 are production examples of the molten flux according to the present invention, No. 5 to 8 are comparative examples. No. according to the present invention. In Nos. 1 to 4, the jet water pressure and the carrier water temperature are adjusted according to the target shape of the flux, the bulk density and the hot water temperature, so that the flux having the target shape and the uniform bulk density is obtained, respectively. It was a satisfactory result.

【0023】比較例中No.5は本発明装置を用いている
が、またNo.8は従来の装置であり搬送水がないので、
トラフ内にフラックスが溜まり水蒸気爆発の危険が生じ
たので中止した。No.6およびNo.7は、目標とする形
状は得られたが、ジェット水噴射がスリット式噴射孔で
あるので、ジェット水流が一定とならず、また水温を調
節した搬送水がないので嵩密度が不均一となった。
No. in Comparative Example No. 5 uses the apparatus of the present invention, but No. 5 is used. No. 8 is a conventional device and there is no carrier water,
Flux was accumulated in the trough and there was a danger of steam explosion, so it was discontinued. No. 6 and No. In No. 7, the target shape was obtained, but since the jet water jet was a slit type jet hole, the jet water flow was not constant, and there was no carrier water whose water temperature was adjusted, so the bulk density became non-uniform. It was

【0024】[0024]

【発明の効果】以上詳述したように、本発明の溶接用溶
融型フラックスの製造方法および装置によれば、低い嵩
密度から高い嵩密度の溶融型フラックスを同一の装置で
形状および嵩密度を均一に製造できるので、溶接用溶融
型フラックスの生産性および高品質化に大きく寄与する
ものである。
As described above in detail, according to the method and apparatus for manufacturing a molten flux for welding of the present invention, the molten flux having a low bulk density to a high bulk density can be formed in the same shape and bulk density. Since it can be manufactured uniformly, it greatly contributes to the productivity and quality improvement of the molten flux for welding.

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

【図1】本発明の溶接用溶融型フラックス装置の主要部
を示す説明図である。
FIG. 1 is an explanatory diagram showing a main part of a melting type flux device for welding according to the present invention.

【図2】図1のa−a′断面図を示す。FIG. 2 is a sectional view taken along the line aa ′ of FIG.

【図3】本発明の溶接用溶融型フラックス装置1例の概
略図を示す。
FIG. 3 shows a schematic view of an example of a melting type flux device for welding of the present invention.

【図4】従来の溶接用溶融型フラックス装置の主要図を
示す。
FIG. 4 shows a main view of a conventional fusion type flux device for welding.

【図5】図4のb−b′断面図を示す。5 is a cross-sectional view taken along the line bb 'of FIG.

【符号の説明】[Explanation of symbols]

1 トラフ 2 ジェット水噴射装置 3 ノズルボックス 4 スリット式噴射装置 5 圧力水供給パイプ 6 ジェット水 7 水流調整板 8 溶融フラックス(溶湯) 9 溶融フラックス投入口 10 排出口 11 水砕フラックス 12 溶融炉 13 ノズル板 14 噴射孔 15 搬送水口 16 搬送水 17 圧力装置 18 水量装置 19 水温計装置 20 搬送水パイプ 21 受槽 22 コンベア 1 Trough 2 Jet Water Injector 3 Nozzle Box 4 Slit Type Injector 5 Pressure Water Supply Pipe 6 Jet Water 7 Water Flow Adjustment Plate 8 Melt Flux 9 Molten Flux Inlet 10 Discharge Port 11 Water Flux 12 Melt Furnace 13 Nozzle Plate 14 Injection hole 15 Conveying water port 16 Conveying water 17 Pressure device 18 Water amount device 19 Water temperature measuring device 20 Conveying water pipe 21 Receiving tank 22 Conveyor

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 円筒形トラフの一端に設けた噴射装置の
噴射孔前方に投入された溶融型フラックスを、該噴射孔
から噴射したジェット水で冷却粉砕してトラフから排出
する溶接用溶融型フラックスの製造方法において、所望
の形状および嵩密度に応じてジェット水の圧力および搬
送水の水温を調節して冷却粉砕することを特徴とする溶
接用溶融型フラックスの製造方法。
1. A fusion type flux for welding, wherein a fusion type flux injected in front of an injection hole of an injection device provided at one end of a cylindrical trough is cooled and pulverized by jet water injected from the injection hole and discharged from the trough. 2. The method for producing a molten flux for welding, which comprises cooling and pulverizing by adjusting the pressure of jet water and the temperature of carrier water according to a desired shape and bulk density.
【請求項2】 円筒形トラフの一端に設けた噴射装置の
噴射孔前方に投入された溶融型フラックスを、該噴射孔
から噴射したジェット水で冷却粉砕してトラフから排出
する溶接用溶融型フラックスの製造装置において、水の
圧力調節装置に連設されたジェット水噴射装置を設け、
該噴射装置のジェット水噴射孔が水平方向に丸孔で上下
左右に間隔を有して複数列設けてあり、かつ噴射孔の下
部に温度調節装置と連設された半円状の搬送水口を設け
てなることを特徴とする溶接用溶融型フラックスの製造
装置。
2. A molten flux for welding, which melts and melts a molten flux that has been injected in front of an injection hole of an injection device provided at one end of a cylindrical trough by cooling and pulverizing with jet water injected from the injection hole and discharging from the trough. In the manufacturing apparatus of, the jet water injection device connected to the water pressure adjusting device is provided,
The jet water jet holes of the jetting device are horizontally arranged in a plurality of rows in the form of round holes at intervals in the vertical and horizontal directions, and a semicircular carrier water port connected to the temperature control device is provided below the jet holes. An apparatus for producing a molten flux for welding, which is characterized by being provided.
JP01371795A 1995-01-31 1995-01-31 Method and apparatus for producing molten flux for welding Expired - Fee Related JP3350268B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP01371795A JP3350268B2 (en) 1995-01-31 1995-01-31 Method and apparatus for producing molten flux for welding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP01371795A JP3350268B2 (en) 1995-01-31 1995-01-31 Method and apparatus for producing molten flux for welding

Publications (2)

Publication Number Publication Date
JPH08206878A true JPH08206878A (en) 1996-08-13
JP3350268B2 JP3350268B2 (en) 2002-11-25

Family

ID=11841004

Family Applications (1)

Application Number Title Priority Date Filing Date
JP01371795A Expired - Fee Related JP3350268B2 (en) 1995-01-31 1995-01-31 Method and apparatus for producing molten flux for welding

Country Status (1)

Country Link
JP (1) JP3350268B2 (en)

Also Published As

Publication number Publication date
JP3350268B2 (en) 2002-11-25

Similar Documents

Publication Publication Date Title
CN101332511B (en) Injection apparatus, injection molding atomizing chamber and injection molding method
US3752611A (en) Apparatus for producing metal powder
CN107427927B (en) Nozzle and tundish device for granulating molten material
SU1745106A3 (en) Method for producing powder, mainly amorphous, and plant for its accomplishment
JPS5676235A (en) Granulator
GB2148330A (en) Improvements in or relating to the granulation of slag
EP3126079B1 (en) Granulation of molten ferrochromium
JPH08206878A (en) Production of fused flux for welding and apparatus therefor
JPS6141707A (en) Apparatus for producing powder metal
JPH10305393A (en) Manufacture of welding flux and apparatus therefor
US7093463B1 (en) Method and device for producing powders that consist of substantially spherical particles
US4220441A (en) Apparatus for making prills from melted substance
JPH05311213A (en) Production of water granulated slag
JP2930655B2 (en) Method and apparatus for producing spherical slag
JP2019214786A (en) Manufacturing method and manufacturing apparatus of metal powder
JPH019638Y2 (en)
CN215279882U (en) Flow guiding device for cold bed smelting type gas atomization powder making
CN114850481B (en) Metal powder manufacturing device
KR100469019B1 (en) method and apparatus for producing fine metal spheres using atomizing by gas flame
JPS5919533A (en) Granulation of molten substance
JPH0656445A (en) Melt-spraying burner and production of molten spherical particle using the burner
JPS58130122A (en) Grinding method of magnetic glass
SU963966A1 (en) Method and apparatus for producing slag
SU1038307A1 (en) Apparatus for utilizing heat of molten slag
JPS61118131A (en) Combustion furnace apparatus for manufacturing thermal sprayed spherical particles

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees