TWI770616B - Nozzle structure on liquid steel distributor and continuous casting method - Google Patents
Nozzle structure on liquid steel distributor and continuous casting method Download PDFInfo
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- TWI770616B TWI770616B TW109133031A TW109133031A TWI770616B TW I770616 B TWI770616 B TW I770616B TW 109133031 A TW109133031 A TW 109133031A TW 109133031 A TW109133031 A TW 109133031A TW I770616 B TWI770616 B TW I770616B
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D41/00—Casting melt-holding vessels, e.g. ladles, tundishes, cups or the like
- B22D41/50—Pouring-nozzles
- B22D41/58—Pouring-nozzles with gas injecting means
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D1/00—Treatment of fused masses in the ladle or the supply runners before casting
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/10—Supplying or treating molten metal
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/10—Supplying or treating molten metal
- B22D11/11—Treating the molten metal
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D41/00—Casting melt-holding vessels, e.g. ladles, tundishes, cups or the like
- B22D41/14—Closures
- B22D41/16—Closures stopper-rod type, i.e. a stopper-rod being positioned downwardly through the vessel and the metal therein, for selective registry with the pouring opening
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D41/00—Casting melt-holding vessels, e.g. ladles, tundishes, cups or the like
- B22D41/50—Pouring-nozzles
Abstract
本發明係提供一種可以在鋼液分配器內使夾雜物浮起的鋼液分配器上噴嘴結構體及連續鑄造方法。在本發明中,係在鋼液分配器上噴嘴(11)的上端部外周之一部分或全周,具備比該鋼液分配器上噴嘴上端部的外形更大的凸鍔狀物(12);並且在凸鍔狀物(12)之下面、外周面、上面、及比凸鍔狀物(12)還下方之鋼液分配器上噴嘴(11)的外周面之其中任一個面或複數個面,具備一個或複數個氣體吐出孔(13a)。藉由在該鋼液分配器上噴嘴結構體中調整長度(L),來使氣體大致全部浮起、或調整氣體往內孔側下方的流量與浮起的量。The present invention provides a nozzle structure on a molten steel distributor capable of floating inclusions in the molten steel distributor, and a continuous casting method. In the present invention, a part or the whole circumference of the upper end of the upper nozzle (11) of the molten steel distributor is provided with a convex collar (12) larger than the outer shape of the upper end of the upper nozzle of the molten steel distributor; And any one or a plurality of surfaces below the convex collar (12), the outer peripheral surface, the upper surface, and the outer peripheral surface of the upper nozzle (11) of the molten steel distributor that is lower than the convex collar (12). , with one or a plurality of gas discharge holes (13a). By adjusting the length (L) of the upper nozzle structure of the molten steel distributor, substantially all the gas is floated, or the flow rate of the gas to the lower side of the inner hole and the amount of the float are adjusted.
Description
本發明係關於一種具備吹氣功能(gas blowing function)的鋼液分配器上噴嘴(tundish upper nozzle)結構體及連續鑄造方法。The present invention relates to a tundish upper nozzle structure with gas blowing function and a continuous casting method.
在鋼的連續鑄造中,大都是進行從鋼液分配器上噴嘴吹入氣體的作業。該氣體的吹入,主要是以如下作為目的。 (1)使氣泡從鋼液分配器上噴嘴的內孔朝向下方流動,藉此抑制朝向該鋼液分配器上噴嘴或者其下方的噴嘴之內孔面的夾雜物之附著或藉由夾雜物之附著所致的內孔閉塞。 (2)從鋼液分配器上噴嘴的下方抑制模具(mold)內的熔融鋼之流動形態。 (3)在鋼液分配器上噴嘴的下方或者模具內使夾雜物浮起。 (4)在鋼液分配器內使夾雜物浮起。 此等,係對鑄造作業的穩定性或生產性、鑄造板坯(casting slab)的品質帶來影響。In the continuous casting of steel, the operation of blowing gas from a nozzle on a molten steel distributor is mostly performed. The blowing of this gas is mainly aimed at the following. (1) Air bubbles flow downward from the inner hole of the upper nozzle of the molten steel distributor, thereby suppressing the adhesion of inclusions toward the inner hole surface of the upper nozzle of the molten steel distributor or the inner hole surface of the nozzle below it, or by the inclusion of inclusions. Inner pore occlusion due to attachment. (2) The flow pattern of molten steel in the mold is suppressed from below the nozzle on the molten steel distributor. (3) The inclusions are floated under the nozzle of the molten steel distributor or in the mold. (4) The inclusions are floated in the molten steel distributor. These influence the stability and productivity of casting operations, and the quality of casting slabs.
關於前述(1)至(4),係以習知的各種形態進行來自鋼液分配器上噴嘴的氣體吐出。
主要關於前述(1)至(3),例如在專利文獻1,係有提出以下的結構:在鋼液分配器上噴嘴的內孔設置氣體吐出用的多孔部(porous part),並且設置於鋼液分配器上噴嘴之上端部外周的環狀耐火物之環狀凸鍔(annular collar)部是覆蓋該鋼液分配器上噴嘴的上部。藉此,就能設成可以確實地進行往鋼液分配器上噴嘴之內孔的氣體供應。Regarding the above (1) to (4), the gas discharge from the nozzle on the molten steel distributor is performed in various conventional forms.
Mainly regarding the above (1) to (3), for example, in
又在專利文獻2,係以防止夾雜物或母金屬(parent metal)附著於止塞桿(stopper)與上噴嘴的接觸部近旁,且能進行穩定的流量控制來獲得良好的鑄造板坯作為目的,而提出一種鋼液分配器底部的止塞桿承接用噴嘴,其特徵在於:以與止塞桿的接觸部作為邊界而在其上下各自的熔融鋼接觸面設置多孔耐火物,且能夠從各自的多孔耐火物獨立地吹出氬氣(argon gas)。Also in
更且,著眼於前述(4),在專利文獻3,係有提出以下的連續鑄造方法:從設置於鋼液分配器之底部的噴嘴之上部所設置的環狀之上部多孔耐火物吹入非活性氣體,並且從設置於前述噴嘴之下部的環狀之下部多孔耐火物吹入非活性氣體。藉此能設成:上部多孔耐火物,係可以將非活性氣體朝向鋼液分配器的熔融鋼吹入;下部多孔耐火物,係可以將非活性氣體朝向噴嘴的開口吹入。
[先前技術文獻]
[專利文獻]Furthermore, focusing on the above-mentioned (4),
專利文獻1:日本特開2003-220450號公報 專利文獻2:日本特開平6-297118號公報 專利文獻3:日本特開2016-182612號公報Patent Document 1: Japanese Patent Laid-Open No. 2003-220450 Patent Document 2: Japanese Patent Application Laid-Open No. 6-297118 Patent Document 3: Japanese Patent Laid-Open No. 2016-182612
[發明所欲解決之課題][The problem to be solved by the invention]
為了提高鑄造板坯的品質,在前述(4)的鋼液分配器內使夾雜物浮起也是重要的。前述(1)至(3)與(4)的平衡(balance),係在於藉由個別的作業條件(包含技術訣竅(know-how))、鋼種、目標的品質等而適當決定的性質。 但是,在藉由前述專利文獻等之先前技術所為的吹氣方法等中,已明白:吹入後的氣體之大部分是流動至鋼液分配器上噴嘴的內孔側,無法使氣體在上方、亦即在鋼液分配器內的熔融鋼中浮起。In order to improve the quality of the cast slab, it is also important to float the inclusions in the molten steel distributor of (4). The balance (balance) of (1) to (3) and (4) above is a property appropriately determined by individual operating conditions (including know-how), steel type, and target quality. However, in the blowing methods and the like by the prior art such as the aforementioned patent documents, it has been found that most of the gas blown flows to the inner hole side of the upper nozzle of the molten steel distributor, and it is impossible to make the gas above , that is, floating in the molten steel in the molten steel distributor.
再者,前述(4)、亦即為了在鋼液分配器內使夾雜物浮起,也有以下的方法:在鋼液分配器上噴嘴以外的鋼液分配器底部之其中任一個位置,將氣體吹入至鋼液分配器內。 但是,為了在鋼液分配器上噴嘴以外的鋼液分配器底部之其中任一個位置,將氣體吹入至鋼液分配器內,需要供其使用的專用設備,原始成本(initial cost)及運轉成本(running cost)將會變高,且作業時的漏鋼等之危險性也會增大。 從如此的觀點來看,為了在鋼液分配器內藉由氣體來除去夾雜物,較佳是使用鋼液分配器上噴嘴,形成往鋼液分配器內熔融鋼的氣體之浮流,且調整其比例。Furthermore, in the above-mentioned (4), that is, in order to float the inclusions in the molten steel distributor, there is also the following method: in any position of the bottom of the molten steel distributor other than the nozzle on the molten steel distributor, the gas is Blow into the molten steel distributor. However, in order to blow gas into the molten steel distributor at any position on the bottom of the molten steel distributor other than the nozzle on the molten steel distributor, special equipment for its use, initial cost and operation are required. The cost (running cost) will increase, and the risk of breakout during operation will also increase. From such a viewpoint, in order to remove the inclusions by the gas in the molten steel distributor, it is preferable to use the upper nozzle of the molten steel distributor to form a floating flow of the molten steel gas into the molten steel distributor, and to adjust the Proportion.
本發明所欲解決的課題,係在於提供一種以下的鋼液分配器上噴嘴結構體及連續鑄造方法:在從鋼液分配器上噴嘴吹入氣體的形態中,可以使從該噴嘴的特定場所吹入的氣體全部在鋼液分配器內(從鋼液分配器上噴嘴起算的上方)浮起、或可以任意地調整朝向鋼液分配器上噴嘴的內孔側或者下方的氣體流量、與朝向鋼液分配器內(從鋼液分配器上噴嘴起算的上方)浮起的氣體流量之平衡。 再者,一個鋼液分配器上噴嘴的吐出位置、多孔體或貫通孔等的吐出孔之形態、吐出孔之數目等,係有各式各樣的;本發明之所謂「從該噴嘴的特定場所吹入的氣體之全部」,係意指一個氣體流出部分,換言之,係意指「從一個貫通孔吐出的氣體之全部,或是著眼於即便是包含多孔體等的複數個吐出孔仍如剛吐出後的複數個氣泡合體成一個氣泡之比如說形成氣泡一個之極小的吐出孔之集合部分的各個,並從該處吐出的氣體之全部」,而並非是將從一個鋼液分配器上噴嘴吐出的氣體全部作為對象。 [解決課題之手段]The problem to be solved by the present invention is to provide a molten steel distributor upper nozzle structure and a continuous casting method in which gas is blown from the molten steel distributor upper nozzle, and the nozzle can be blown from a specific location of the nozzle. All the blown gas floats in the molten steel distributor (from the top of the nozzle on the molten steel distributor), or the flow rate of the gas toward the inner hole side or the bottom of the nozzle on the molten steel distributor, and the direction can be adjusted arbitrarily. The balance of the floating gas flow in the molten steel distributor (from the top of the nozzle on the molten steel distributor). Furthermore, the discharge position of the nozzle on a molten steel distributor, the shape of the discharge holes such as the porous body or the through hole, the number of discharge holes, etc., are various; The whole of the gas blown into the place” means one gas outflow part, in other words, it means “the whole of the gas expelled from one through-hole, or if it is considered that even a plurality of spit holes including a porous body, etc., remain the same. A plurality of bubbles immediately after being spit out are combined into one bubble, for example, each of the collection parts of the extremely small discharge holes that form one bubble, and all the gas that is expelled from there”, not from a molten steel distributor. All the gas ejected from the nozzle is targeted. [Means of Solving Problems]
本發明人等係獲得以下的知識見解:如前述專利文獻從鋼液分配器上噴嘴的上端附近吹入後的氣體之大部分會流動至鋼液分配器上噴嘴的內孔側,無法使氣體在上方、亦即鋼液分配器內的熔融鋼中浮起的理由,係基於以下所造成:往鋼液分配器上噴嘴之上端附近的氣體吐出孔附近之該噴嘴內孔的熔融鋼流會成為主體,且該熔融鋼流比氣泡的浮流更強所致。The inventors of the present invention have obtained the following knowledge and insight: as in the aforementioned patent documents, most of the gas blown from the vicinity of the upper end of the upper nozzle of the molten steel distributor flows to the inner hole side of the upper nozzle of the molten steel distributor, and it is impossible to make the gas The reason why the molten steel floats above, that is, the molten steel in the molten steel distributor, is because the molten steel flow to the inner hole of the nozzle near the gas discharge hole near the upper end of the upper nozzle of the molten steel distributor will become the main body, and the molten steel flow is stronger than the floating flow of bubbles.
亦即,本發明的要旨,係為了使氣泡的浮流比往該噴嘴內孔的熔融鋼流更強,而提供一種使氣體吐出至往噴嘴內孔的熔融鋼流速成為比氣泡的浮起流速更小的位置,而且可以調整往該噴嘴內孔的氣體流量與浮起的氣體流量之平衡的鋼液分配器上噴嘴結構體、以及使用該鋼液分配器上噴嘴結構體的連續鑄造方法。That is, the gist of the present invention is to provide a flow velocity of molten steel in which the gas is discharged to the inner hole of the nozzle to be higher than the flow velocity of the floating bubbles in order to make the floating flow of the bubbles stronger than the flow of molten steel to the inner hole of the nozzle. A nozzle structure on a molten steel distributor capable of adjusting the balance between the flow rate of gas to the inner hole of the nozzle and the flow rate of floating gas, and a continuous casting method using the nozzle structure on the molten steel distributor.
具體而言,本發明係一種以下之1至11的鋼液分配器上噴嘴結構體及12的連續鑄造方法。
1.
一種鋼液分配器上噴嘴結構體,其特徵在於:在鋼液分配器上噴嘴的上端部外周之一部分或全周,具備比該鋼液分配器上噴嘴上端部的外形更大的凸鍔狀物;在前述凸鍔狀物之下面、外周面、上面、及比前述凸鍔狀物更下方之前述鋼液分配器上噴嘴的外周面之其中任一個面或複數個面,具備一個或複數個氣體吐出孔。
2.
如前述1所述之鋼液分配器上噴嘴結構體,其中,前述凸鍔狀物的氣體吐出孔,是作為該凸鍔狀物內之空間的氣體流通路徑之端部或從該凸鍔狀物之下面貫通於上面的孔。
3.
如前述1或2所述之鋼液分配器上噴嘴結構體,其中,在前述凸鍔狀物之下面係具備一個或複數個氣體可以通過的溝槽。
4.
如前述1或2所述之鋼液分配器上噴嘴結構體,其中,在已將該鋼液分配器上噴嘴結構體安裝於鋼液分配器的狀態下,在前述凸鍔狀物的下面之一部分或全部係具備氣體可以通過的空間。
5.
如前述1至4中任一項所述之鋼液分配器上噴嘴結構體,其中,該鋼液分配器上噴嘴結構體,是藉由止塞桿進行熔融鋼之流量控制以供鋼的連續鑄造用;
從前述鋼液分配器上噴嘴的下端之內孔面的鉛直位置直至前述凸鍔狀物的上面之氣體吐出孔或外周面為止的長度L(mm),是滿足下述之數式1:
其中,M:鑄造速度(t/min)。
6.
如前述1至4中任一項所述之鋼液分配器上噴嘴結構體,其中,該鋼液分配器上噴嘴結構體,是藉由止塞桿進行熔融鋼之流量控制以供鋼的連續鑄造用;
從前述鋼液分配器上噴嘴的下端之內孔面的鉛直位置直至前述凸鍔狀物的上面之氣體吐出孔或外周面為止的長度L(mm),是滿足下述之數式2:
其中,M:鑄造速度(t/min)。
7.
如前述1至5中任一項所述之鋼液分配器上噴嘴結構體,其中,從前述鋼液分配器上噴嘴的下端之內孔面的鉛直位置直至前述凸鍔狀物的上面之氣體吐出孔或外周面為止的長度L(mm),為60mm以上。
8.
如前述1至7中任一項所述之鋼液分配器上噴嘴結構體,其中,前述凸鍔狀物,係接合於前述鋼液分配器上噴嘴。
9.
如前述8所述之鋼液分配器上噴嘴結構體,其中,前述凸鍔狀物與前述鋼液分配器上噴嘴,是藉由螺絲或是卡口結構(bayonet structure)、或接著材料所接合。
10.
如前述1至7中任一項所述之鋼液分配器上噴嘴結構體,其中,前述凸鍔狀物,係嵌合於前述鋼液分配器上噴嘴的外周,且接合於與該鋼液分配器上噴嘴鄰接的風口或鋼液分配器底部耐火物層。
11.
如前述10所述之鋼液分配器上噴嘴結構體,其中,前述凸鍔狀物與前述風口或前述鋼液分配器底部耐火物層,是藉由螺絲或是卡口結構、或接著材料所接合。
12.
一種連續鑄造方法,係使用前述1至4中任一項所述之鋼液分配器上噴嘴結構體的連續鑄造方法,其特徵在於:
前述鋼液分配器上噴嘴結構體,是藉由止塞桿進行熔融鋼之流量控制以供鋼的連續鑄造用;
將從前述鋼液分配器上噴嘴的下端之內孔面的鉛直位置直至前述凸鍔狀物的上面之氣體吐出孔或外周面為止的長度L(mm),設成滿足下述之數式3的邊界長度LB(mm)以上來使氣體大致全部浮起、或設成未滿前述邊界長度LB(mm)來調整氣體往內孔側下方的流量與浮起的量;
其中,M:鑄造速度(t/min)。
[發明效果]Specifically, the present invention relates to a continuous casting method for the nozzle structure and 12 of the molten steel distributor of the following 1 to 11. 1. A nozzle structure on a liquid steel distributor, characterized in that: a part or the whole circumference of the outer periphery of the upper end of the nozzle on the liquid steel distributor has a larger convex shape than the shape of the upper end of the nozzle on the liquid steel distributor. A collar; any one or a plurality of surfaces below the convex collar, the outer peripheral surface, the upper surface, and the outer peripheral surface of the nozzle of the molten steel distributor below the convex collar, with a Or a plurality of gas discharge holes. 2. The upper nozzle structure of the molten steel distributor as described in the above 1, wherein the gas discharge hole of the convex collar is the end of the gas flow path of the space in the convex collar or from the convex collar. The bottom of the collar penetrates the hole above. 3. The upper nozzle structure of the molten steel distributor according to the above 1 or 2, wherein one or a plurality of grooves through which the gas can pass are provided under the convex collar. 4. The upper nozzle structure of the molten steel distributor according to the above 1 or 2, wherein in the state that the upper nozzle structure of the molten steel distributor has been mounted on the molten steel distributor, in the above-mentioned convex flange. Part or all of the lower part has a space through which gas can pass. 5. The upper nozzle structure of the molten steel distributor according to any one of the aforementioned 1 to 4, wherein the upper nozzle structure of the molten steel distributor is to control the flow of molten steel by means of a stopper rod to supply steel. For continuous casting; the length L (mm) from the vertical position of the inner hole surface of the lower end of the nozzle of the molten steel distributor to the gas discharge hole or the outer peripheral surface of the upper surface of the convex collar is the following: Formula 1: Among them, M: casting speed (t/min). 6. The upper nozzle structure of the molten steel distributor according to any one of the aforementioned 1 to 4, wherein the upper nozzle structure of the molten steel distributor is to control the flow rate of molten steel by means of a stopper rod to supply steel. For continuous casting; the length L (mm) from the vertical position of the inner hole surface of the lower end of the nozzle of the molten steel distributor to the gas discharge hole or the outer peripheral surface of the upper surface of the convex collar is the following: Formula 2: Among them, M: casting speed (t/min). 7. The upper nozzle structure of the molten steel distributor according to any one of the above 1 to 5, wherein from the vertical position of the inner hole surface of the lower end of the upper nozzle of the molten steel distributor to the upper surface of the above-mentioned convex collar The length L (mm) to the gas discharge hole or the outer peripheral surface is 60 mm or more. 8. The upper nozzle structure of the molten steel distributor according to any one of 1 to 7 above, wherein the protruding collar is connected to the upper nozzle of the molten steel distributor. 9. The upper nozzle structure of the molten steel distributor according to the above 8, wherein, the protruding collar and the upper nozzle of the molten steel distributor are made of screws, bayonet structures, or adhesive materials. joined. 10. The upper nozzle structure of the molten steel distributor according to any one of the above 1 to 7, wherein the convex flange is fitted to the outer circumference of the upper nozzle of the molten steel distributor, and is joined to the upper nozzle of the molten steel distributor. The tuyere adjacent to the nozzle on the molten steel distributor or the refractory layer at the bottom of the molten steel distributor. 11. The upper nozzle structure of the molten steel distributor according to the aforementioned 10, wherein, the protruding flange and the tuyere or the refractory layer at the bottom of the molten steel distributor are made of screws or a bayonet structure, or a material joined. 12. A continuous casting method using the continuous casting method of the nozzle structure on the molten steel distributor described in any one of the aforementioned 1 to 4, characterized in that: the nozzle structure on the aforementioned molten steel distributor is made by The stopper rod is used to control the flow of molten steel for continuous casting of steel; from the vertical position of the inner hole surface of the lower end of the nozzle of the molten steel distributor to the gas discharge hole or the outer peripheral surface of the upper surface of the convex collar The length L (mm) up to this point is set to be equal to or greater than the boundary length LB (mm) satisfying the
依據本發明,藉由在鋼液分配器上噴嘴的上端部外周之一部分或全周,設置比該鋼液分配器上噴嘴的外形更大的凸鍔狀物,就可以將氣體引導至鋼液分配器上噴嘴的外周側、亦即往內孔之熔融鋼流速較小的區域,並從其附近使氣體轉向上方。藉此,可以使氣體在鋼液分配器內浮起,且可以獲得在鋼液分配器內使夾雜物浮起的功效。甚至可以改善鑄造板坯品質。 又,藉由任意地調節比該鋼液分配器上噴嘴的外形更大的凸鍔狀物之從內孔下端的鉛直位置直至氣體吐出孔或沿凸鍔狀物流動之後達至朝向上方釋放的部位之氣體吐出部分為止的長度(前述L),就可以因應個別的作業等來任意地調節氣體往噴嘴內孔側下方的流量與往鋼液分配器內的浮起流量。According to the present invention, the gas can be guided to the molten steel by arranging a portion or the entire circumference of the upper end portion of the nozzle on the molten steel distributor with a protrusion larger than the outer shape of the nozzle on the molten steel distributor. The outer peripheral side of the nozzle on the distributor, that is, the area where the flow rate of molten steel to the inner hole is small, and from its vicinity, the gas is diverted upward. Thereby, the gas can be floated in the molten steel distributor, and the effect of floating inclusions in the molten steel distributor can be obtained. Even casting slab quality can be improved. In addition, by arbitrarily adjusting the vertical position of the convex collar larger than the outer shape of the nozzle on the molten steel distributor from the lower end of the inner hole until the gas discharge hole or after flowing along the convex collar, it can reach the upward release. The length of the part to the gas discharge part (the above-mentioned L) can arbitrarily adjust the flow rate of the gas to the lower side of the nozzle inner hole and the floating flow rate to the molten steel distributor according to individual operations.
圖1係顯示本發明之一實施形態的鋼液分配器上噴嘴結構體之主要部分。
本實施形態的鋼液分配器上噴嘴結構體10,是藉由止塞桿20進行熔融鋼之流量控制以供鋼的連續鑄造用;在鋼液分配器上噴嘴11的上端部外周之全周,具備比該鋼液分配器上噴嘴11的外形(外徑)更大的凸鍔狀物12。又,本實施形態的鋼液分配器上噴嘴結構體10,係在比凸鍔狀物12還下方之鋼液分配器上噴嘴11的外周面,具備複數個(在周方向以等間隔排列有六個)氣體吐出孔13a。更且,本實施形態的鋼液分配器上噴嘴結構體10,係在鋼液分配器上噴嘴11的上端面,也具備複數個(在周方向以等間隔排列有24個)氣體吐出孔13b。
再者,如圖1所示,鋼液分配器上噴嘴結構體10,係在已將之安裝於鋼液分配器30的狀態下,在凸鍔狀物12的下面之一部分或全部係具備氣體可以通過的空間S(鑄造中係由於在鋼液分配器內充滿熔融鋼,所以在該空間係存在熔融鋼)。Fig. 1 shows a main part of a nozzle structure on a molten steel distributor according to an embodiment of the present invention.
The
如此,藉由在本實施形態的鋼液分配器上噴嘴結構體10中係設置有凸鍔狀物12,就可以將氣體引導至鋼液分配器上噴嘴11的外周側、亦即往內孔11a之熔融鋼流速(箭頭A方向)較小的區域(箭頭B方向),並從其附近使氣體轉向上方。藉此,可以使氣體在鋼液分配器30內浮起,且可以獲得在鋼液分配器30內使夾雜物浮起的功效。甚至可以改善鑄造板坯品質。As described above, by providing the
更且,本發明人等,係在如此的鋼液分配器上噴嘴結構體10中,獲得以下的知識見解:氣體往內孔11a側下方的流量與往鋼液分配器30的浮起量之比例,係大幅地依存於圖1所示的長度L(mm)及鑄造速度M(t/min)。在此所謂圖1所示的長度L,係指從鋼液分配器上噴嘴11的下端之內孔面11b的鉛直位置直至凸鍔狀物12的上面之氣體吐出孔或外周面為止的長度;鑄造速度M(t/min),係與熔融鋼的產能(throughput)同義。Furthermore, the inventors of the present invention have obtained the following knowledge in the
再者,將該長度L設為從鋼液分配器上噴嘴11的下端之內孔面11b的鉛直位置起算,此是因:雖然鋼液分配器上噴嘴的外周或上端附近係能設為各式各樣的形狀,但是下端之內孔面的位置(與內孔徑大致相同)係只要是同樣的鑄造速度就大部分不會變動,亦即在往內孔流入的熔融鋼之速度上沒有較大的差異所致;更且,即便是在止塞桿控制的情況下,其嵌合部位置仍會伴隨該內孔的直徑而為同樣的半徑方向位置所致。In addition, the length L is calculated from the vertical position of the
亦即,本發明人等,係發現了以下的知識見解:在該長度L(mm),是滿足下述之數式1的情況下,可以使氣體的大致全部在鋼液分配器內浮起;在滿足下述之數式2的情況下,可以調整氣體往內孔側下方的流量與浮起的量。 That is, the inventors of the present invention have found the following knowledge: when the length L (mm) satisfies the
如同前述,本發明中之控制氣體的內孔側或浮起之比例,係依每次從各自的吐出孔所吐出的氣體來進行。 從而,在成為決定該長度L(mm)的一方之基準的前述凸鍔狀物之上面有氣體吐出孔的情況下,無論存在一個或複數個都是指與其各個吐出孔之每一個有關的前述之長度;或者,在從前述凸鍔狀物的下方之其中任一個或從外周面使氣體流動並在凸鍔狀物的外周面使氣體朝向上方釋放的情況下,係指直至該凸鍔狀物之的外周面為止之長度。即便此等並存,各自的吐出氣體仍能藉由其長度L(mm)分別決定藉由前述數式所得的內孔側/浮起之比例。是否使其並存、或如何決定數目係與作為鋼液分配器上噴嘴整體的氣體之吐出量或形態的控制有關,此點係只要因應個別的作業條件(任意)來設定即可。As described above, in the present invention, the control of the inner hole side or the floating ratio of the gas is performed according to the gas discharged from the respective discharge holes each time. Therefore, in the case where there are gas discharge holes on the upper surface of the convex collar that serves as a reference for determining the length L (mm), whether there are one or a plurality of gas discharge holes means the above-mentioned gas discharge holes related to each of the discharge holes. length; or, in the case of flowing gas from any one of the underside of the aforesaid protruding flanges or from the outer peripheral surface and releasing the gas upwards on the outer peripheral surface of the protruding flanges, it means up to the protruding flanges. The length of a thing up to its outer circumference. Even if these coexist, the ratio of inner hole side/floating obtained by the above-mentioned formula can be determined by the length L (mm) of each discharge gas. Whether to coexist or how to determine the number is related to the control of the gas discharge amount and form as the entire nozzle on the molten steel distributor, and this point can be set according to individual operating conditions (optional).
再者,當將此等數式1及數式2的右邊予以圖形化就如同圖2,在長度L位於該近似線以上之區域的情況下,可以使氣體的大致全部在鋼液分配器內浮起;在位於未滿近似線之區域的情況下,可以調整氣體往內孔側下方的流量與浮起的量。Furthermore, when the right sides of the
其次,針對前述之數式1及數式2的技術根據(導出根據)等來加以說明。Next, the technical basis (derivation basis) and the like of the
首先,使用流動分析軟體(FLUENT(計算流體力學軟體)),並以以下的條件進行了模擬(simulation)。 •將鋼液分配器上噴嘴的內孔徑設為80mmφ; •作為止塞桿控制,係相對於全閉時的嵌合部之直徑100mmφ將空間設為約12mm; •氣體吐出孔為0.3mmφ的貫通孔,→13b(24孔)、13a (6孔); •將氣泡直徑設為3.5mmφ; •鑄造速度係設為0t/min至5t/min。 更且,以以下的條件進行了水模型(water model)實驗。 •將鋼液分配器上噴嘴的內孔徑設為80mmφ; •作為止塞桿控制,係相對於全閉時的嵌合部之直徑100mmφ將空間設為約15mm; •氣體吐出孔為0.3mmφ的貫通孔(氣泡直徑結果約為1.5mmφ至3.5mmφ); •鑄造速度係設為3t/min。First, a flow analysis software (FLUENT (computational fluid dynamics software)) was used, and a simulation was performed under the following conditions. • Set the inner diameter of the nozzle on the molten steel distributor to 80mmφ; • As the stopper rod control, the space is set to about 12mm relative to the diameter of the fitting part when it is fully closed: 100mmφ; • The gas discharge hole is a 0.3mmφ through hole, → 13b (24 holes), 13a (6 holes); •Set the bubble diameter to 3.5mmφ; • The casting speed is set from 0t/min to 5t/min. Furthermore, a water model experiment was performed under the following conditions. • Set the inner diameter of the nozzle on the molten steel distributor to 80mmφ; • As the stopper rod control, the space is set to about 15mm relative to the diameter of the fitting part when fully closed, 100mmφ; • The gas discharge hole is a through hole with a diameter of 0.3mmφ (the diameter of the bubble is about 1.5mmφ to 3.5mmφ); • The casting speed is set to 3t/min.
再者,本發明人等係根據至今的實驗、實際作業的結果等而發現了以下的知識見解:在水模型中,在氣體吐出孔的直徑為0.3mmφ的情況下,氣泡直徑係成為約1.5mmφ至3.5mmφ,而在熔融鋼中更成為其2倍至3倍;以及該氣體吐出孔0.3mmφ的貫通孔與氧化鋁(alumina)-石墨質的多孔體(所謂的多孔耐火物,平均氣孔直徑≒100μm至120μm)之氣泡直徑,係成為大部分相同的大小。Furthermore, the inventors of the present invention have found the following knowledge based on the results of previous experiments and actual work. In the water model, when the diameter of the gas discharge hole is 0.3 mmφ, the bubble diameter is about 1.5 mm. mmφ to 3.5 mmφ, and 2 to 3 times larger in molten steel; and through holes of 0.3 mmφ of the gas discharge holes and alumina-graphite porous bodies (so-called porous refractories, average pores The diameter of the bubbles with a diameter of ≒ 100 μm to 120 μm) is mostly the same size.
藉由使此等鑄造速度變化的模擬,來獲得可以使從外周吹入來的(13a)氣體之大致全部浮起之作為邊界值的前述之長度L(mm)(圖2的各個軌跡圖(plot)),且以藉由迴歸分析所得的近似線及近似式來表示該結果,並獲得以下的數式3。 The above-mentioned length L (mm) as a boundary value at which almost all of the (13a) gas blown in from the outer periphery can be floated is obtained by changing the casting speed by simulation (each locus diagram in Fig. 2 ( plot)), and the result is represented by an approximate line and an approximate expression obtained by regression analysis, and the following
在此等的模擬與水模型實驗之比較中,前述之長度L(mm)係大致一致。In the comparison between these simulations and water model experiments, the aforementioned length L (mm) is approximately the same.
當將此等換句話來說時,可以將前述之長度L(mm),設為滿足前述之數式3的邊界長度LB(mm)以上來使氣體大致全部浮起、或設為未滿邊界長度LB(mm)來調整氣體往內孔側下方的流量與浮起的量。In other words, the above-mentioned length L (mm) may be set to be equal to or larger than the boundary length LB (mm) satisfying the above-mentioned
再者,在此圖2中,縱軸L(mm),由於是從鋼液分配器上噴嘴內孔下端的鉛直位置起算的長度,所以是包含該鋼液分配器上噴嘴結構體的凸鍔狀物設置位置之壁厚在內的長度。從而,凸鍔狀物為前述之壁厚(mm)<LB (mm)的情況是成為本發明的範圍。 又,在一般的(大半的)鑄造中,係在如此之鋼液分配器上噴嘴每一個的鑄造速度約為3(t/min)以上的情況下,氣體的浮起量減少的情形較多,當考慮如此的實際情況時,只要長度L(mm)大致為60mm以上,大致全部的氣體就會朝向上方浮起。 亦即,在一般的(大半的)鑄造中,為了使從外周吹入來的(13a)氣體全部朝向上方浮起,需要L≧60mm,又在L<60mm的情況下,L變得越小,氣體往內孔側下方的流量就變得越多(參照圖3)。In addition, in this FIG. 2, the vertical axis L (mm) is the length from the vertical position of the lower end of the nozzle inner hole of the molten steel distributor, so it is the convex flange including the nozzle structure of the molten steel distributor. The length including the wall thickness where the object is placed. Therefore, the case where the above-mentioned wall thickness (mm)<LB (mm) of the convex collar falls within the scope of the present invention. In addition, in general (most of) casting, when the casting speed per nozzle of the molten steel distributor is about 3 (t/min) or more, the amount of gas floating is often reduced. , when considering such an actual situation, as long as the length L (mm) is approximately 60 mm or more, approximately all the gas will float upward. That is, in general (mostly) casting, in order to float all the gas (13a) blown from the outer periphery upward, L≧60mm is required, and when L<60mm, L becomes smaller. , the flow rate of the gas to the lower side of the inner hole becomes larger (refer to FIG. 3 ).
以下,針對本實施形態(圖1)的變化例加以例示。
(A)在本實施形態中,雖然凸鍔狀物12,係設置於鋼液分配器上噴嘴11的上端部外周之全周,但是也可設置於鋼液分配器上噴嘴11的上端部外周之一部分。即便凸鍔狀物12的設置位置是假設為鋼液分配器上噴嘴11的上端部外周之一部分,仍能獲得不少使氣體在鋼液分配器內浮起的功效(在鋼液分配器內使夾雜物浮起的功效)。
又,凸鍔狀物12的俯視觀察形狀係不限於圓形,例如也可為橢圓形或多角形。Hereinafter, a modification of the present embodiment ( FIG. 1 ) will be illustrated.
(A) In the present embodiment, although the
(B)在本實施形態中,雖然氣體吐出孔13a,係在比凸鍔狀物12還下方之鋼液分配器上噴嘴11的外周面設置有複數個(在周方向以等間隔設置有六個),但是氣體吐出孔13a,也可在凸鍔狀物12的下面、外周面、上面之其中任一個面或複數個面設置一個或複數個。在如此地將氣體吐出孔13a設置於凸鍔狀物12的情況下,該凸鍔狀物12的氣體吐出孔13a,係可以設成作為凸鍔狀物12內之空間的氣體流通路徑之端部或從凸鍔狀物12的下面貫通於上面的孔。(B) In the present embodiment, although the
(C)在本實施形態中,雖然在凸鍔狀物12的下面係具備氣體可以通過的空間S,但是也可以在凸鍔狀物12的下面具備一個或複數個氣體可以通過的溝槽。
又,在前述溝槽,係包含:使凸鍔狀物12的下面朝向圓周方方向彎曲並將圓周方向的一部分形成凹狀,且使該凹狀部朝向半徑方向延伸的形態。亦即,前述溝槽,係只要具備作為氣體可以集中並朝向外周側方向移動之氣體流通路徑的結構即可。
更且,也可以在前述空間S的位置換成空間而設置氣體穿透性較高的多孔性之耐火物。(C) In this embodiment, although the space S through which the gas can pass is provided on the lower surface of the
(D)在本實施形態中,雖然凸鍔狀物12,係藉由接著材料來與鋼液分配器上噴嘴11接合,但是也可藉由螺絲或卡口結構來與鋼液分配器上噴嘴11接合。
又,凸鍔狀物12,也可嵌合於鋼液分配器上噴嘴11的外周,且接合於與該鋼液分配器上噴嘴11鄰接的風口31或鋼液分配器底部耐火物層32。該接合,係可以藉由螺絲或是卡口結構、或接著材料來進行。(D) In this embodiment, although the protruding
(E)雖然本實施形態的鋼液分配器上噴嘴結構體10,是藉由止塞桿20進行熔融鋼之流量控制以供鋼的連續鑄造用,但是也可以作為藉由滑動噴嘴裝置(sliding nozzle device)進行熔融鋼之流量控制以供鋼的連續鑄造用。亦即,也可以應用於鋼液分配器上噴嘴上方沒有使熔融鋼之流動產生變化的所謂障礙物的結構。
[實施例](E) Although the
在下述的鑄造條件及鋼液分配器上噴嘴條件之下,使用未設置凸鍔狀物12的習知品(比較例)、與設置凸鍔狀物12並使前述之長度L(mm)在30mm至60mm之範圍內變化的本發明品(實施例),來實施藉由止塞桿進行熔融鋼之流量控制的鋼之連續鑄造試驗,且評估了鋼液分配器上噴嘴內的氧化鋁附著厚度、與作為製品的線圈(coil)之表面瑕疵的產生數。具體而言,將習知品中的鋼液分配器上噴嘴內的氧化鋁附著厚度設為1.0,將本發明品中的鋼液分配器上噴嘴內的氧化鋁附著厚度指數化。該噴嘴內氧化鋁附著厚度指數越小,鋼液分配器上噴嘴內的氧化鋁附著厚度就越小。又,將習知品中的線圈之表面瑕疵的產生數設為1.0,將本發明品中的線圈之表面瑕疵的產生數指數化。該線圈表面瑕疵產生指數越小,線圈之表面瑕疵的產生數就越少,亦即鑄造板坯的品質就越佳。Under the following casting conditions and the conditions of the nozzle on the molten steel distributor, a conventional product (comparative example) without the
<鑄造條件> •鋼種:一般鋁脫氧鋼(aluminium killed steel) •鑄造尺寸:250mm(厚度)×1250mm(寬度) •鑄造速度(熔融鋼的產能):約3(t/min) <鋼液分配器上噴嘴條件> •內孔徑:80mm •氣體吐出孔的直徑×數目:0.3(mm)×13b(24孔)、13a (6孔) 氣體(氬)吐出量:10(L/min) 氣體(氬)吐出流速:1.56(m/min)<Casting conditions> • Steel grade: general aluminum deoxidized steel (aluminium killed steel) •Casting size: 250mm(thickness)×1250mm(width) • Casting speed (production capacity of molten steel): about 3 (t/min) <Conditions for nozzles on the molten steel distributor> • Bore diameter: 80mm • Diameter x number of gas discharge holes: 0.3 (mm) x 13b (24 holes), 13a (6 holes) Gas (argon) discharge volume: 10 (L/min) Gas (argon) discharge flow rate: 1.56 (m/min)
表1係顯示連續鑄造試驗的結果。再者,在本連續鑄造試驗中,由於鑄造速度(熔融鋼的產能)約為3(t/min),所以前述之數式3中的邊界長度LB約為60mm。Table 1 shows the results of the continuous casting test. In addition, in this continuous casting test, since the casting speed (production capacity of molten steel) was about 3 (t/min), the boundary length LB in the above-mentioned
氣泡的浮起量(比例),係將總量設為100的指數,且為藉由來自目視及水模型實驗等的推測值(實施例)所得者,100是意指大致全部浮起,0是意指全部往內孔側流入。The floating amount (ratio) of air bubbles is an index with the total amount set to 100, and is obtained from the estimated value (example) from visual observation and water model experiments, etc., 100 means almost all floating, 0 It means that all flows into the inner hole side.
如表1所示,有關L(mm)為邊界長度LB(約60mm)以上的本發明品(實施例3),係比習知品(比較例1),其鋼液分配器上噴嘴內的氧化鋁附著厚度變小,且線圈之表面瑕疵的產生數也變小。 再者,有關L(mm)未滿邊界長度LB(約60mm)的本發明品(實施例1、2),係顯示可以藉由調整L(mm)來調整氣泡的浮起量/內孔側量之比例,且其也可以調整鑄造板坯的品質。As shown in Table 1, the product of the present invention (Example 3) whose L (mm) is the boundary length LB (about 60 mm) or more is higher than the conventional product (Comparative Example 1), and the alumina in the nozzle of the molten steel distributor The adhesion thickness is reduced, and the number of occurrences of surface flaws on the coil is also reduced. In addition, regarding the product of the present invention (Examples 1 and 2) whose L (mm) is less than the boundary length LB (about 60 mm), it is shown that the amount of bubble floating/inner hole side can be adjusted by adjusting L (mm). and it can also adjust the quality of the cast slab.
10:鋼液分配器上噴嘴結構體
11:鋼液分配器上噴嘴
11a:內孔
11b:內孔面
12:凸鍔狀物
13a,13b:氣體吐出孔
20:止塞桿
30:鋼液分配器
31:風口
32:鋼液分配器底部耐火物層
L:長度
S:空間10: Nozzle structure on the molten steel distributor
11: Nozzle on the
[圖1]係顯示本發明之一實施形態的鋼液分配器上噴嘴結構體之主要部分的概略剖視圖。
[圖2]係將前述的數式1及數式2之右邊予以曲線化的圖。
[圖3]係顯示圖1之鋼液分配器上噴嘴結構體中的氣體舉動解析結果的圖。1 is a schematic cross-sectional view showing a main part of a nozzle structure on a molten steel distributor according to an embodiment of the present invention.
[ Fig. 2 ] It is a graph in which the right-hand sides of the above-mentioned
10:鋼液分配器上噴嘴結構體 10: Nozzle structure on the molten steel distributor
11:鋼液分配器上噴嘴 11: Nozzle on the molten steel distributor
11a:內孔 11a: Inner hole
11b:內孔面 11b: Bore surface
12:凸鍔狀物 12: Convex collar
13a,13b:氣體吐出孔 13a, 13b: Gas discharge holes
20:止塞桿 20: stop rod
30:鋼液分配器 30: Liquid steel distributor
31:風口 31: Air outlet
32:鋼液分配器底部耐火物層 32: Refractory layer at the bottom of the molten steel distributor
L:長度 L: length
S:空間 S: space
Claims (12)
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JP2019175256A JP2021049564A (en) | 2019-09-26 | 2019-09-26 | Tundish upper nozzle structure and method of continuous casting |
JP2019-175256 | 2019-09-26 |
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TW202128310A TW202128310A (en) | 2021-08-01 |
TWI770616B true TWI770616B (en) | 2022-07-11 |
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TW109133031A TWI770616B (en) | 2019-09-26 | 2020-09-24 | Nozzle structure on liquid steel distributor and continuous casting method |
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US (1) | US20220324017A1 (en) |
EP (1) | EP4035795A4 (en) |
JP (1) | JP2021049564A (en) |
CN (1) | CN114040823A (en) |
BR (1) | BR112022001629A2 (en) |
TW (1) | TWI770616B (en) |
WO (1) | WO2021060122A1 (en) |
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- 2019-09-26 JP JP2019175256A patent/JP2021049564A/en active Pending
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- 2020-09-17 BR BR112022001629A patent/BR112022001629A2/en unknown
- 2020-09-17 EP EP20868567.7A patent/EP4035795A4/en not_active Withdrawn
- 2020-09-17 WO PCT/JP2020/035165 patent/WO2021060122A1/en unknown
- 2020-09-17 CN CN202080046023.XA patent/CN114040823A/en active Pending
- 2020-09-17 US US17/639,848 patent/US20220324017A1/en not_active Abandoned
- 2020-09-24 TW TW109133031A patent/TWI770616B/en active
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Publication number | Publication date |
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US20220324017A1 (en) | 2022-10-13 |
CN114040823A (en) | 2022-02-11 |
WO2021060122A1 (en) | 2021-04-01 |
JP2021049564A (en) | 2021-04-01 |
EP4035795A4 (en) | 2023-02-08 |
EP4035795A1 (en) | 2022-08-03 |
TW202128310A (en) | 2021-08-01 |
BR112022001629A2 (en) | 2022-04-19 |
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