CN106978519A - A kind of method that blowing argon gas prevent whirlpool slag in ladle tapping process - Google Patents

A kind of method that blowing argon gas prevent whirlpool slag in ladle tapping process Download PDF

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Publication number
CN106978519A
CN106978519A CN201710263683.3A CN201710263683A CN106978519A CN 106978519 A CN106978519 A CN 106978519A CN 201710263683 A CN201710263683 A CN 201710263683A CN 106978519 A CN106978519 A CN 106978519A
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ladle
whirlpool
molten steel
gas
argon gas
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王强
李宏侠
王连钰
蒋佳伟
赫冀成
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Northeastern University China
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Northeastern University China
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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/04Removing impurities by adding a treating agent
    • C21C7/072Treatment with gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D41/00Casting melt-holding vessels, e.g. ladles, tundishes, cups or the like
    • B22D41/50Pouring-nozzles
    • B22D41/58Pouring-nozzles with gas injecting means

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Treatment Of Steel In Its Molten State (AREA)

Abstract

The present invention relates to one kind in ladle tapping process, a kind of method prevented and treated by bottom blowing argon gas whirlpool slag phenomenon belongs to metallurgical technology field.The present invention is that during steel ladle pouring, low discharge air blowing is carried out by the gas hole for wrapping bottom, and the Flow Field Distribution of whirlpool formation in tapping process is upset with this, thoroughly suppresses the formation of whirlpool and the generation of whirlpool slag phenomenon.Advantages of the present invention:Ladle structure is not changed, whirlpool slag phenomenon just can be effectively eliminated, and improves molten steel cleanness and recovery rate of iron;The gas hole used when can be using refining, it is not necessary to which gas hole is located near the mouth of a river, it is also an option that setting multiple gas holes, larger temperature drop is caused all without the molten steel to flowing into tundish;Overall process of tapping carries out low discharge blowing argon gas, to further promoting inclusion floating and molten steel temperature homogenization also to play a role, while it is exposed not result in molten steel.

Description

A kind of method that blowing argon gas prevent whirlpool slag in ladle tapping process
Technical field
The invention belongs to metallurgical technology field, and in particular to a kind of blowing argon gas prevent whirlpool slag in ladle tapping process Method.
Background technology
With continuing to develop for the every profession and trades such as space flight, traffic, oil and automobile, requirement of each field to steel performance is then not It is disconnected to improve, therefore, steel inclusion how is reduced, improve the cleanliness factor of steel, and then steel product quality is improved, obtain high-performance Gao Pin One of the problem of matter steel are iron and steel enterprise's extensive concerns.And casting process is the important step of clean steel production, to the clean of steel Cleanliness influence is very big, and the whirlpool slag phenomenon wherein produced in ladle tapping process has just had a strong impact on the cleanliness factor of molten steel, Molten steel is polluted, while can also bring ladle liner to be corroded, nozzle blocking, slag clear up the harm such as difficulty.
The specific forming process of whirlpool slag is:After the mouth of a river is opened, due to produced by molten steel ladle self gravitation The poor not releveling of static pressure, promotes molten steel constantly to flow into tundish from ladle, liquid level starts continuous decline;The energy provided when gravity When amount is not enough, the fluid of surrounding can not fill up the fluid volume at the outflow mouth of a river in time, and liquid level just starts to be recessed;Then it is recessed Fall into and constantly extend downward into the mouth of a river in coniform, so just gradually formed the whirlpool being observed that in people's vision.Whirlpool Tip reach the mouth of a river at when liquid level be defined as critical altitude, when liquid level be less than critical altitude when, slag is just rolled up Enter into tundish.The whirlpool actually formed in ladle tapping process is divided to two kinds of forms, and one kind is non-rotary whirlpool of confluxing, one It is the funnel type whirlpool rotated to plant.Both formation mechenisms are entirely different, and its difference is essentially consisted in:The funnel type whirlpool ratio of rotation Conflux the formation condition that many one of whirlpool tangentially disturbs.Refining, transport and molten steel of this tangential disturbance mainly due to ladle The molten steel that causes of temperature difference etc. reason inside there is the motion of tangential direction, then under the conditions of angular momentum conservation law, As fluid constantly flows to the mouth of a river, the distance apart from mouth of a river center is nearer, and its angular speed is bigger, so increase over time, Fluid rotary obtains more and more faster, so more seriously prevents surrounding fluid to go to supplement the fluid volume at the outflow mouth of a river in time, Then the formation of liquid surface hollow is accelerated.Therefore, the critical altitude for comparing non-rotary whirlpool of confluxing is very low, and rotate The critical altitude of funnel type whirlpool is very high, and slag is very serious, is the main cause for causing slag.And traditional technology is pin For confluxing in molten steel, whirlpool has been formed, in order to which the starting point for reducing whirlpool size is prevented and treated, not from whirlpool formation machine Reason is prevented and treated, therefore is not suitable for solving " the funnel type whirlpool " of rotation.In addition, the air blowing flow that traditional technology needs is relative It is larger, it is necessary to which strict control, otherwise can cause slag and the exposed phenomenon by secondary oxidation of molten steel on the contrary.Meanwhile, traditional skill Porous breathable brick is set to need to change original ladle structure in tapping hole in art, larger also easily cause of air blowing flow is blown steel The temperature drop of liquid is larger, and air blowing can extend the tapping time at tapping hole.
At present, prevent the technology of whirlpool slag to be broadly divided into following three class in casting process, be respectively on hide method, lower Tibetan method With suppression method (Huang Ye:Jiangxi Metallurgical, 19 (1999), 1).Method of hiding on so-called refers to the steel retained before ladle is withdrawn in ladle Liquid depth just stops cast when being more than critical altitude, the generation of whirlpool is hidden from top, but will be to sacrifice molten steel recovery rate as generation Valency.This method is usually required to install various slag automatic detection devices, and slide gate nozzle is closed in time according to monitoring signals, but Due to not suppressing whirlpool fundamentally, so the problem of still there is delayed and sacrifice molten steel recovery rate.So-called lower Tibetan method is Refer to the ladle bottom position near the locality reduction mouth of a river, make critical altitude part so that all hiding within the reduction position, Hide whirlpool from bottom, so as to reach the dual purpose for reducing slag and improving molten steel recovery rate.But the method is to ladle structure Change larger, and easily cause dry slag, also limited by production environment and space.And suppression method refers to take measures fundamentally The critical altitude of whirlpool is reduced, the generation of whirlpool is postponed or prevents the formation of through funnel-form whirlpool, so as to reduce whirlpool volume Slag phenomenon, and then the recovery rate of molten steel is improved, the method is the most commonly used one kind being studied in three kinds of methods.Common suppression For example various valve bodies that swim of preparation method, the anti-whirlpool of electromagnetism and anti-whirlpool of blowing.Nippon has invented skimming ball (Zheng Xinyou within 1970:Steel Iron is studied, 1 (2000), 59), Labate M D summarize the experience that West Germany's scum rod is used in the U.S. within 1987, have invented top (the Labate M D such as floating plug of spiral shell shape:US4799650), these methods are added in tapping process with molten steel liquid level one The valve body declined is acted, density can block the mouth of a river automatically to suppress whirlpool between molten steel and slag in the front valve shell of slag Slag phenomenon.French IRSID research institutes proposed the whirlpool in tundish is controlled using electromagnetic principle in 1978 Design (Pierre V:France, No2443892), Suh J W etc. propose to carry out anti-whirlpool (Suh J W using magnetostatic field:ISIJ, 41 (2001), 689), and the design such as I.I. Da Er Dicks the anti-whirlpool device of rotary electromagnetic field, these methods are to utilize magnetic field pair The Lorentz force that molten steel is produced carries out contactless control to whirlpool slag phenomenon.Ono-Nakazato H are proposed in whirlpool soon Inert gas is blown at the mouth of a river carry out anti-whirlpool (Ono-Nakazato H during formation:Journal of JSEM,7(2007), 120), the method is being to prevent being involved in for field trash to the active force of molten steel using gas.For the various valve bodies that swim, New impurity has been introduced into molten steel;Calutron is difficult to determine due to the hot environment of actual production and whirlpool direction of rotation Restriction, also exist only in conceptual phase;And the anti-whirlpool method of air blowing proposed at present is mainly when whirlpool is soon formed in water Mouthful place blown, it is necessary to air-blowing quantity it is relatively large, easily cause liquid fluctuating increase, formation slag blister cause molten steel to aoxidize, Larger temperature drop is caused to the molten steel for flowing into tundish simultaneously.The pros and cons of more each anti-whirlpool method, are generally adopted in current actual production Anti- whirlpool method be still sacrifice molten steel recovery rate on hide method, mainly using slag monitoring technology to close in time the mouth of a river with Molten steel cleanness is ensured, therefore, greatly increases ton steel cost, very big economic loss is brought to enterprise.
The content of the invention
For the deficiency of various anti-whirlpool methods in existing ladle tapping process, steel is prevented the invention provides a kind of blowing argon gas The method of whirlpool slag phenomenon in bag tapping process, it is therefore intended that, overall process is carried out by bottom blowing hole in tapping process Low discharge is blown, and then upsets Flow Field Distribution when whirlpool is formed, and thoroughly eliminates the formation of whirlpool and the hair of whirlpool slag phenomenon It is raw.
The present invention relates to ladle, tundish and argon-blowing device;The ladle bottom is provided with the mouth of a river;In the ladle Molten steel flows into tundish by the mouth of a river;The gas hole communicated with argon-blowing device, the air blowing are also provided with the ladle bottom Hole be single hole or can simultaneously blowing argon gas it is porous.During use, it is desirable to open Argon while opening ladle nozzle cast Device, Argon operation is carried out in tapping overall process, carries out single hole by the gas hole of ladle bottom or porous while blowing argon gas, and Single hole or porous total gas flow rate are 1~100L/min.The argon-blowing device is that those skilled in the art are usually used in this area Known device.
When wherein described air blowing flow is smaller, it can effectively eliminate whirlpool and temperature drop is very small;Described blowing gas stream When measuring larger, it can effectively eliminate whirlpool and inclusion floating, molten steel temperature homogenization have been promoted.
Air blowing flow can also further be adjusted according to actual conditions, for example, air blowing flow can be increased in tapping early stage 38~100L/min, little particle inclusion floating and the uniform purpose of temperature are promoted to reach, the later stage gradually subtracts with molten steel amount Air blowing flow can be turned down to 1~38L/min less and reach the purpose for reducing temperature drop.
The present invention can be carried out single hole air blowing, just can be had to whirlpool slag phenomenon using gas hole used in refining link Suppressed.
Currently preferred technical scheme is, distance of the gas hole away from ladle center for ladle radius 3/4ths with It is interior.Described air blowing hole site is most preferably close to ladle center, and carrying out blowing here can reach optimal whirlpool suppression effect Really.
Currently preferred technical scheme is that described porous air blowing makes wherein a hole refines link by ladle bottom Gas hole, distance of other gas holes away from ladle center is that other gas holes are away from steel within 3/4ths of ladle radius The optimal distance at bag center is 1/2nd of ladle radius.
Compared with other anti-whirlpool methods, difference and advantage of the invention is:Molten steel blowing argon gas smelt production link in be Through frequently with, it is very acute that it is primarily due to the effect that inert gas will not be polluted between molten steel, and bubble and molten steel It is strong, there is very strong change effect to the flow field in ladle, therefore, selection blowing argon gas, which carry out anti-whirlpool, can realize many anti-whirlpool methods The pollution-free and significantly effective anti-whirlpool effect being difficult to, substantially increases the recovery rate of molten steel.The present invention can be answered simultaneously With the existing gas hole of ladle, so operation implements simple and easy, without being modified to ladle structure, cost is relatively low. And compared with others blow anti-whirlpool, the present invention is not the active force using air blowing when whirlpool is soon formed passively to offset Liquid surface hollow caused by whirlpool, but carry out blowing always before whirlpool formation upsetting the Flow Field Distribution form that whirlpool is formed, Active by rotary-type whirlpool eliminate in rudiment.The air blowing flow that uses of the present invention is smaller simultaneously, and it is exposed not result in molten steel, The low discharge of tapping overall process, which is blown, can also be conducive to further removing the little particle field trash still suffered from ladle after refining, have Beneficial to the homogenization of molten steel temperature, and avoid to flowing into the drawbacks of molten steel in tundish causes larger temperature drop.
Brief description of the drawings
The anti-whirlpool schematic diagram of Fig. 1 ladle argon-blowns:In figure, 101, whirlpool;102nd, molten steel;103rd, molten steel is circulated;201st, steel Bag;202nd, gas hole;203rd, the mouth of a river;207th, tundish.
Fig. 2 water model experimental provision schematic diagrams:In figure, 201, model ladle;202nd, gas hole;203rd, the mouth of a river;204th, valve Door;205th, pop one's head in;206th, supersonic Doppler tachymeter;207th, model tundish;208th, flowmeter;209th, nitrogen cylinder.
Fig. 3 gas hole locations drawing:In figure, 1-8 be air blowing hole site;Wherein 1-No. 4 gas holes away from ladle center away from From 1/2nd for ladle radius, 5,6, No. 8 distances of the gas hole away from ladle center be 3/4ths of ladle radius, No. 7 Gas hole is located at ladle center.
Fig. 4 tangential velocities and the variation relation figure of air blowing flow.
Fig. 5 whirlpools critical altitudes and gas hole change in location graph of a relation.
Fig. 6 difference air blowings hole site sets figure.
Fig. 7 whirlpools critical altitudes and molten steel/slag blanket mixed zone thickness.
Embodiment
Following non-limiting examples can make one of ordinary skill in the art be more fully understood the present invention, but not with Any mode limits the present invention.Any one skilled in the art in the technical scope of present disclosure, according to Technical scheme and its inventive concept carry out equivalent substitution or changed to belong to protection category of the present invention.
Below in conjunction with the accompanying drawings and according to the principle of similitude carry out water model EXPERIMENTAL EXAMPLE the present invention is further described.
The blowing argon gas that the present invention is implemented prevent water model device such as Fig. 1 and 2 of whirlpool slag phenomenon in ladle tapping process Shown, model ladle 201 is with 1 by actual 60t ladles:4 geometric proportion is manufactured, wherein filling the water that height is 60cm (simulation molten steel), stands after 5min, and the valve 204 for opening the mouth of a river 203 carries out tapping steel, passes through while opening nitrogen cylinder 209 Gas hole 202 carries out bottom nitrogen blowing (simulation argon gas) operation, and the gas flow that is passed through is controlled using flowmeter 208, and with surpassing Acoustic doppler tachymeter 206 measures the tangential velocity value of 205 positions of probe.Can be with by water model EXPERIMENTAL EXAMPLE The mobility status of molten steel ladle when illustrating the present invention to the inhibition of whirlpool in tapping process and the implementation present invention.
Embodiment 1
Using described water model experimental provision, stream is blown into by No. 1 gas hole 202 in Fig. 3 respectively in tapping process Measure as 0~1.3L/min gases.When air blowing flow is 0L/min, i.e., the critical altitude of whirlpool is higher when not blown in tapping process For 9.4cm, it is passed through after gas, the critical altitude with the increase whirlpool of air blowing flow significantly declines.It is in air blowing flow Constantly, the critical altitude of whirlpool is reduced to 5.5cm to 0.04L/min;When air blowing flow is 1.3L/min, the critical altitude drop of whirlpool To minimum 1.8cm.It is consequently possible to calculate the liquid recovery rate for going out the final gained of water model experiment carried out according to the present invention can Improve about 13% or so.
According to above-mentioned experimental result, by the reduction formula Q between simulation gas and actual air-blowing quantityAr=0.901 λ-5/2QN2 The argon gas amount being blown into the actual tapping process for reach identical inhibition, wherein Q can be calculatedArFor in actual tapping process The argon flow amount being blown into, QN2For the nitrogen amount being blown into simulation process, λ is the geometric proportion factor of model ladle and actual ladle (Xu Hailun:University of Science & Technology, Beijing's journal, 32 (2010), 843).By calculate the argon flow amount that is actually blown into should 1~ 38L/min.Wherein, when being blown into less argon flow amount, good whirlpool inhibition just can be reached, and is blown into relatively large Argon flow amount when, except can preferably suppress whirlpool slag phenomenon, the flowing of molten steel 102 can also be increased.Such as Fig. 4 institutes Show, the tangential velocity after air blowing in ladle 201 with the distribution form away from the bottom level of ladle 201 when not blowing compared with Change, upset the velocity field of whirlpool formation, thus inhibit the formation of whirlpool;And larger air blowing flow makes in ladle 201 The tangential velocity of molten steel has increased that (tangential velocity is not average tangential velocity of the measurement point relative to the center of ladle 201, and not Consider direction of rotation), the disturbance of molten steel is become big, promote the flowing between molten steel.Meanwhile, air blowing can also make molten steel tap Formed in journey on vertical direction as shown in Figure 1 and circulate 103, this circulate can fill up as in Fig. 1 in time The volume for the liquid surface hollow that whirlpool 103 is formed, while the upper of heat exchange between molten steel and little particle field trash can also be promoted It is floating.
The temperature drop formula Δ T=M of molten steel is caused by blowing argon gasAr×CAr×(TSteel-TAr)/(CSteel×MSteel) can calculate and blow The temperature drop brought after argon gas, wherein Δ T are temperature drop, MArFor argon gas mass flow, MSteelFor the quality of molten steel, CArFor the ratio of argon gas Thermal capacitance 0.879J/ (kg. DEG C), CSteelFor specific heat capacity 1.465J/ (kg. DEG C) (Yu Haiming of molten steel:The external refining skill of converter molten steel Art, 2011,163).Then molten steel temperature is 1600 DEG C, when temperature of argon gas is 20 DEG C, and argon gas density is 1.784kg/m3, ladle appearance Measure as 60t, because ladle tapping process molten steel amount is constantly reduced, take the half of ladleful substantially to estimate that its temperature drop can be obtained, When being blown into argon flow amount for 0.04L/min, the temperature drop produced to molten steel is about 0.000002 DEG C, very small to ignore;And When being blown into argon flow amount for 38L/min, the temperature drop produced to molten steel is about 0.002 DEG C.Therefore, the present invention not at the mouth of a river to steel Liquid is blown, and make it that argon gas gradually disperses in whole ladle, and the temperature drop formed to molten steel is all relatively small.
Embodiment 2
Using described water model experimental provision, it is blown into respectively by 1-No. 8 gas holes 202 in Fig. 3 in tapping process Flow is 0.06L/min gas, obtains the experimental result such as Fig. 5.As shown in Figure 5, whirlpool when not blown in tapping process Critical altitude is very high, and when being blown by 1-No. 8 gas holes 202, the critical altitude of whirlpool is decreased obviously, therefore, Gas hole 202 used, the whirlpool inhibition that just may be significantly when can be refined in practice using ladle 201.And phase Than under, preferably, i.e., gas hole 202 is located proximate to ladle to the inhibition of whirlpool when being blown by No. 7 gas holes 202 201 centers, the inhibition of whirlpool is relatively preferable.Blown simultaneously in the optimal position of gas hole 202, air blowing flow is only Just critical altitude can be dropped to 1.5cm during for 0.06L/min, it is seen then that further adjust air blowing flow in this position, one can be entered The critical altitude of step reduction whirlpool, obtains higher recovery rate of iron.
The present invention in actual applications, can also further be adjusted according to actual conditions to air blowing flow, in tapping early stage Air blowing flow can be increased, little particle inclusion floating and the uniform purpose of temperature are promoted to reach, the later stage with molten steel amount gradually Reduction can turn air blowing flow down, reach the purpose for reducing temperature drop.
Embodiment 3
Using method for numerical simulation, simulate after being blown respectively by the different gas holes in Fig. 6 in tapping process Slag situation is specific to set as follows:I.e. air blowing flow of not blowing is 0L/min;Single hole is blown, and air blowing hole site is No. 1 air blowing Hole, air blowing flow is 100L/min, and diplopore is blown, and air blowing hole site is No. 1 and No. 2 gas holes, and total air blowing flow is 100L/ Min (single hole flow is 50L/min);Diplopore is blown, and air blowing hole site is No. 1 and No. 3, and total air blowing flow is 100L/min (single Hole flow is 50L/min).Each distance of the gas hole away from the mouth of a river is R/4 (R is ladle bottom radius).Fig. 7 is analog result, By analog result it can be found that either single hole is blown or diplopore air blowing can significantly decrease the critical altitude of whirlpool, Inhibit the generation of whirlpool slag phenomenon.

Claims (6)

1. a kind of method that blowing argon gas prevent whirlpool slag in ladle tapping process, it is characterised in that:In tapping overall process, lead to The gas hole for crossing ladle bottom carries out single hole or porous while blowing argon gas, and single hole or porous total gas flow rate are 1~100L/ min。
2. the method that a kind of blowing argon gas according to claim 1 prevent whirlpool slag in ladle tapping process, its feature exists In:Distance of the gas hole away from ladle center is within 3/4ths of ladle radius.
3. the method that a kind of blowing argon gas according to claim 1 or 2 prevent whirlpool slag in ladle tapping process, its feature It is:The gas hole is gas hole used in ladle bottom refining link.
4. the method that a kind of blowing argon gas according to claim 3 prevent whirlpool slag in ladle tapping process, its feature exists In:Described porous air blowing, wherein a hole is gas hole used in ladle bottom refining link, other gas holes are away from ladle The distance of the heart is within 3/4ths of ladle radius.
5. the method that a kind of blowing argon gas according to claim 1 or 2 prevent whirlpool slag in ladle tapping process, its feature It is:Described air blowing hole site is close to ladle center.
6. the method that a kind of blowing argon gas according to claim 1 prevent whirlpool slag in ladle tapping process, its feature exists In:Described air blowing is to increase air blowing 38~100L/min of flow in tapping early stage, and the later stage will blow as molten steel amount is gradually decreased Throughput is adjusted to 1~38L/min.
CN201710263683.3A 2017-04-21 2017-04-21 A kind of method that blowing argon gas prevent whirlpool slag in ladle tapping process Pending CN106978519A (en)

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Cited By (7)

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CN107608397A (en) * 2017-08-21 2018-01-19 河钢股份有限公司邯郸分公司 LF refining adjusts the device and method of ladle bottom blowing argon flow amount during standing
CN107858479A (en) * 2017-12-20 2018-03-30 马鞍山钢铁股份有限公司 A kind of converter tapping vortex inhibitor
CN108273987A (en) * 2018-04-09 2018-07-13 东北大学 A kind of ladle ventilating filling pipe end brick cup and its method for controlling ladle roughing slag
CN108620544A (en) * 2018-06-04 2018-10-09 东北大学 A kind of casting process control stuffing sand enters the method for tundish
CN109047695A (en) * 2018-08-01 2018-12-21 东北大学 A kind of immersed nozzle for continuous casting mould Argon control method
CN110523966A (en) * 2019-09-25 2019-12-03 张家港广大特材股份有限公司 A kind of double porous cores of ladle
CN113042699A (en) * 2021-03-16 2021-06-29 北部湾大学 Method for judging air blowing slag entrapment of slab crystallizer

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CN104525929A (en) * 2014-12-18 2015-04-22 东北大学 Method for controlling steel ladle tapping slag by blowing argon gas to annular steel outlet in bottom of steel ladle
CN105714013A (en) * 2014-12-01 2016-06-29 鞍钢股份有限公司 Control method for eddy slag rolling during converter tapping

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EP0956917A1 (en) * 1998-05-11 1999-11-17 Berthold Raubuch Metallurgical vessel and tapping method
KR20010059603A (en) * 1999-12-30 2001-07-06 이구택 Electric furnace having gas blowing nozzle for forming gas curtain
CN1204274C (en) * 2001-04-05 2005-06-01 格奥尔格斯玛林许特有限公司 Method and device for preventing slag from flowing along when tapping molten metal
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Cited By (10)

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Publication number Priority date Publication date Assignee Title
CN107608397A (en) * 2017-08-21 2018-01-19 河钢股份有限公司邯郸分公司 LF refining adjusts the device and method of ladle bottom blowing argon flow amount during standing
CN107608397B (en) * 2017-08-21 2020-09-18 河钢股份有限公司邯郸分公司 Device and method for adjusting bottom blowing argon flow of steel ladle during LF refining standing
CN107858479A (en) * 2017-12-20 2018-03-30 马鞍山钢铁股份有限公司 A kind of converter tapping vortex inhibitor
CN108273987A (en) * 2018-04-09 2018-07-13 东北大学 A kind of ladle ventilating filling pipe end brick cup and its method for controlling ladle roughing slag
CN108273987B (en) * 2018-04-09 2020-05-19 东北大学 Ladle air-permeable upper nozzle pocket brick and method for controlling ladle slag discharging
CN108620544A (en) * 2018-06-04 2018-10-09 东北大学 A kind of casting process control stuffing sand enters the method for tundish
CN109047695A (en) * 2018-08-01 2018-12-21 东北大学 A kind of immersed nozzle for continuous casting mould Argon control method
CN109047695B (en) * 2018-08-01 2019-06-18 东北大学 A kind of immersed nozzle for continuous casting mould Argon control method
CN110523966A (en) * 2019-09-25 2019-12-03 张家港广大特材股份有限公司 A kind of double porous cores of ladle
CN113042699A (en) * 2021-03-16 2021-06-29 北部湾大学 Method for judging air blowing slag entrapment of slab crystallizer

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