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CN107267703A - Molten iron dephosphorization device and dephosphorization method for rotary powder injection - Google Patents

Molten iron dephosphorization device and dephosphorization method for rotary powder injection Download PDF

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Publication number
CN107267703A
CN107267703A CN201710269742.8A CN201710269742A CN107267703A CN 107267703 A CN107267703 A CN 107267703A CN 201710269742 A CN201710269742 A CN 201710269742A CN 107267703 A CN107267703 A CN 107267703A
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dephosphorization
molten iron
podwer gun
injection system
powder
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唐复平
万雪峰
廖相巍
曹东
李广帮
任子平
贾吉祥
张晓光
赵亮
李晓伟
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Angang Steel Co Ltd
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Angang Steel Co Ltd
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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
    • C21C1/00Refining of pig-iron; Cast iron
    • C21C1/02Dephosphorising or desulfurising
    • 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
    • C21C7/064Dephosphorising; Desulfurising

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)

Abstract

本发明公开一种旋转喷吹粉剂的铁水脱磷装置及脱磷方法,通过旋转喷粉铁水脱磷装置,利用倒T型喷粉枪可实现多点同时脱磷处理,提升了脱磷反应的动力学条件,有效提升脱磷率,加快脱磷反应速度,缩短脱磷处理时间,投资小;供料系统、喷吹系统可实现自动控制及在线调节;有效防止喷粉枪堵塞,并且能够实现喷粉枪自动除渣。

The invention discloses a molten iron dephosphorization device and a dephosphorization method for rotating powder spraying. Through the rotating powder spraying molten iron dephosphorization device, an inverted T-shaped powder spray gun can be used to realize multi-point simultaneous dephosphorization treatment, and the efficiency of the dephosphorization reaction is improved. Dynamic conditions can effectively improve the dephosphorization rate, accelerate the dephosphorization reaction speed, shorten the dephosphorization treatment time, and reduce investment; the feeding system and injection system can realize automatic control and online adjustment; effectively prevent the clogging of the powder spraying gun, and can realize The powder spray gun automatically removes slag.

Description

一种旋转喷吹粉剂的铁水脱磷装置及脱磷方法Dephosphorization device and dephosphorization method for molten iron with rotary injection powder

技术领域technical field

本发明涉及钢铁冶金领域,特别涉及一种旋转喷吹粉剂的铁水脱磷装置及脱磷方法。The invention relates to the field of iron and steel metallurgy, in particular to a molten iron dephosphorization device and a dephosphorization method for rotary spraying powder.

背景技术Background technique

磷是绝大多数钢种中的有害元素,容易在晶界偏析,引起钢的低温脆性和回火脆性。近年来,随着科学技术的迅速发展,用户对钢质量的要求不断提高。例如,对于低温用钢、海洋用钢、抗氢致裂纹钢和部分厚板用钢,除了要求极低的硫含量以外,也要求钢中的磷含量<0.01%或0.005%。Phosphorus is a harmful element in most steel types, and it is easy to segregate at grain boundaries, causing low temperature brittleness and temper brittleness of steel. In recent years, with the rapid development of science and technology, users' requirements for steel quality have been continuously improved. For example, for low-temperature steel, marine steel, hydrogen-induced cracking-resistant steel and steel for some thick plates, in addition to requiring extremely low sulfur content, the phosphorus content in steel is also required to be <0.01% or 0.005%.

此外,为了降低氧气转炉钢的生产成本和实行少渣炼钢,也要求铁水磷含量<0.015%。因此,80年代以来许多冶金工作者致力于研究铁水的预处理脱磷问题,开发了各种处理方法。In addition, in order to reduce the production cost of oxygen converter steel and implement less slag steelmaking, the phosphorus content of molten iron is also required to be <0.015%. Therefore, since the 1980s, many metallurgists have devoted themselves to the research on the pretreatment and dephosphorization of molten iron, and developed various treatment methods.

铁水预脱磷处理可以分为氧化脱磷和还原脱磷,目前,各钢厂普遍采用氧化脱磷工艺。脱磷方法根据脱磷剂不同分为SARP法、铁水罐法、ORP法、转炉法和NRP法等。常用的两类:一种是在盛铁水的铁水包或鱼雷车中进行脱磷;另一种是在转炉内进行铁水脱磷预处理。这两种方法在工业上均得到了实际应用。Hot metal pre-dephosphorization treatment can be divided into oxidative dephosphorization and reductive dephosphorization. At present, the oxidation dephosphorization process is widely used in steel mills. Dephosphorization methods are divided into SARP method, hot metal tank method, ORP method, converter method and NRP method according to different dephosphorization agents. There are two commonly used types: one is dephosphorization in ladle or torpedo car containing molten iron; the other is dephosphorization pretreatment in converter. These two methods have been practically used in industry.

申请号201310508854.6公开了一种名称为“一种铁水脱磷方法”其特征是本发明提供了一种铁水脱磷方法,主要针对大型转炉铁水脱磷。采用以下步骤进行:①通过氧枪从顶部向铁水表面供给氧气,供氧强度在0.8-1.1Nm3/t/min范围内变化;②通过转炉上方设置的料斗向铁水中加入以石灰、轻烧白云石、矿石为主体的造渣料进行造渣,成渣后炉渣二元碱度(CaO/SiO2)为1.6-2.0;③通过转炉炉底供气系统向钢水内部供给搅拌气体,供气强度在0.25-0.40Nm3/t/min。本发明利用低碱度炉渣熔点低,铁水温度低易成渣,通过较大矿石用量来促进成渣和供氧,利用低供氧强度吹炼来延长吹炼时间,大底吹强度搅拌实现渣、金间的充分混合,实现去磷,具有脱磷效果好,石灰用量少,脱磷用辅料消耗少,钢渣排放少的优点。但该方法脱磷率低,同时设备改造投资巨大。Application No. 201310508854.6 discloses a method named "a method for dephosphorizing molten iron", which is characterized in that the present invention provides a method for dephosphorizing molten iron, which is mainly aimed at dephosphorizing molten iron in large-scale converters. The following steps are adopted: ① Supply oxygen to the surface of molten iron from the top through an oxygen lance, and the oxygen supply intensity varies within the range of 0.8-1.1Nm 3 /t/min; ② Add lime, lightly burnt Dolomite and ore are the main slagging materials for slagging. After slagging, the binary alkalinity (CaO/SiO 2 ) of the slag is 1.6-2.0; The intensity is 0.25-0.40Nm 3 /t/min. The invention utilizes the low melting point of low-alkalinity slag, the low temperature of molten iron is easy to form slag, promotes slag formation and oxygen supply by using a large amount of ore, and prolongs the blowing time by blowing with low oxygen supply intensity, and realizes slag by stirring with large bottom blowing intensity , Fully mixed between gold and gold to achieve dephosphorization, has the advantages of good dephosphorization effect, less lime consumption, less consumption of auxiliary materials for dephosphorization, and less discharge of steel slag. However, the dephosphorization rate of this method is low, and the investment in equipment transformation is huge.

发明内容Contents of the invention

为了克服上述缺陷,本发明提供一种能够实现温降小、处理时间短;脱磷率高、设备改造及投资小的旋转喷吹粉剂的铁水脱磷装置及脱磷方法。In order to overcome the above-mentioned defects, the present invention provides a molten iron dephosphorization device and dephosphorization method capable of realizing small temperature drop, short processing time, high dephosphorization rate, equipment transformation and small investment in rotary spraying powder.

本发明目的是通过下面的技术方案实现的:The object of the invention is achieved by the following technical solutions:

一种旋转喷吹粉剂的铁水脱磷装置,其特征在于:包括升降装置、防喷溅装置、供料系统、喷吹系统、旋转装置、喷粉枪;所述的喷粉枪为倒T形中空管,管头两端带有喷孔,外部包裹耐火材料;所述的旋转装置包括旋转接头和内部带有空心轴的电机,旋转接头整体为三通结构,内部轴承与电机内的空心轴上端连接,旋转接头水平方向分别与管道连通,空心轴下端通过法兰与喷粉枪上端连接;所述防喷溅装置为上小下大的圆柱,旋转装置位于防喷溅装置内,所述的管道穿过防喷溅装置并通过金属软管分别与供料系统和喷吹系统连通,防喷溅装置下表面覆盖一层耐火材料;防喷溅装置与升降装置连接,防喷溅装置、旋转装置、喷粉枪均可随升降装置上下升降移动;所述的升降装置包括支架、升降机和支撑臂,支架与防喷溅装置连接,支架通过支撑臂与升降机连接;供料系统中的熔剂和喷吹系统中的载气通过旋转装置吹入喷粉枪,实现旋转喷粉。A molten iron dephosphorization device for rotating and spraying powder, characterized in that it includes a lifting device, an anti-splash device, a feeding system, an injection system, a rotating device, and a powder spraying gun; the powder spraying gun is an inverted T shape Hollow pipe, with spray holes at both ends of the pipe head, and refractory material wrapped on the outside; the rotating device includes a rotary joint and a motor with a hollow shaft inside. The upper end of the shaft is connected, the rotary joint is connected to the pipeline in the horizontal direction, and the lower end of the hollow shaft is connected to the upper end of the powder spray gun through a flange; the anti-splash device is a cylinder with a small upper part and a larger lower part. The above pipeline passes through the anti-splash device and communicates with the feeding system and the injection system respectively through metal hoses. The lower surface of the anti-splash device is covered with a layer of refractory material; the anti-splash device is connected with the lifting device, and the anti-splash device , the rotating device, and the powder spraying gun can move up and down with the lifting device; the lifting device includes a support, a lift and a support arm, the support is connected with the anti-splash device, and the support is connected with the lift through the support arm; The flux and the carrier gas in the injection system are blown into the powder spray gun through the rotating device to realize the rotary powder spraying.

所述防喷溅装置下表面直径为罐口外径的110~130%。The diameter of the lower surface of the splash prevention device is 110-130% of the outer diameter of the tank mouth.

所述喷粉枪横向钢管直径为纵向钢管直径的2/3~4/5;外部耐火材料长度为喷粉枪总长度的1/2~2/3。The diameter of the transverse steel pipe of the powder spraying gun is 2/3 to 4/5 of the diameter of the longitudinal steel pipe; the length of the external refractory material is 1/2 to 2/3 of the total length of the powder spraying gun.

一种旋转喷吹粉剂的旋转喷吹粉剂的铁水脱磷方法,其特征在于包括如下步骤:A method for dephosphorizing molten iron by rotary spraying powder, characterized in that it comprises the following steps:

1)将高炉出铁后进行铁水脱磷处理;1) Dephosphorization of molten iron is carried out after blast furnace tapping;

2)启动喷吹系统,将纯度为99.9%以上、压力0.4~0.6MPa的氮气或惰性气体通过喷粉枪吹入铁水,同时开启升降装置将喷粉枪下降至距铁水罐底部400~500mm,当喷粉枪达到工作位时开启旋转装置,旋转速度为10~30转/分钟,同时启动供料系统将需要加入的脱磷剂总量通过喷粉枪喷吹到铁水中,其合金粒径为0.09~0.125mm,调整喷吹系统将压力调至工作压力0.8~0.9MP直至脱磷完成;2) Start the injection system, blow nitrogen or inert gas with a purity of more than 99.9% and a pressure of 0.4 to 0.6 MPa into the molten iron through the powder spray gun, and at the same time open the lifting device to lower the powder spray gun to 400 to 500 mm from the bottom of the molten iron tank, When the powder spray gun reaches the working position, turn on the rotating device, the rotation speed is 10-30 rpm, and start the feeding system at the same time to spray the total amount of dephosphorization agent that needs to be added into the molten iron through the powder spray gun. 0.09~0.125mm, adjust the injection system to adjust the pressure to the working pressure of 0.8~0.9MP until the dephosphorization is completed;

3)铁水脱磷完成后,关闭供料系统并启动升降装置将喷粉枪提升至铁水液面以上,调整喷吹系统将压力调整至0.9~1.1MP,调整旋转装置将旋转速度调至30~50转/分钟,对喷粉枪进行1~2min除渣及防堵处理;3) After the dephosphorization of molten iron is completed, close the feeding system and start the lifting device to lift the powder spray gun above the molten iron level, adjust the injection system to adjust the pressure to 0.9~1.1MP, and adjust the rotating device to adjust the rotation speed to 30~ 50 revolutions per minute, 1-2 minutes for slag removal and anti-blocking treatment on the powder spray gun;

4)进行铁水扒渣处理及后序操作。4) Perform molten iron slag removal treatment and subsequent operations.

所述的脱磷剂中含氧化铁废料与石灰的质量比例为40~60:60~40,其中含氧化铁废料氧化铁质量百分比含量≥85%,石灰中氧化钙质量百分比含量≥90%。The mass ratio of iron oxide-containing waste to lime in the dephosphorization agent is 40-60:60-40, wherein the iron oxide-containing waste has a mass percentage of iron oxide ≥ 85% and calcium oxide in the lime ≥ 90% by mass.

本发明的有益效果:1.本发明通过采用专用旋转喷粉铁水脱磷装置,利用倒T型喷粉枪可实现多点同时脱磷处理,提升了脱磷反应的动力学条件,有效提升脱磷率。2.本发明采用旋转喷吹脱磷剂的方法进行铁水脱磷,可加快脱磷反应速度,缩短脱磷处理时间。3.本发明可在原有铁水脱硫工位进行部分改造即可实现,所以其设备改造及投资小。4.本发明其供料系统、喷吹系统可实现自动控制及在线调节。5.本发明可有效防止喷粉枪堵塞,并且能够实现喷粉枪自动除渣。Beneficial effects of the present invention: 1. The present invention adopts a special rotary powder-spraying molten iron dephosphorization device, and utilizes an inverted T-shaped spraying gun to realize multi-point simultaneous dephosphorization treatment, which improves the kinetic conditions of the dephosphorization reaction and effectively improves the dephosphorization process. Phosphorus rate. 2. The present invention adopts the method of rotating and spraying dephosphorizing agent to carry out dephosphorization of molten iron, which can accelerate the dephosphorization reaction speed and shorten the dephosphorization treatment time. 3. The present invention can be realized by partial transformation of the original hot metal desulfurization station, so its equipment transformation and investment are small. 4. The feeding system and injection system of the present invention can realize automatic control and online adjustment. 5. The present invention can effectively prevent the clogging of the powder spraying gun, and can realize the automatic deslagging of the powder spraying gun.

附图说明Description of drawings

图1为旋转喷吹粉剂的铁水脱磷装置结构示意图;Fig. 1 is the structural schematic diagram of the molten iron dephosphorization device of rotary injection powder;

图2为图1的A向放大图;Figure 2 is an enlarged view of the direction A of Figure 1;

其中,1-支架;2-防喷溅装置;3-供料系统;4-旋转装置;5-铁水罐;6-铁水罐车;7-喷粉枪;8-喷吹系统;9-升降机;10-支撑臂;11-旋转接头;12-电机;13-空心轴;14-法兰。Among them, 1-bracket; 2-splash prevention device; 3-feeding system; 4-rotating device; 5-hot metal tank; 6-hot metal tank car; 7-dusting gun; 10-support arm; 11-rotary joint; 12-motor; 13-hollow shaft; 14-flange.

具体实施方式detailed description

下面结合具体实施例进行说明:Describe below in conjunction with specific embodiment:

一种旋转喷吹粉剂的铁水脱磷装置,进行铁水脱磷处理装置,包括升降装置、防喷溅装置2、供料系统3、喷吹系统8、旋转装置4、喷粉枪7;升降装置包括支架1、升降机9和支撑臂10,支架1与防喷溅装置2连接,支架1通过支撑臂10与升降机9连接,升降机9采用液压系统作为驱动力;所述的喷粉枪7为倒T形中空管,管头两端带有喷孔,外部包裹耐火材料;所述的旋转装置4包括旋转接头11和内部带有空心轴13的电机12,旋转接头11整体为三通结构,内部轴承与电机12内的空心轴13上端连接,旋转接头水平方向分别与管道连通,空心轴13下端通过法兰14与喷粉枪7上端连接;所述防喷溅装置2为上小下大的圆柱,旋转装置4位于防喷溅装置2内,所述的管道穿过防喷溅装置2并通过金属软管分别与供料系统3和喷吹系统8连通,防喷溅装置2下表面覆盖一层耐火材料;防喷溅装置2与升降装置连接,防喷溅装置2、旋转装置4、喷粉枪7均可随升降装置上下升降移动;供料系统3中的熔剂和喷吹系统8中的载气通过旋转装置4吹入喷粉枪7,实现旋转喷粉。A molten iron dephosphorization device for rotating and spraying powder, a device for processing molten iron dephosphorization, including a lifting device, an anti-splashing device 2, a feeding system 3, an injection system 8, a rotating device 4, and a powder spraying gun 7; a lifting device Including a support 1, a lift 9 and a support arm 10, the support 1 is connected to the splash prevention device 2, the support 1 is connected to the lift 9 through the support arm 10, and the lift 9 uses a hydraulic system as a driving force; the powder spray gun 7 is an inverted T-shaped hollow tube, with spray holes at both ends of the tube head, and refractory material wrapped on the outside; the rotary device 4 includes a rotary joint 11 and a motor 12 with a hollow shaft 13 inside, and the rotary joint 11 is a three-way structure as a whole. The inner bearing is connected to the upper end of the hollow shaft 13 in the motor 12, the rotary joint is connected to the pipeline in the horizontal direction, and the lower end of the hollow shaft 13 is connected to the upper end of the powder spray gun 7 through the flange 14; The cylinder, the rotating device 4 is located in the anti-splash device 2, the pipeline passes through the anti-splash device 2 and communicates with the feeding system 3 and the injection system 8 through metal hoses, the lower surface of the anti-splash device 2 Cover with a layer of refractory material; the anti-splash device 2 is connected with the lifting device, and the anti-splash device 2, the rotating device 4, and the powder spray gun 7 can all move up and down with the lifting device; the flux and the injection system in the feeding system 3 The carrier gas in 8 is blown into the powder spraying gun 7 through the rotating device 4 to realize rotary powder spraying.

电机功率及大小,根据喷粉枪7具体尺寸及重量确定;The power and size of the motor are determined according to the specific size and weight of the powder spray gun 7;

防喷溅装置2下表面直径为铁水罐5罐口外径的110~130%;The diameter of the lower surface of the anti-splash device 2 is 110% to 130% of the outer diameter of the mouth of the molten iron tank 5;

所述喷粉枪7内部采用耐磨无缝钢管采用焊接手段制成,T形喷头横向钢管直径为纵向钢管直径的2/3~4/5;外部耐火材料长度为喷粉枪总长度的1/2~2/3。The inside of the powder spraying gun 7 is made of wear-resistant seamless steel pipe by means of welding, and the diameter of the transverse steel pipe of the T-shaped nozzle is 2/3 to 4/5 of the diameter of the longitudinal steel pipe; the length of the external refractory material is 1% of the total length of the powder spraying gun. /2~2/3.

将高炉出铁后载有铁水罐5的铁水罐车6开至处理位,采用本发明旋转喷吹粉剂铁水脱磷装置,进行铁水脱磷处理。The molten iron tank car 6 carrying the molten iron tank 5 is driven to the treatment position after the blast furnace is tapped, and the molten iron dephosphorization treatment is carried out by using the rotary spraying powder molten iron dephosphorization device of the present invention.

实施例1:Example 1:

采用本发明进行铁水脱磷试验,防喷溅装置2最大直径为铁水罐5罐口外径的110%,喷粉枪7外部包裹耐火材料其耐火材料长度为喷粉枪总长度的1/2;启动喷吹系统8将纯度为99.9%以上、压力0.4MPa的氮气或惰性气体通过喷粉枪7喷吹入铁水,同时开启升降机9将外部包裹耐火材料喷粉枪7下降至距铁水罐5底部400mm,当喷粉枪7达到工作位时开启旋转装置4,旋转速度为10转/分钟,同时启动供料系统3将需要加入的脱磷剂总量通过喷粉枪7喷吹到铁水中;其脱磷剂含氧化铁废料与石灰的比例为1:1,氧化铁废料氧化铁含量为85%,石灰中氧化钙含量90%,脱磷剂粒径为0.09mm;调整喷吹系统8将压力调至工作压力0.8MP直至铁水脱磷完成。铁水脱磷完成后,关闭供料系统3并启动升降机9将喷粉枪7提升至铁水液面以上,调整喷吹系统8将压力调整至0.9MP,调整旋转装置4将旋转速度调至30转/分钟,进行1min除渣、防堵处理。铁水脱磷完成后进行扒渣处理。完成上述处理后,按照常规进行后序操作。采用上述工艺方法及装置可实现如下技术指标:铁水温降为62℃、处理时间为35min;脱磷率为90%Using the present invention to carry out the molten iron dephosphorization test, the maximum diameter of the anti-splash device 2 is 110% of the outer diameter of the mouth of the molten iron tank 5, and the powder spray gun 7 is wrapped with refractory material, and the length of the refractory material is 1/2 of the total length of the powder spray gun; Start the injection system 8 to spray nitrogen or inert gas with a purity of 99.9% or more and a pressure of 0.4 MPa into the molten iron through the powder spray gun 7, and at the same time open the elevator 9 to lower the powder spray gun 7 wrapped with refractory material to the bottom of the molten iron tank 5 400mm, when the powder spray gun 7 reaches the working position, turn on the rotating device 4, the rotation speed is 10 rpm, and start the feeding system 3 at the same time to spray the total amount of dephosphorization agent to be added into the molten iron through the powder spray gun 7; The ratio of the dephosphorization agent containing iron oxide waste to lime is 1:1, the content of iron oxide in the iron oxide waste is 85%, the content of calcium oxide in the lime is 90%, and the particle size of the dephosphorization agent is 0.09mm; adjust the injection system 8 to The pressure is adjusted to the working pressure of 0.8MP until the dephosphorization of molten iron is completed. After the dephosphorization of molten iron is completed, close the feeding system 3 and start the elevator 9 to lift the powder spray gun 7 above the liquid level of the molten iron, adjust the injection system 8 to adjust the pressure to 0.9MP, and adjust the rotating device 4 to adjust the rotation speed to 30 rpm /min, carry out 1min slag removal and anti-blocking treatment. After the dephosphorization of molten iron is completed, slag removal is carried out. After the above-mentioned processing is completed, follow-up operations are carried out as usual. The following technical indicators can be achieved by using the above-mentioned process method and device: the temperature drop of molten iron is 62°C, the treatment time is 35 minutes; the dephosphorization rate is 90%

实施例2:Example 2:

采用本发明进行铁水脱磷试验,防喷溅装置2最大直径为铁水罐5罐口外径的120%,喷粉枪7外部包裹耐火材料其耐火材料长度为喷粉枪总长度的2/3;启动喷吹系统8将纯度为99.9%以上、压力0.5MPa的氮气或惰性气体通过喷粉枪7喷吹入铁水,同时开启升降机9将外部包裹耐火材料喷粉枪7下降至距铁水罐5底部450mm,当喷粉枪7达到工作位时开启旋转装置4,旋转速度为20转/分钟,同时启动供料系统3将需要加入的脱磷剂总量通过喷粉枪7喷吹到铁水中;其脱磷剂含氧化铁废料与石灰的比例为1:1,氧化铁废料氧化铁含量为90%,石灰中氧化钙含量94%,脱磷剂粒径为0.106mm;调整喷吹系统8将压力调至工作压力0.9MP直至铁水脱磷完成。铁水脱磷完成后,关闭供料系统3并启动升降机9将喷粉枪7提升至铁水液面以上,调整喷吹系统8将压力调整至1.0MP,调整旋转装置4将旋转速度调至40转/分钟,进行2min除渣、防堵处理。铁水脱磷完成后进行扒渣处理。完成上述处理后,按照常规进行后序操作。采用上述工艺方法及装置可实现如下技术指标:铁水温降为60℃、处理时间为30min;脱磷率为95%Adopting the present invention to carry out the molten iron dephosphorization test, the maximum diameter of the anti-splash device 2 is 120% of the outer diameter of the mouth of the molten iron tank 5, and the powder spray gun 7 is wrapped with refractory material, and the length of the refractory material is 2/3 of the total length of the powder spray gun; Start the injection system 8 to spray nitrogen or inert gas with a purity of 99.9% or more and a pressure of 0.5 MPa into the molten iron through the powder spray gun 7, and at the same time open the elevator 9 to lower the powder spray gun 7 wrapped with refractory material to the bottom of the molten iron tank 5 450mm, when the powder spray gun 7 reaches the working position, turn on the rotating device 4, the rotation speed is 20 rpm, and start the feeding system 3 at the same time to spray the total amount of dephosphorization agent to be added into the molten iron through the powder spray gun 7; The ratio of the dephosphorization agent containing iron oxide waste to lime is 1:1, the content of iron oxide in the iron oxide waste is 90%, the content of calcium oxide in the lime is 94%, and the particle size of the dephosphorization agent is 0.106mm; adjust the injection system 8 to The pressure is adjusted to the working pressure of 0.9MP until the dephosphorization of molten iron is completed. After the dephosphorization of molten iron is completed, close the feeding system 3 and start the elevator 9 to lift the powder spray gun 7 above the liquid level of the molten iron, adjust the injection system 8 to adjust the pressure to 1.0MP, and adjust the rotating device 4 to adjust the rotation speed to 40 rpm /min, carry out 2min slag removal and anti-blocking treatment. After the dephosphorization of molten iron is completed, slag removal is carried out. After the above-mentioned processing is completed, follow-up operations are carried out as usual. The following technical indicators can be achieved by using the above-mentioned process method and device: the temperature of molten iron is reduced to 60°C, the treatment time is 30 minutes; the dephosphorization rate is 95%

实施例3:Example 3:

采用本发明进行铁水脱磷试验,防喷溅装置2最大直径为铁水罐5罐口外径的130%,喷粉枪7外部包裹耐火材料其耐火材料长度为喷粉枪总长度的2/3;启动喷吹系统8将纯度为99.9%以上、压力0.6MPa的氮气或惰性气体通过喷粉枪7喷吹入铁水,同时开启升降机9将外部包裹耐火材料喷粉枪7下降至距铁水罐5底部500mm,当喷粉枪7达到工作位时开启旋转装置4,旋转速度为30转/分钟,同时启动供料系统3将需要加入的脱磷剂总量通过喷粉枪7喷吹到铁水中;其脱磷剂含氧化铁废料与石灰的比例为1:1,氧化铁废料氧化铁含量为95%,石灰中氧化钙含量98%,脱磷剂粒径为0.129mm;调整喷吹系统8将压力调至工作压力0.9MP直至铁水脱磷完成。铁水脱磷完成后,关闭供料系统3并启动升降机9将喷粉枪7提升至铁水液面以上,调整喷吹系统8将压力调整至1.1MP,调整旋转装置4将旋转速度调至50转/分钟,进行2min除渣、防堵处理。铁水脱磷完成后进行扒渣处理。完成上述处理后,按照常规进行后序操作。采用上述工艺方法及装置可实现如下技术指标:铁水温降为64℃、处理时间为33℃;脱磷率为98%Using the present invention to carry out the molten iron dephosphorization test, the maximum diameter of the anti-splash device 2 is 130% of the outer diameter of the mouth of the molten iron tank 5, and the powder gun 7 is wrapped with refractory material, and the length of the refractory material is 2/3 of the total length of the powder spray gun; Start the injection system 8 to spray nitrogen or inert gas with a purity of 99.9% or more and a pressure of 0.6 MPa into the molten iron through the powder spray gun 7, and at the same time open the elevator 9 to lower the powder spray gun 7 wrapped with refractory material to the bottom of the molten iron tank 5 500mm, when the powder spray gun 7 reaches the working position, turn on the rotating device 4, the rotation speed is 30 rpm, and start the feeding system 3 at the same time to spray the total amount of dephosphorization agent to be added into the molten iron through the powder spray gun 7; The ratio of the dephosphorization agent containing iron oxide waste to lime is 1:1, the content of iron oxide in the iron oxide waste is 95%, the content of calcium oxide in the lime is 98%, and the particle size of the dephosphorization agent is 0.129mm; adjust the injection system to 8 The pressure is adjusted to the working pressure of 0.9MP until the dephosphorization of molten iron is completed. After the molten iron dephosphorization is completed, close the feeding system 3 and start the elevator 9 to lift the powder spray gun 7 above the liquid level of the molten iron, adjust the injection system 8 to adjust the pressure to 1.1MP, and adjust the rotating device 4 to adjust the rotation speed to 50 rpm /min, carry out 2min slag removal and anti-blocking treatment. After the dephosphorization of molten iron is completed, slag removal is carried out. After the above-mentioned processing is completed, follow-up operations are carried out as usual. The following technical indicators can be achieved by using the above-mentioned process method and device: the temperature drop of molten iron is 64°C, the treatment time is 33°C; the dephosphorization rate is 98%

实施效果:Implementation Effect:

在某钢铁企业炼钢厂,采用旋转喷吹粉剂的铁水脱磷方法及装置,对铁水罐容量260t的铁水,进行铁水脱磷试验,并取得良好的效果,具体如下:In a steelmaking plant of an iron and steel enterprise, the hot metal dephosphorization method and device of rotating injection powder were used to conduct a hot metal dephosphorization test on a molten iron tank with a capacity of 260t, and good results were obtained, as follows:

采用本发明进行钢水铁水脱磷试验,其脱磷率为90~98%、平均94.33%,铁水温降为60~64℃、平均62℃;铁水脱磷处理时间为30~35min、平均32.67min;铁水脱磷各项技术指标控制稳定,与常规铁水脱磷工艺相比其脱磷率提高10~15%、温降减少30℃以上、铁水脱磷处理时间平均缩短60min以上。总之,采用全新的旋转喷吹粉剂的铁水脱磷方法比常规铁水脱磷方法在脱磷率、温降、铁水脱磷处理时间等技术指标上均有较大的提高,本发明的研制成功将是铁水脱磷工艺的一大革新。Using the present invention to carry out the dephosphorization test of molten steel and hot metal, the dephosphorization rate is 90-98%, with an average of 94.33%, the temperature of molten iron is reduced to 60-64°C, with an average of 62°C; the dephosphorization treatment time of molten iron is 30-35min, with an average of 32.67min The technical indicators of hot metal dephosphorization are controlled stably. Compared with the conventional hot metal dephosphorization process, the dephosphorization rate is increased by 10-15%, the temperature drop is reduced by more than 30°C, and the hot metal dephosphorization treatment time is shortened by more than 60 minutes on average. In a word, compared with conventional molten iron dephosphorization methods, the method for dephosphorizing molten iron using a brand-new rotary injection powder has greatly improved technical indicators such as dephosphorization rate, temperature drop, and treatment time for molten iron dephosphorization. The successful development of the present invention will It is a major innovation in the dephosphorization process of molten iron.

Claims (4)

1. a kind of dephosphorization of molten iron device of rotary blowing pulvis, it is characterised in that:Including lowering or hoisting gear, anti-splash device, feed System, injection system, rotating device, podwer gun;Described podwer gun is inverted T-shaped hollow tube, and tube head two ends carry spray orifice, outside Wrap up refractory material;Described rotating device includes swivel joint and the internal motor for carrying hollow shaft, and swivel joint is generally Three-port structure, internal bearings are connected with the hollow shaft upper end in motor, swivel joint horizontal direction respectively with pipeline communication, it is hollow Axle lower end is connected by flange with podwer gun upper end;The anti-splash device is up-small and down-big cylinder, and rotating device is located at anti- In spraying and splashing facility, described pipeline respectively with feeding system and injection system is connected through anti-splash device and by metal hose Logical, anti-splash device lower surface covers one layer of refractory material;Anti-splash device is connected with lowering or hoisting gear, anti-splash device, rotation Device, podwer gun can be moved with lowering or hoisting gear oscilaltion;Described lowering or hoisting gear includes support, lift and support arm, Support is connected with anti-splash device, and support is connected by support arm with lift;In flux and injection system in feeding system Carrier gas podwer gun is blown into by rotating device, realize rotating injecting powder.
2. a kind of dephosphorization of molten iron device of rotary blowing pulvis according to claim 1, it is characterised in that:The antispray The 110~130% of a diameter of tank mouth external diameter of device lower surface.
3. a kind of dephosphorization of molten iron device of rotary blowing pulvis according to claim 1, it is characterised in that:The podwer gun Horizontal diameter of steel tube is the 2/3~4/5 of longitudinal diameter of steel tube;Refractory material outside length is the 1/2~2/ of podwer gun total length 3。
4. the dephosphorization method of rotary blowing pulvis dephosphorization of molten iron device described in a kind of application claim 1, it is characterised in that including Following steps:
1) dephosphorization of molten iron processing will be carried out after blast furnace casting;
2) start injection system, be more than 99.9%, 0.4~0.6MPa of pressure nitrogen or inert gas by dusting by purity Rifle is blown into molten iron, drops to podwer gun away from molten iron 400~500mm of pot bottom while opening lowering or hoisting gear, when podwer gun reaches Rotating device is opened during working position, rotary speed is 10~30 revs/min, while the dephosphorization of addition will be needed by starting feeding system Agent total amount is blown into molten iron by podwer gun, and its alloy particle diameter is 0.09~0.125mm, and pressure is adjusted to by adjustment injection system 0.8~0.9MP of operating pressure is until dephosphorization is completed;
3) after the completion of dephosphorization of molten iron, close feeding system and start lowering or hoisting gear podwer gun is promoted to more than molten iron level, adjust Whole injection system adjusts pressure to 0.9~1.1MP, and rotary speed is adjusted to 30~50 revs/min by adjustment rotating device, to spray Powder rifle carries out 1~2min slagging-off and anti-blocking processing;
4) molten iron drossing processing and subsequent operations are carried out;
The mass ratio of waste material containing iron oxide and lime is 40~60 in described Dephosphorising agent:60~40, wherein useless containing iron oxide Expect calcium oxide mass percentage content >=90% in iron oxide mass percentage content >=85%, lime.
CN201710269742.8A 2017-04-24 2017-04-24 Molten iron dephosphorization device and dephosphorization method for rotary powder injection Pending CN107267703A (en)

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CN107245544A (en) * 2017-04-24 2017-10-13 鞍钢股份有限公司 Rotary powder injection device for ladle slag modification and modification method
CN107267711A (en) * 2017-04-24 2017-10-20 鞍钢股份有限公司 Molten steel alloying device and method of rotary blowing powder
CN107723416A (en) * 2017-11-15 2018-02-23 钢铁研究总院 A kind of ladle rotation spray gun dephosphorization apparatus
CN112458227A (en) * 2020-10-27 2021-03-09 扬州一川镍业有限公司 Dephosphorization equipment for producing nickel pig iron by using laterite-nickel ore and using method thereof

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CN107245544A (en) * 2017-04-24 2017-10-13 鞍钢股份有限公司 Rotary powder injection device for ladle slag modification and modification method
CN107267711A (en) * 2017-04-24 2017-10-20 鞍钢股份有限公司 Molten steel alloying device and method of rotary blowing powder

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CN203096107U (en) * 2013-02-07 2013-07-31 武汉钢铁(集团)公司 Blowing desulfurization spray gun for torpedo ladle
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Application publication date: 20171020