CN102443679B - Production method of steel with ultralow oxide inclusions - Google Patents
Production method of steel with ultralow oxide inclusions Download PDFInfo
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Abstract
Description
技术领域 technical field
本发明属于炼钢工艺技术领域,特别涉及一种超低氧化夹杂物钢种的生产控制方法。 The invention belongs to the technical field of steelmaking technology, and in particular relates to a production control method of ultra-low oxidation inclusion steel grades.
背景技术 Background technique
随着钢铁冶炼技术的发展,对钢水洁净度的要求亦越来越高,特别是高级轴承钢、高级切割线、高级帘线钢以及液化气储油罐等高级钢的开发,都对钢种夹杂物提出了更高的明确要求,并且要求愈来愈高。衡量氧化夹杂物多少的关键指标是钢中[Or]的含量。目前,一些钢种成品材检验要求钢中[Or]的含量达到10ppm以下,即所谓的超低氧化夹杂物钢,甚至有些极其特殊的钢种,要求[Or]达到5ppm以下。如何将钢中的[Or]稳定控制在5ppm以下,并且具备批量生产条件,已成为一个亟待解决的重要课题。 With the development of iron and steel smelting technology, the requirements for the cleanliness of molten steel are getting higher and higher, especially the development of high-grade steel such as high-grade bearing steel, high-grade cutting wire, high-grade cord steel and liquefied gas oil storage tank, etc. Inclusions put forward higher specific requirements, and the requirements are getting higher and higher. The key indicator to measure the amount of oxidized inclusions is the content of [Or] in steel. At present, the inspection of finished products of some steel grades requires the content of [Or] in the steel to be less than 10ppm, that is, the so-called ultra-low oxidation inclusion steel, and even some extremely special steel grades require [Or] to be less than 5ppm. How to stably control [Or] in steel below 5ppm and meet the conditions for mass production has become an important issue to be solved urgently.
发明内容 Contents of the invention
本发明的目的就是为了解决上述问题,从而提供一种能将钢中[Or]控制在5ppm以下,并且实现单浇次达到3罐以上连浇的超低氧化夹杂物钢的生产方法。 The purpose of the present invention is to solve the above problems, thereby providing a production method of ultra-low oxidation inclusion steel which can control [Or] in steel below 5ppm and realize continuous pouring of more than 3 cans in a single pouring time.
为达此目的,本发明采取了如下技术解决方案: For reaching this purpose, the present invention has taken following technical solution:
一种超低氧化夹杂物钢的生产方法,采取两次真空处理工艺,并在两次真空处理工艺之间加入LF炉处理工艺,真空处理结束后进行弱吹氩操作;其具体方法是: A method for producing ultra-low oxidation inclusion steel, which adopts two vacuum treatment processes, and adds an LF furnace treatment process between the two vacuum treatment processes, and performs weak argon blowing operation after the vacuum treatment is completed; the specific method is:
第一次真空处理要求: First vacuum treatment requirements:
(1)、转炉出钢采取不脱氧、沸腾出钢,转炉出钢碳重量百分比控制在0.08-0.12%; (1) Non-deoxidation and boiling tapping are used for tapping the converter, and the carbon weight percentage of the tapping of the converter is controlled at 0.08-0.12%;
(2)、搬入真空设备后,按每吨钢加入1kg的比例加入增碳剂,提高C—O反应速度; (2) After moving into the vacuum equipment, add carburizer at a rate of 1kg per ton of steel to increase the reaction speed of C—O;
(3)、真空处理时间控制在13-18min,吹氩流量为400-500Nl/min,待钢液面平稳后,破空,搬至LF炉进行处理; (3) The vacuum treatment time is controlled at 13-18min, and the argon blowing flow rate is 400-500Nl/min. After the molten steel level is stable, the vacuum is broken and moved to the LF furnace for treatment;
(4)、自搬入真空设备后的整个真空处理时间控制在35-45min; (4) The entire vacuum treatment time after moving into the vacuum equipment is controlled within 35-45 minutes;
LF炉处理: LF Furnace Treatment:
(1)、LF炉加热处理期间不进行大氩气搅拌,脱硫与调整成分均在高真空条件下进行; (1) During the heating treatment in LF furnace, no large argon gas stirring is carried out, and the desulfurization and composition adjustment are all carried out under high vacuum conditions;
(2)、LF炉炉渣碱度控制在2.8-3.2,温度达到进真空要求后即搬入真空处理区域; (2) The basicity of the LF furnace slag is controlled at 2.8-3.2, and the temperature is moved into the vacuum treatment area after the temperature reaches the vacuum requirement;
(3)、整个LF炉处理时间控制在60-80min; (3) The processing time of the whole LF furnace is controlled within 60-80 minutes;
第二次真空处理要求: Requirements for the second vacuum treatment:
(1)、真空处理时间控制在15min; (1) The vacuum treatment time is controlled at 15 minutes;
(2)、真空处理阶段钢包吹氩流量控制在500Nl/min; (2) During the vacuum treatment stage, the argon blowing flow rate of the ladle is controlled at 500Nl/min;
(3)、此阶段时间控制在35-45min; (3) The time at this stage is controlled within 35-45 minutes;
真空处理结束后,在真空设备上进行弱吹氩: After the vacuum treatment, carry out weak argon blowing on the vacuum equipment:
(1)、弱吹氩流量控制在100-300Nl/min; (1) The flow rate of weak argon blowing is controlled at 100-300Nl/min;
(2)、弱吹氩时间控制在14-16min。 (2) The time of weak argon blowing is controlled at 14-16min.
本发明的积极效果为: The positive effect of the present invention is:
由于本发明针对所要解决的技术问题,采取两次真空处理工艺,第一次真空处理利用碳脱氧,可有效降低钢中自由氧的含量。第二次真空处理可使夹杂物充分上浮,有利于自由氧的排除。 Because the present invention aims at the technical problem to be solved, two vacuum treatment processes are adopted, and the first vacuum treatment utilizes carbon deoxidation, which can effectively reduce the content of free oxygen in the steel. The second vacuum treatment can fully float the inclusions, which is conducive to the removal of free oxygen.
由于在两次真空处理工艺之间加入LF炉处理工艺,既可保证钢水的升温效果,并利用加铝进一步脱除钢中氧含量,形成易于吸附夹杂物的炉渣。同时,在第二次真空处理后期,采取弱吹氩工艺,可进一步促进夹杂物的上浮和排除。 Since the LF furnace treatment process is added between the two vacuum treatment processes, the temperature rise effect of the molten steel can be guaranteed, and the oxygen content in the steel can be further removed by adding aluminum to form a slag that is easy to absorb inclusions. At the same time, in the later stage of the second vacuum treatment, the weak argon blowing process can further promote the floating and removal of inclusions.
经生产实践检验,实施本发明,可以将钢中氧含量稳定控制在5ppm以下,并且实现单浇次平均连浇3罐以上。 Tested in production practice, the implementation of the present invention can stably control the oxygen content in the steel below 5ppm, and realize the average continuous pouring of more than 3 cans in a single pouring time.
具体实施方式 detailed description
采用100吨转炉,100吨LF炉,100吨真空处理设备,生产GCr15钢种。 100-ton converter, 100-ton LF furnace, and 100-ton vacuum treatment equipment are used to produce GCr15 steel.
实施例1: Example 1:
第一次真空处理工艺: The first vacuum treatment process:
1、转炉出钢采取不脱氧、沸腾出钢,转炉出钢碳重量百分比控制在0.09%。 1. Non-deoxidation and boiling tapping are adopted for converter tapping, and the carbon weight percentage of converter tapping is controlled at 0.09%.
2、搬入真空设备后,加入100kg增碳剂,提高C—O反应速度。 2. After moving into the vacuum equipment, add 100kg recarburizer to increase the reaction speed of C—O.
3、真空处理时间控制在15min,吹氩流量为400Nl/min,待钢液面平稳后,破空,搬至LF炉进行处理。 3. The vacuum treatment time is controlled at 15 minutes, and the argon blowing flow rate is 400Nl/min. After the molten steel level is stable, the vacuum is broken and moved to the LF furnace for treatment.
4、整个真空处理时间控制在43min。 4. The entire vacuum treatment time is controlled at 43 minutes.
LF炉处理工艺: LF furnace treatment process:
1、LF炉加热处理期间不进行大氩气搅拌,脱硫与调整成分均在高真空条件下进行。 1. During the heating treatment of LF furnace, there is no argon gas stirring, and the desulfurization and composition adjustment are all carried out under high vacuum conditions.
2、LF炉炉渣碱度控制在2.9,温度达到进真空要求后即搬入真空处理区域。 2. The basicity of LF furnace slag is controlled at 2.9. After the temperature reaches the requirement of vacuum, it will be moved into the vacuum treatment area.
3、此阶段时间控制在65min。 3. The time of this stage is controlled at 65 minutes.
第二次真空处理工艺: The second vacuum treatment process:
1、真空处理时间控制在15min。 1. The vacuum treatment time is controlled at 15 minutes.
2、真空处理阶段钢包吹氩流量控制在500Nl/min。 2. During the vacuum treatment stage, the argon blowing flow rate of the ladle is controlled at 500Nl/min.
3、此阶段时间控制在40min; 3. The time of this stage is controlled within 40 minutes;
真空处理结束后,在真空设备上进行弱吹氩: After the vacuum treatment, carry out weak argon blowing on the vacuum equipment:
弱吹氩流量控制在160Nl/min;弱吹氩时间控制在16min。 The flow rate of weak argon blowing is controlled at 160Nl/min; the time of weak argon blowing is controlled at 16min.
实施例2: Example 2:
第一次真空处理工艺: The first vacuum treatment process:
1、转炉出钢不脱氧、沸腾出钢,转炉出钢碳重量百分比控制在0.11%。 1. Converter tapping without deoxidation, boiling tapping, the weight percentage of carbon in converter tapping is controlled at 0.11%.
2、搬入真空设备后,加入100kg增碳剂。 2. After moving into the vacuum equipment, add 100kg recarburizer.
3、真空处理时间控制在17min,吹氩流量为480Nl/min,待钢液面平稳后,破空,搬至LF炉进行处理。 3. The vacuum treatment time is controlled at 17 minutes, and the argon blowing flow rate is 480Nl/min. After the liquid steel level is stable, the vacuum is broken and moved to the LF furnace for treatment.
4、整个真空处理时间控制在36min。 4. The entire vacuum treatment time is controlled at 36 minutes.
LF炉处理工艺: LF furnace treatment process:
1、LF炉加热处理期间不进行大氩气搅拌,脱硫与调整成分均在高真空条件下进行。 1. During the heating treatment of LF furnace, there is no argon gas stirring, and the desulfurization and composition adjustment are all carried out under high vacuum conditions.
2、LF炉炉渣碱度控制在3.1,温度达到进真空要求后即搬入真空处理区域。 2. The basicity of LF furnace slag is controlled at 3.1. After the temperature reaches the requirement of vacuum, it will be moved into the vacuum treatment area.
3、此阶段时间控制在80min。 3. The time of this stage is controlled at 80 minutes.
第二次真空处理工艺: The second vacuum treatment process:
1、真空处理时间控制在15min。 1. The vacuum treatment time is controlled at 15 minutes.
2、真空处理阶段钢包吹氩流量控制在500Nl/min。 2. During the vacuum treatment stage, the argon blowing flow rate of the ladle is controlled at 500Nl/min.
3、此阶段时间控制在37min。 3. The time of this stage is controlled at 37 minutes.
真空处理结束后,在真空设备上进行弱吹氩: After the vacuum treatment, carry out weak argon blowing on the vacuum equipment:
弱吹氩流量控制在280Nl/min;弱吹氩时间控制在14min。 The flow rate of weak argon blowing is controlled at 280Nl/min; the time of weak argon blowing is controlled at 14min.
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CN103924030B (en) * | 2014-04-09 | 2015-05-06 | 中国科学院金属研究所 | Smelting method of ultra-low oxygen pure steel |
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1676621A (en) * | 2004-03-30 | 2005-10-05 | 宝山钢铁股份有限公司 | Suboxide steel production method |
CN101633974A (en) * | 2009-08-18 | 2010-01-27 | 武汉钢铁(集团)公司 | Smelting process of ultra low oxygen steel |
CN102061351A (en) * | 2010-12-21 | 2011-05-18 | 南阳汉冶特钢有限公司 | Method for producing low-carbon steel and ultra-low-carbon steel by VD, LF and VD processes |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1676621A (en) * | 2004-03-30 | 2005-10-05 | 宝山钢铁股份有限公司 | Suboxide steel production method |
CN101633974A (en) * | 2009-08-18 | 2010-01-27 | 武汉钢铁(集团)公司 | Smelting process of ultra low oxygen steel |
CN102061351A (en) * | 2010-12-21 | 2011-05-18 | 南阳汉冶特钢有限公司 | Method for producing low-carbon steel and ultra-low-carbon steel by VD, LF and VD processes |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108330389A (en) * | 2018-01-31 | 2018-07-27 | 日照钢铁控股集团有限公司 | One kind exempting from Calcium treatment calmness clean steel production technology |
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