CN107012283B - Converter slag retention method - Google Patents
Converter slag retention method Download PDFInfo
- Publication number
- CN107012283B CN107012283B CN201610059280.2A CN201610059280A CN107012283B CN 107012283 B CN107012283 B CN 107012283B CN 201610059280 A CN201610059280 A CN 201610059280A CN 107012283 B CN107012283 B CN 107012283B
- Authority
- CN
- China
- Prior art keywords
- slag
- converter
- splashing
- slag splashing
- shake
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/36—Processes yielding slags of special composition
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Abstract
本发明提供一种转炉留渣方法,根据上炉冶炼终点温度和氧值进行倒渣角度控制,倒渣结束转炉摇至零位,采用氮气溅渣,溅渣时加入溅渣剂;溅渣结束前加入活性白灰和轻烧白云石进行稠渣;溅渣结束后,转炉摇至90°~98°,对渣况进行确认,确认后加废钢兑铁水,兑铁结束吹炼时氧气流量采用25000~26500Nm3/h,枪位2100~2250mm。本发明可避免兑铁时产生喷爆现象,消除安全隐患,避免吹炼前期因打不着火造成的干法除尘泄爆问题,稳定生产节奏,保证设备安全;同时,能够极大减少熔剂消耗,使每炉次活性白灰和轻烧白云石用量分别降低11.1kg/t钢和8kg/t钢,从而有效降低冶炼成本。The invention provides a method for leaving slag in a converter. The slag pouring angle is controlled according to the end temperature of the upper furnace smelting and the oxygen value. After the slag pouring is completed, the converter is shaken to zero position, nitrogen gas is used to splash the slag, and a slag splashing agent is added during the slag splashing; the slag splashing is finished Add activated lime and light-burned dolomite before the thick slag; after the slag splashing, the converter is shaken to 90°~98°, and the slag condition is confirmed. ~26500Nm 3 /h, gun position 2100~2250mm. The present invention can avoid explosion phenomenon when mixing iron, eliminate potential safety hazards, avoid the problem of dry dust removal and explosion relief caused by failure of ignition in the early stage of blowing, stabilize production rhythm, and ensure equipment safety; at the same time, it can greatly reduce flux consumption, The amount of active lime and light-burned dolomite per furnace is reduced by 11.1kg/t steel and 8kg/t steel respectively, thereby effectively reducing smelting costs.
Description
技术领域technical field
本发明属于炼钢工艺技术领域,特别涉及一种在干法除尘条件下防止干法泄爆,降低熔剂单耗的转炉留渣方法。The invention belongs to the technical field of steelmaking technology, and in particular relates to a converter slag retention method for preventing dry explosion venting and reducing the unit consumption of flux under the condition of dry dust removal.
背景技术Background technique
降低转炉冶炼成本一直是炼钢厂的一个重要控制指标,其中熔剂成分占炼钢成本较大份额,因此降低炼钢熔剂成本势在必行。通常情况下,配有干法除尘的转炉炼钢在溅渣后都将熔渣倒掉,因为留渣量不合适会造成吹炼时打火不畅,进而造成干法除尘泄爆,严重时会损坏干法除尘设备。Reducing the cost of converter smelting has always been an important control indicator for steelmaking plants, in which flux components account for a large share of steelmaking costs, so it is imperative to reduce the cost of steelmaking fluxes. Usually, the slag is poured out after splashing slag in converter steelmaking equipped with dry dust removal, because the unsuitable amount of slag left will cause poor ignition during blowing, which will cause dry dust removal and explosion relief, and in severe cases Will damage the dry dust removal equipment.
发明内容Contents of the invention
本发明旨在提供一种可杜绝吹炼时打火不畅现象,避免兑铁时产生喷爆,减少熔剂消耗,降低冶炼成本的转炉留渣方法。The present invention aims to provide a method for leaving slag in a converter that can prevent poor ignition during blowing, avoid blasting during iron mixing, reduce flux consumption, and reduce smelting costs.
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:
一种转炉留渣方法,其具体方法和步骤为:A method for leaving slag in a converter, its specific method and steps are:
(1)根据上炉冶炼终点温度和氧值进行倒渣角度控制,上炉冶炼终点出钢温度T和出钢氧值[O]对应的倒渣角度为:(1) Carry out slagging angle control according to the end point temperature and oxygen value of upper furnace smelting, the corresponding slagging angle of tapping temperature T at the end point of upper furnace smelting and tapping oxygen value [O] is:
(2)倒渣结束后,转炉摇至零位,采用氮气溅渣,氮气流量38000~42000Nm3/h,溅渣枪位从2000mm逐渐降至500mm,溅渣时溅渣剂加入量如步骤(1)所示,溅渣时间控制在2~4min;(2) After the slag pouring is finished, shake the converter to zero position, use nitrogen gas for slag splashing, the flow rate of nitrogen gas is 38000-42000Nm 3 /h, the position of the slag splashing gun is gradually reduced from 2000mm to 500mm, and the amount of slag splashing agent added during slag splashing is as follows ( As shown in 1), the slag splashing time is controlled within 2 to 4 minutes;
(3)溅渣结束前18~22s加入活性白灰和轻烧白云石各980~1050kg进行稠渣;(3) 18-22 seconds before the end of slag splashing, add 980-1050 kg of active lime and lightly burned dolomite to make thick slag;
(4)溅渣结束后,转炉摇至90°~98°,对渣况进行确认,确保熔渣溅干;(4) After the slag splashing is over, the converter is shaken to 90°~98°, and the slag condition is confirmed to ensure that the slag is splashed dry;
(5)炉渣确认后加废钢兑铁水,兑铁时间控制在4~6min;(5) After the slag is confirmed, add scrap steel to molten iron, and the iron mixing time is controlled at 4 to 6 minutes;
(6)兑铁结束吹炼时氧气流量采用25000~26500Nm3/h,枪位2100~2250mm,开始吹炼30s如果打火不畅,立即抬枪摇炉,摇炉时向炉后摇至-40°,向前摇至60°,然后将转炉摇至零位继续吹炼。(6) The oxygen flow rate is 25000-26500Nm 3 /h at the end of blowing after mixing iron, and the gun position is 2100-2250mm. If the ignition is not smooth after starting blowing for 30 seconds, immediately raise the gun and shake the furnace, and shake the furnace backward to - 40°, shake forward to 60°, then shake the converter to zero position to continue blowing.
所述溅渣剂主要含有C和MgO,其中含C:9~11wt%,含MgO:55~60wt%。本发明的有益效果为:The slag splashing agent mainly contains C and MgO, wherein C: 9-11wt%, MgO: 55-60wt%. The beneficial effects of the present invention are:
采用本发明先倒渣、后溅渣以及稠渣的方法,可避免兑铁时产生喷爆现象,消除了安全隐患;通过合理控制留渣量,避免了吹炼前期因打不着火造成的干法除尘泄爆问题,稳定了生产节奏,保证了设备安全;同时,本发明能够极大减少熔剂消耗,使每炉次活性白灰和轻烧白云石用量分别降低11.1kg/t钢和8kg/t钢,从而有效降低了冶炼成本。The method of pouring slag first, then splashing slag and thick slag in the present invention can avoid the phenomenon of blasting when mixing iron, and eliminate potential safety hazards; by reasonably controlling the amount of slag remaining, dryness caused by failure to ignite in the early stage of blowing can be avoided. The problem of dedusting and explosion relief by means of method stabilizes the production rhythm and ensures the safety of equipment; at the same time, the invention can greatly reduce the consumption of flux, reducing the consumption of active lime and light-burned dolomite by 11.1kg/t steel and 8kg/t respectively per furnace. steel, thereby effectively reducing the cost of smelting.
具体实施方式Detailed ways
溅渣剂含C:9~11wt%,含MgO:55~60wt%。The slag splashing agent contains C: 9-11wt%, and MgO: 55-60wt%.
实施例1:Example 1:
1、上炉冶炼终点出钢温度T1710℃,出钢氧值[O]840ppm,确定倒渣角度116°。1. The tapping temperature at the end of the upper furnace smelting is T1710℃, the tapping oxygen value [O] is 840ppm, and the slag pouring angle is determined to be 116°.
2、倒渣结束后,转炉摇至零位,采用氮气溅渣,氮气流量39500Nm3/h,溅渣枪位由高到低,从2000mm逐渐降至500mm,溅渣时溅渣剂加入量为2.75kg/t钢,溅渣时间4min。2. After the slag pouring is finished, shake the converter to zero position, use nitrogen gas for slag splashing, the nitrogen flow rate is 39500Nm 3 /h, the position of the slag splashing gun is gradually reduced from high to low, from 2000mm to 500mm, and the amount of slag splashing agent added during slag splashing is 2.75kg/t steel, slag splashing time 4min.
3、溅渣结束前20s加入活性白灰和轻烧白云石各1000kg进行稠渣。3. Add 1000kg of activated lime and lightly burned dolomite 20s before the end of slag splashing to make thick slag.
4、溅渣结束后,转炉摇至95°,对渣况进行确认,确保熔渣溅干。4. After the slag splash is over, the converter is shaken to 95°, and the slag condition is confirmed to ensure that the slag is splashed dry.
5、炉渣确认后加废钢兑铁水,兑铁时小流慢兑,时间控制在5min。5. After the slag is confirmed, add scrap steel to molten iron. When mixing iron, it is mixed slowly in a small flow, and the time is controlled within 5 minutes.
6、兑铁结束吹炼时氧气流量采用26000Nm3/h,枪位2200mm。开始吹炼30s出现打火不畅,立即抬枪摇炉,摇炉时向炉后摇至-40°,向前摇至60°,然后将转炉摇至零位继续吹炼。6. The oxygen flow rate is 26000Nm 3 /h and the gun position is 2200mm when the blowing is completed. If the ignition is not smooth after 30 seconds of blowing, immediately raise the gun and shake the furnace. When shaking the furnace, shake the furnace backward to -40° and forward to 60°, and then shake the converter to zero to continue blowing.
实施例2:Example 2:
1、上炉冶炼终点出钢温度T1650℃,出钢氧值[O]855ppm,确定倒渣角度为106°。1. The tapping temperature at the end of upper furnace smelting is T1650℃, the tapping oxygen value [O] is 855ppm, and the slag pouring angle is determined to be 106°.
2、倒渣结束后,转炉摇至零位,采用氮气溅渣,氮气流量40000Nm3/h,溅渣枪位由高到低,从2000mm逐渐降至500mm,溅渣时溅渣剂加入量为1.65kg/t钢,溅渣时间2.5min。2. After the slag pouring is finished, shake the converter to zero position, use nitrogen gas for slag splashing, the nitrogen flow rate is 40000Nm 3 /h, the position of the slag splashing gun is gradually reduced from high to low, from 2000mm to 500mm, and the amount of slag splashing agent added during slag splashing is 1.65kg/t steel, slag splashing time 2.5min.
3、溅渣结束前19s加入活性白灰990kg、轻烧白云石1020kg进行稠渣。3. Add 990kg of activated lime and 1020kg of lightly burned dolomite 19s before the end of slag splashing to make thick slag.
4、溅渣结束后,转炉摇至95°,对渣况进行确认,确保熔渣溅干。4. After the slag splash is over, the converter is shaken to 95°, and the slag condition is confirmed to ensure that the slag is splashed dry.
5、炉渣确认后加废钢兑铁水,兑铁时小流慢兑,时间控制在5.5min。5. After the slag is confirmed, add scrap steel to molten iron. When mixing iron, add it in a small flow and slowly, and the time is controlled at 5.5 minutes.
6、兑铁结束吹炼时氧气流量采用25500Nm3/h,枪位2150mm。6. The oxygen flow rate is 25500Nm 3 /h and the gun position is 2150mm when the blowing is completed.
实施例3:Example 3:
1、上炉冶炼终点出钢温度T1690℃,出钢氧值[O]840ppm,确定倒渣角度为109°。1. The tapping temperature at the end of the upper furnace smelting is T1690℃, the tapping oxygen value [O] is 840ppm, and the slag pouring angle is determined to be 109°.
2、倒渣结束后,转炉摇至零位,采用氮气溅渣,氮气流量41000Nm3/h,溅渣枪位由高到低,从2000mm逐渐降至500mm,溅渣时溅渣剂加入量为2.2kg/t钢,溅渣时间3min。2. After the slag pouring is completed, the converter is shaken to zero position, nitrogen slag splashing is used, the nitrogen flow rate is 41000Nm 3 /h, the slag splashing gun position is gradually reduced from high to low, from 2000mm to 500mm, and the amount of slag splashing agent added during slag splashing is 2.2kg/t steel, slag splashing time 3min.
3、溅渣结束前21s加入活性白灰1010kg、轻烧白云石990kg进行稠渣。3. Add 1010kg of activated lime and 990kg of lightly burned dolomite 21s before the end of slag splashing to make thick slag.
4、溅渣结束后,转炉摇至95°,对渣况进行确认,确保熔渣溅干。4. After the slag splash is over, the converter is shaken to 95°, and the slag condition is confirmed to ensure that the slag is splashed dry.
5、炉渣确认后加废钢兑铁水,兑铁时小流慢兑,时间控制在4.5min。5. After the slag is confirmed, add scrap steel to molten iron. When mixing iron, it will be mixed in a small flow and slowly, and the time will be controlled within 4.5 minutes.
6、兑铁结束吹炼时氧气流量采用26200Nm3/h,枪位2210mm。6. The oxygen flow rate is 26200Nm 3 /h and the gun position is 2210mm when the blowing is completed.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610059280.2A CN107012283B (en) | 2016-01-27 | 2016-01-27 | Converter slag retention method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610059280.2A CN107012283B (en) | 2016-01-27 | 2016-01-27 | Converter slag retention method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN107012283A CN107012283A (en) | 2017-08-04 |
CN107012283B true CN107012283B (en) | 2018-10-09 |
Family
ID=59438624
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610059280.2A Active CN107012283B (en) | 2016-01-27 | 2016-01-27 | Converter slag retention method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107012283B (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110656215A (en) * | 2019-09-27 | 2020-01-07 | 山东钢铁股份有限公司 | Method for preventing unsuccessful blowing and igniting of converter |
CN113201618A (en) * | 2021-03-19 | 2021-08-03 | 阳春新钢铁有限责任公司 | Production method for reducing down-converter times and reducing tapping temperature |
CN113388713A (en) * | 2021-05-25 | 2021-09-14 | 鞍钢股份有限公司 | Treatment method for converter blowing oxygen lance incapable of normally striking fire |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102337372A (en) * | 2011-10-27 | 2012-02-01 | 北京科技大学 | Cooling solidification recycling method for high-temperature liquid-state slag in steelmaking furnace |
CN102888487A (en) * | 2012-10-12 | 2013-01-23 | 武汉钢铁(集团)公司 | High-efficiency remaining slag smelting method of converters |
CN102925621A (en) * | 2012-11-13 | 2013-02-13 | 攀钢集团研究院有限公司 | Method for preventing dry dedusting system of semi-steel steel converter from explosion venting |
CN104451023A (en) * | 2013-09-24 | 2015-03-25 | 上海梅山钢铁股份有限公司 | Smelting method for retaining hot dreg of converter |
CA2851604C (en) * | 2012-06-27 | 2015-11-10 | Nippon Steel & Sumitomo Metal Corporation | Method of reduction processing of steel-making slag |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4267190B2 (en) * | 2000-09-14 | 2009-05-27 | 新日本製鐵株式会社 | Effective use of fly ash and iron-containing waste |
-
2016
- 2016-01-27 CN CN201610059280.2A patent/CN107012283B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102337372A (en) * | 2011-10-27 | 2012-02-01 | 北京科技大学 | Cooling solidification recycling method for high-temperature liquid-state slag in steelmaking furnace |
CA2851604C (en) * | 2012-06-27 | 2015-11-10 | Nippon Steel & Sumitomo Metal Corporation | Method of reduction processing of steel-making slag |
CN102888487A (en) * | 2012-10-12 | 2013-01-23 | 武汉钢铁(集团)公司 | High-efficiency remaining slag smelting method of converters |
CN102925621A (en) * | 2012-11-13 | 2013-02-13 | 攀钢集团研究院有限公司 | Method for preventing dry dedusting system of semi-steel steel converter from explosion venting |
CN104451023A (en) * | 2013-09-24 | 2015-03-25 | 上海梅山钢铁股份有限公司 | Smelting method for retaining hot dreg of converter |
Also Published As
Publication number | Publication date |
---|---|
CN107012283A (en) | 2017-08-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101956040B (en) | Producing method of clean steel | |
CN103173586B (en) | Method for lowering contents of oxygen and nitrogen in molten steel at smelting end in semisteel smelting converter | |
CN105112595A (en) | Smelting method capable of realizing phosphorus content of less than 70ppm in high-carbon converter tapping | |
CN103397133B (en) | Method for protecting converter with vanadium slag | |
CN110117689B (en) | A method for smelting low phosphorus steel based on high silicon molten iron converter double slag method | |
CN107012283B (en) | Converter slag retention method | |
CN105525055A (en) | Method for controlling splashing in less slag smelting decarbonization period of converter | |
CN103103308A (en) | Method for controlling phosphorus content of end point molten steel smelted by a top-bottom combined blowing converter to be less than 30 ppm | |
CN103627842A (en) | Method for enhancing end point carbon content in smelting medium-carbon steel from semisteel and semisteel steelmaking method | |
CN103627843B (en) | Semi-steel making slagging method and Semi-steel making method | |
CN108998614A (en) | Smelting method of ultra-low manganese steel | |
CN104195290A (en) | Molten steel dephosphorization agent and molten steel dephosphorization refining method | |
CN106148629B (en) | Method for controlling manganese content of high-manganese molten iron end point | |
CN103290163A (en) | Semisteel steelmaking method | |
CN102965465A (en) | Method for curing converter slag | |
CN106148632A (en) | Economical converter less-slag combined blowing smelting process | |
CN104017932B (en) | The method of the two slag steel-making of a kind of converter | |
CN103397132B (en) | A method for improving the anti-corrosion ability of vanadium extracting converter lining | |
CN105296703B (en) | Method for smelting phosphorus-containing steel by top-bottom combined blown converter | |
CN104109727B (en) | The method of half steel converter smelting Low-phosphorus Steel | |
CN104060017B (en) | A kind of method of semisteel converter steelmaking | |
CN103060514B (en) | Slag-making method and semi-steel smelting method capable of preventing semi-steel steel-making converter from dedusting and exploding | |
CN104789732A (en) | Method for slagging in semisteel steelmaking converter | |
CN105714012A (en) | Converter less-slag smelting method for high-silicon molten iron | |
CN104745760A (en) | Slag-splashing furnace protection method of converter |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |