Optimization of 180 t LF Deep Desulphurization Refining Process for Pipeline Steel X70
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Optimization of 180 t LF Deep Desulphurization Refining Process for Pipeline Steel X70
Special SteelVol. 34, Issue 5, Pages: 47-50(2013)
作者机构:
1. 江苏省沙钢 1 钢铁研究院
2. 宏发炼钢厂,张家港,215625
作者简介:
基金信息:
DOI:
CLC:
Received:24 April 2013,
Online First:22 September 2022,
Published:22 September 2013
稿件说明:
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邹长东, 赵家七, 周彦召, et al. Optimization of 180 t LF Deep Desulphurization Refining Process for Pipeline Steel X70[J]. Special Steel, 2013, 34(5): 47-50.
DOI:
邹长东, 赵家七, 周彦召, et al. Optimization of 180 t LF Deep Desulphurization Refining Process for Pipeline Steel X70[J]. Special Steel, 2013, 34(5): 47-50.DOI:
Optimization of 180 t LF Deep Desulphurization Refining Process for Pipeline Steel X70
X70管线钢的生产流程为KR铁水预脱硫-180 t BOF-LF-RH-板坯连铸工艺。通过优化精炼渣成分和造渣制度
以及根据底吹流量(400-700 L/min)对终点[S
]
的影响
制定了LF深脱硫工艺。生产试验结果表明
通过控制精炼渣成分(/%)45~55CaO、30~40Al
2
O
3
、≤10SiO
2
、≤10MgO、≤1.5(TFe+MnO)
造渣时分两批(首次出钢过程第二批LF到站加入)或多批加入石灰
精炼过程根据炉渣情况适当调渣
LF精炼脱硫期的底吹气体流量为500~700 L/min
可在40 min内将钢液[S
]
降低到10×10
-6
以下
满足了管线钢快速深脱硫的需求。
Abstract
The production flow sheet for pipeline steel X70 is KR metal pre-desulphuration-180 t BOF-LF-RH-slab CC process. With optimization of refining slag ingredient and slagging operation
and based on effect of bottom gas blowing rate (400-700 L/min) on end [S
]
the LF deep desulphurization process has been schemed. Pilot production results show that by controlling refining slag ingredient (/% ) 45-55CaO
30-40Al
2
O
3
≤10SiO
2
≤10Mgo
≤1.5(TFe + MnO)
with the technology measures including during slagging the lime being added in two separate batch (first in tapping
second at beginning of LF refining) or being added in multi-batch
during LF refining according to slag condition adjusting ingredient of slag
and bottom gas blowing rate 500-700 L/min during LF desulphurization period
the sulphur content in liquid-
[S
]
could be decreased to lower than 10 x 10
-6
in 40 min to meet the requirement of quick deep desulphurization for pipeline steel.