JPS6026608A - Method for dephosphorizing molten iron - Google Patents
Method for dephosphorizing molten ironInfo
- Publication number
- JPS6026608A JPS6026608A JP13535283A JP13535283A JPS6026608A JP S6026608 A JPS6026608 A JP S6026608A JP 13535283 A JP13535283 A JP 13535283A JP 13535283 A JP13535283 A JP 13535283A JP S6026608 A JPS6026608 A JP S6026608A
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- cao
- slag
- dephosphorization
- flux
- 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.)
- Pending
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
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/02—Dephosphorising or desulfurising
Landscapes
- 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
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は、溶銑の脱燐方法に関するものである〇〈従来
技術〉
従来、溶銑の脱燐は生石灰を主体とした7ラツクスを用
い、燐の酸化剤として酸化鉄または気体酸素あるいは両
者を生石灰と共に溶銑に添加することによシ酸化した燐
を該反応雰囲気で安定維持する方法がとられて来た。[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to a method for dephosphorizing hot metal. <Prior Art> Conventionally, dephosphorization of hot metal was carried out using 7 lacs mainly composed of quicklime. A method has been adopted in which oxidized phosphorus is stably maintained in the reaction atmosphere by adding iron oxide or gaseous oxygen, or both, together with quicklime, to the hot metal as an oxidizing agent.
一般に生石灰と酸素の適正な添加比率は不明に等しく、
その添加条件については、現場の実験と経験からの模索
状態にあり、種々の添加条件が使用されているのが実状
である。したがって、CaOの脱燐利用効率の低下ある
いは予測を超える脱炭等の問題が生じていた。In general, the appropriate addition ratio of quicklime and oxygen is unknown;
The conditions for addition are still being explored based on field experiments and experience, and the reality is that various addition conditions are being used. Therefore, problems such as a decrease in CaO dephosphorization utilization efficiency and unexpected decarburization have occurred.
上記の問題を解決するだめ、本発明者は種々の実験をし
、検討を重ねた結果、特願昭56−114974で提案
したごとく、生石灰と酸素を溶銑に添加して脱燐するに
際し、生石灰と酸素の重量比Ca O/ 02 を1.
5〜2.5にすると、生石灰および酸素の脱燐利用効率
が最大となり、その結果高い脱燐率が得られることを見
出した。しかしながら、Ca O102重量比1.5〜
2.5を満足させて溶銑中に生石灰と酸素を実際にイン
ジェクションして脱燐したところ、7シツクスの脱燐能
が実験の場合よシも低く、かつCaO吹き込み後、浮上
する経過中およびスラグ層を形成した後に復燐反応が生
じ、CaOO脱燐利用効率が低下するという問題がある
ことが判明した。In order to solve the above problem, the inventor of the present invention conducted various experiments and repeated studies, and as a result, as proposed in Japanese Patent Application No. 56-114974, when quicklime and oxygen are added to hot metal to dephosphorize it, quicklime and oxygen are added to hot metal. The weight ratio of CaO/02 and oxygen is 1.
It has been found that when the ratio is set to 5 to 2.5, the dephosphorization utilization efficiency of quicklime and oxygen becomes maximum, and as a result, a high dephosphorization rate can be obtained. However, CaO102 weight ratio 1.5~
When 2.5 was satisfied and quicklime and oxygen were actually injected into hot metal to dephosphorize it, the dephosphorization ability of 7six was lower than that in the experiment, and the slag and slag during the process of floating after CaO injection were found to be lower than in the experiment. It has been found that there is a problem in that a rephosphorization reaction occurs after the layer is formed, resulting in a decrease in the CaOO dephosphorization utilization efficiency.
実験を重ねた結果、第1図の図表を得た。この図表から
脱燐フラックスが浮上した後yc溶銑上l(浮上したス
ラグ中に、スラグ中のCaO分と酸素量の比が1.5〜
2.5 vcなるように酸素源を供給することIcより
上記問題を解決できることを知得した。As a result of repeated experiments, the diagram shown in Figure 1 was obtained. This diagram shows that after the dephosphorization flux has floated to the top of the yc hot metal (in the floated slag, the ratio of CaO content to oxygen content in the slag is 1.5~
It has been learned that the above problem can be solved by supplying an oxygen source at a voltage of 2.5 vc.
従って本発明はこの知見にもとづいて効率のよい脱燐方
法を提供することを目的とする。Therefore, an object of the present invention is to provide an efficient dephosphorization method based on this knowledge.
〈発明の構成・作用)
本発明は上記の知見をもとVCしてなされたもので、そ
の要旨は、溶銑r生石灰分と酸素量を添加して脱燐する
処理において、溶銑中に吹き込むフラックス中のCa0
重量とCaOと反応する気体酸素および/または酸化鉄
中の酸素の重量との比CaO102を1.5〜2.5
K維持し、フラックスの浮上(Cより生成したトップス
ラグへ酸素および/または酸化鉄を添加してスラグ中の
CaO102重量比を2.5以下vcm持することを特
徴とする溶銑の脱燐方法である。(Structure and operation of the invention) The present invention was made by VC based on the above knowledge, and its gist is that flux blown into hot metal is used in the process of dephosphorizing hot metal by adding quicklime and oxygen. Ca0 inside
The ratio between the weight and the weight of gaseous oxygen and/or oxygen in iron oxide that reacts with CaO102 is 1.5 to 2.5.
A hot metal dephosphorization method characterized by maintaining K and flux flotation (adding oxygen and/or iron oxide to top slag produced from C to maintain a CaO102 weight ratio in the slag of 2.5 vcm or less. be.
ここでCaOと反応する酸素とは理論的ycは供給酸素
の総量から燐より酸化が容易な溶銑中シリコンと反応す
る酸素量をさし引いたものである。The theoretical yc of oxygen that reacts with CaO is the total amount of supplied oxygen minus the amount of oxygen that reacts with silicon in the hot metal, which is easier to oxidize than phosphorus.
〈実施例〉
以下に本発明方法の実施例ycよる脱燐率と比較例によ
る脱燐率とを牙1表VC示し、本発明の効果な明らかに
する。<Example> The dephosphorization rate according to Example yc of the method of the present invention and the dephosphorization rate according to a comparative example are shown in Table 1 below to clarify the effects of the present invention.
下記成分(wt%)の溶銑を牙1表の条件で鍋内で脱燐
した。Hot metal containing the following components (wt%) was dephosphorized in a pot under the conditions listed in Table 1.
C4,5〜4.8%、Sio、t 〜o、s%、MnO
,3〜o、5a10. P O,10〜O112o10
.80.02〜0.04%。C4, 5-4.8%, Sio, t~o, s%, MnO
, 3-o, 5a10. P O,10~O112o10
.. 80.02-0.04%.
上表。例にd件、酸化、、ヤッケーヤ(、。。)および
鉄鉱石あるいは焼結鉱(F e 20s ) を用いた
。Above table. As an example, oxidation, yakkeya (...) and iron ore or sintered ore (F e 20s ) were used.
第1表から明らかなように、吹き込みフラックスのCa
Olo 2 が15〜2.5の範囲を外れ、かつトッ
プ不ラグへの酸素供給がない比較例All、、12では
脱燐が急激に減少し、脱燐率は65チに達しなかった。As is clear from Table 1, Ca of the blown flux
In Comparative Examples All and 12 in which Olo 2 was outside the range of 15 to 2.5 and there was no oxygen supply to the top lag, the dephosphorization decreased rapidly and the dephosphorization rate did not reach 65 degrees.
吹き込みフラックスのCa O10□が1.5〜2.5
の範囲を外れている比較例A 6 、8 、13ではト
ップスラグへ酸素を供給しても脱燐率が70チに達しな
かった。また、吹き込みフラックスのCaO10□を1
.5〜z5に設定しているが、トップスラグへの酸素供
給を行なわなかった比較何屋1,9,10.14では脱
燐率は90チに達しなかった。一方、吹き込みフラック
ス中のCa 102を1.5〜z5に設定し、かつトッ
プスラグに酸素を供給し、トップスラグ中のCaO10
□を2.5より小さくじた本発明例のA 2 、3 、
4 、5 、7では、脱燐率94%以上が安定して得ら
れた。CaO10□ of blown flux is 1.5 to 2.5
In Comparative Examples A 6, 8, and 13, which were outside the range, the dephosphorization rate did not reach 70% even if oxygen was supplied to the top slag. In addition, CaO10□ of the blown flux was added to 1
.. 5 to z5, but the dephosphorization rate did not reach 90 in comparison products No. 1, 9, and 10.14, which did not supply oxygen to the top slag. On the other hand, by setting Ca102 in the blown flux to 1.5 to z5 and supplying oxygen to the top slag, CaO102 in the top slag
A 2, 3 of the present invention example in which □ is smaller than 2.5,
In samples 4, 5, and 7, a dephosphorization rate of 94% or more was stably obtained.
なお、43とAIOの例では吹き込み7ラツクス中の酸
素源として酸化鉄を使用したが酸素ガスの場合と脱燐率
に差がなかった。また、扁7と8υ例ではトップスラグ
へ供給する酸素源として酸化鉄を使用したが、酸素ガス
の場合と脱燐率に差がなかった。Incidentally, in the examples of No. 43 and AIO, iron oxide was used as the oxygen source in the blown 7 lux, but there was no difference in the dephosphorization rate compared to the case of oxygen gas. Furthermore, in the 7 and 8 υ cases, iron oxide was used as the oxygen source to be supplied to the top slag, but there was no difference in the dephosphorization rate compared to the case of oxygen gas.
〈発明の効果〉
以上説明したように本発明方法によれば、溶銑を脱燐す
る際に吹き込み7ラツクスのCa O102重量比を1
.5〜2.5とし、トップスラグのCaO10□比を2
.5以下に維持するので、酸素および生石灰の利用効率
を高く保つことができ従来法に比べて少ないフラックス
等で必要な脱燐レベルを達成でき、酸素および生石灰の
原単位の大幅減少が可能となシ、多大の経済的効果が得
られる。<Effects of the Invention> As explained above, according to the method of the present invention, when dephosphorizing hot metal, the weight ratio of CaO102 of 7 lux of blown iron is reduced to 1.
.. 5 to 2.5, and the CaO10□ ratio of the top slag is 2.
.. 5 or less, the utilization efficiency of oxygen and quicklime can be kept high, and the required level of dephosphorization can be achieved with less flux compared to conventional methods, making it possible to significantly reduce the basic unit of oxygen and quicklime. Therefore, a large economic effect can be obtained.
第1図はトップスラグに酵素を供給した場合および供給
のない場合のスラックス中のCa O/ 02重量比と
脱燐率との関係を示す図である。
代理人 弁理士 秋 沢 政 光
外2名FIG. 1 is a diagram showing the relationship between the CaO/02 weight ratio in the slack and the dephosphorization rate when an enzyme is supplied to the top slag and when no enzyme is supplied. Agent: Patent attorney Masaaki Akizawa, Mitsugai (2 people)
Claims (1)
において、溶銑中に吹き込む7ラツクス中のCaO重量
とCaOと反応する気体酸素および/または酸化鉄中の
酸素の重量との比CaO10t を1.5〜2.5に維
持し、ノラックスの浮上によシ生成したトップスラグへ
酸素および/または酸化鉄を添加してスラグ中のCaO
10□ 重量比を2.5以下に維持することを特徴とす
る溶銑の脱燐方法。(1) In the process of dephosphorizing hot metal by adding quicklime and oxygen, the ratio of the weight of CaO in 7 lux injected into hot metal to the weight of gaseous oxygen and/or oxygen in iron oxide that reacts with CaO CaO10t is maintained at 1.5 to 2.5, and oxygen and/or iron oxide is added to the top slag produced by the floating of Norax to remove CaO in the slag.
10□ A method for dephosphorizing hot metal, characterized by maintaining a weight ratio of 2.5 or less.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13535283A JPS6026608A (en) | 1983-07-25 | 1983-07-25 | Method for dephosphorizing molten iron |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13535283A JPS6026608A (en) | 1983-07-25 | 1983-07-25 | Method for dephosphorizing molten iron |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6026608A true JPS6026608A (en) | 1985-02-09 |
Family
ID=15149745
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13535283A Pending JPS6026608A (en) | 1983-07-25 | 1983-07-25 | Method for dephosphorizing molten iron |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6026608A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01215916A (en) * | 1988-02-24 | 1989-08-29 | Nippon Steel Corp | Method for treating dephosphorization of molten iron |
JPH0270014A (en) * | 1988-09-06 | 1990-03-08 | Nippon Steel Corp | Dephosphorization treatment of molten iron |
-
1983
- 1983-07-25 JP JP13535283A patent/JPS6026608A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01215916A (en) * | 1988-02-24 | 1989-08-29 | Nippon Steel Corp | Method for treating dephosphorization of molten iron |
JPH0514003B2 (en) * | 1988-02-24 | 1993-02-24 | Nippon Steel Corp | |
JPH0270014A (en) * | 1988-09-06 | 1990-03-08 | Nippon Steel Corp | Dephosphorization treatment of molten iron |
JPH0514004B2 (en) * | 1988-09-06 | 1993-02-24 | Nippon Steel Corp |
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