JPH07107174B2 - Solid fuel injection method and injection device for electric furnace and converter - Google Patents
Solid fuel injection method and injection device for electric furnace and converterInfo
- Publication number
- JPH07107174B2 JPH07107174B2 JP11148986A JP11148986A JPH07107174B2 JP H07107174 B2 JPH07107174 B2 JP H07107174B2 JP 11148986 A JP11148986 A JP 11148986A JP 11148986 A JP11148986 A JP 11148986A JP H07107174 B2 JPH07107174 B2 JP H07107174B2
- Authority
- JP
- Japan
- Prior art keywords
- electric furnace
- converter
- furnace
- solid fuel
- combustion chamber
- 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.)
- Expired - Lifetime
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Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Carbon Steel Or Casting Steel Manufacturing (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、例えば屑鉄等の被溶解原材料を溶解して溶鋼
を製造する電気炉又は転炉において上記原材料を予熱,
溶解する方法及び該方法の実施に適した予熱,溶解装置
に関し、特に電気炉では固体燃料を用いた場合の電力原
単位の改善,転炉では低コストの熱補償法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention preheats the above raw materials in an electric furnace or a converter for melting molten raw materials such as scrap iron to produce molten steel,
The present invention relates to a melting method and preheating and melting equipment suitable for carrying out the method, and more particularly, to improvement of an electric power consumption rate when a solid fuel is used in an electric furnace, and a low-cost heat compensation method in a converter.
従来、屑鉄等を溶かして溶鋼を製造する電気炉におい
て、電力原単位を低減するための方法として、助燃バー
ナにより重油あるいは灯油を炉内に吹き込んだり、ある
いは酸素富化を行ったりする方法がある。例えば酸素吹
込量を理論酸素量の1.3〜1.4倍で酸素富化させることに
よって電力原単位は3〜5kwH/t減少する。20T/Hの電気
炉の操業を例にとると、最大灯油500l/hの吹込みでは電
力原単位は約10%の減少となる。Conventionally, in an electric furnace that manufactures molten steel by melting scrap iron, etc., there is a method of blowing heavy oil or kerosene into the furnace with an auxiliary combustion burner, or enriching oxygen, as a method for reducing the electric power consumption rate. . For example, by enriching the amount of oxygen blown with 1.3 to 1.4 times the theoretical amount of oxygen, the electric power consumption rate is reduced by 3 to 5 kwH / t. Taking the operation of an electric furnace of 20 T / H as an example, when the maximum kerosene of 500 l / h is injected, the electricity consumption rate will decrease by about 10%.
第3図及び第4図はこのような従来装置を示し、図にお
いて、1は電気炉であり、これは耐火材で内張りされた
炉本体1aの上面に炉蓋1bを開閉自在に装着し、炉内に電
極6を挿入してなる。なお、1cは排気ガスを煙突に導く
煙道である。上記炉本体1aの側壁には多数の助燃バーナ
2が炉内の原材料,ひいては溶鋼3の上面に向けて配設
されている。上記助燃バーナ2はその中心部に空気ノズ
ル2a,及び油ノズル2bを、これの外方に酸素ノズル2cを
それぞれ配置し、これらの外方を冷却水ケーシング2dに
囲んだ構成となっている。3 and 4 show such a conventional apparatus, in which 1 is an electric furnace in which a furnace lid 1b is openably and closably mounted on the upper surface of a furnace body 1a lined with a refractory material, The electrode 6 is inserted into the furnace. Note that 1c is a flue that guides the exhaust gas to the chimney. A large number of auxiliary burners 2 are arranged on the side wall of the furnace main body 1a toward the raw materials in the furnace, and further toward the upper surface of the molten steel 3. The auxiliary burner 2 has a structure in which an air nozzle 2a and an oil nozzle 2b are arranged at the center thereof, and an oxygen nozzle 2c is arranged outside thereof, and the outside is surrounded by a cooling water casing 2d.
この従来装置では、重油又は灯油と空気とが助燃バーナ
2によって電気炉1内の溶鋼3の上面から吹き込まれ、
さらに酸素吹込みランスによって酸素が溶鋼3中に吹き
込まれ、酸素富化が行われる。これにより上記助燃バー
ナ2による予熱及び酸素富化に応じて電力原単位が減少
することとなる。In this conventional apparatus, heavy oil or kerosene and air are blown from the upper surface of the molten steel 3 in the electric furnace 1 by the auxiliary combustion burner 2,
Further, oxygen is blown into the molten steel 3 by the oxygen blowing lance to enrich the oxygen. As a result, the electric power consumption rate is reduced according to the preheating and oxygen enrichment by the auxiliary burner 2.
しかしながら、上記従来装置では、重油又は灯油の吹込
み量を増大しても電力原単位はそれほど減少できない。
その理由としては、以下の点が考えられる。即ち、上記
従来装置では、重油又は灯油を炉内に吹き込み、炉内で
燃焼させる方式であるので、低温の屑鉄に重油等が当た
り、これらの温度が上昇しにくかったり,未燃焼のスモ
ークを発生したりする点、また、一般に炉内は還元性雰
囲気であるので上記重油等の完全燃焼は困難であり、結
局重油等の顕熱を有効に利用できない点に基づく。However, in the above conventional device, the electric power consumption rate cannot be reduced so much even if the injection amount of heavy oil or kerosene is increased.
The reason is considered as follows. That is, in the above conventional apparatus, since heavy oil or kerosene is blown into the furnace and burned in the furnace, low temperature scrap iron is hit with heavy oil or the like, and it is difficult for these temperatures to rise, or unburned smoke is generated. This is because it is difficult to completely combust the above heavy oil and the like because the inside of the furnace is in a reducing atmosphere in general and the sensible heat of the heavy oil and the like cannot be effectively used.
本発明の目的は、上記従来の問題点を解消して吹込み用
補助燃料の顕熱を有効に利用でき、電気炉では電力原単
位を大幅に向上でき、転炉では低コストで鉄屑精練がで
きる電気炉,転炉の固体燃料吹込み方法及び吹込み装置
を提供する点にある。The object of the present invention is to eliminate the above-mentioned conventional problems and to effectively utilize the sensible heat of the auxiliary fuel for injection, to significantly improve the electric power consumption rate in the electric furnace, and in the converter to refine the iron scrap at low cost. It is an object of the present invention to provide an electric furnace, a method for injecting solid fuel in a converter, and an injecting device capable of performing the above.
そこで本願の第1発明は、電気炉,転炉の固体燃料吹込
み方法において、固体燃料を電気炉,又は転炉の炉外に
て空燃比1.0以下で1次燃焼させ、さらに該未燃焼ガス
を電気炉の入口付近にて2次燃焼させ、該二段燃焼によ
る高温の排気ガスを炉内に吹き込むようにしたことを特
徴としている。Therefore, the first invention of the present application is a solid fuel injection method for an electric furnace or a converter, in which solid fuel is primarily burned outside the furnace of the electric furnace or the converter at an air-fuel ratio of 1.0 or less, and the unburned gas is further burned. Is secondarily combusted in the vicinity of the inlet of the electric furnace, and high-temperature exhaust gas produced by the second-stage combustion is blown into the furnace.
また、第2発明は、電気炉,転炉の固体燃料吹込み装置
において、電気炉,又は転炉の炉外に固体燃料と1次空
気を供給して空燃比1.0以下で燃焼させる1次燃焼室を
形成し、電気炉,又は転炉の入口部に、上記1次燃焼室
からの未燃焼ガスに2次空気を供給して2次燃焼させる
とともに、この二段燃焼による高温の排気ガスを炉内に
吹込む2次燃焼室を形成したことを特徴としている。A second aspect of the present invention is, in a solid fuel injection device for an electric furnace or a converter, a primary combustion in which solid fuel and primary air are supplied to the outside of the electric furnace or the converter to burn at an air-fuel ratio of 1.0 or less. A chamber is formed, and secondary air is supplied to the unburned gas from the primary combustion chamber for secondary combustion at the inlet of the electric furnace or the converter, and high-temperature exhaust gas due to this two-stage combustion is generated. The feature is that a secondary combustion chamber blown into the furnace is formed.
本発明に係る電気炉,転炉の固体燃料吹込み方法及び装
置によれば、固体燃料を、まず炉外で空燃比1.0以下で
1次燃焼させ、さらに電気炉入口部で2次燃焼させるよ
うに、即ち二段燃焼させるようにしたので、固体燃料を
略完全燃焼させることができ、この完全燃焼による高温
の排気ガスによって屑鉄等を予熱,溶解でき、これによ
り、従来の重油等を直接炉内に吹き込む場合に比較して
予熱,溶解用補助燃料の有する顕熱の利用率を大きき向
上でき、その結果電力原単位を低減できる。According to the method and apparatus for injecting solid fuel in the electric furnace and the converter according to the present invention, the solid fuel is firstly burned outside the furnace at an air-fuel ratio of 1.0 or less, and then secondarily burned at the inlet of the electric furnace. In other words, since the two-stage combustion is performed, the solid fuel can be almost completely burned, and the scrap iron and the like can be preheated and melted by the high-temperature exhaust gas due to this complete combustion. The utilization ratio of preheat and sensible heat of the auxiliary fuel for melting can be greatly improved as compared with the case of blowing into the interior, and as a result, the power consumption rate can be reduced.
以下、本発明の実施例を図について説明する。 Embodiments of the present invention will be described below with reference to the drawings.
第1図は本願の第2発明の一実施例による電気炉の固定
燃料吹込み装置を示す。図において、第3図と同一符号
は同一又は相当部分を示し、電気炉本体1aの側方には1
次燃焼室4が設置されている。該1次燃焼室4は、内面
が耐火材で内張りされた円筒状のもので、その軸芯は炉
内の溶鋼3の中心部に向いている。またこの1次燃焼室
4の側壁には1次空気又は酸素をその円周方向に吹き込
むための空気吹込管4a,4aが接続されている。該空気吹
込管4a,4aには微粉炭を吹き込むためのバーナ4cが挿入
されている。またこの1次燃焼室4の下面部には、上記
固体燃料から生成される灰分を回収するための灰ポット
4bが形成されている。FIG. 1 shows a fixed fuel injection device for an electric furnace according to an embodiment of the second invention of the present application. In the figure, the same reference numerals as those in FIG.
The next combustion chamber 4 is installed. The primary combustion chamber 4 has a cylindrical shape whose inner surface is lined with a refractory material, and its axis is directed to the center of the molten steel 3 in the furnace. Further, air blowing pipes 4a, 4a for blowing the primary air or oxygen in the circumferential direction are connected to the side wall of the primary combustion chamber 4. A burner 4c for blowing pulverized coal is inserted in the air blowing pipes 4a, 4a. An ash pot for collecting ash produced from the solid fuel is provided on the lower surface of the primary combustion chamber 4.
4b is formed.
そして上記1次燃焼室4の先端部には、2次燃焼室5が
接続形成されている。該2次燃焼室5の軸芯は上記1次
燃焼室4の軸線と同一線上にあり、その吹込口5aは炉本
体1aの開口1dを通して炉内中心に溶鋼レベル付近に向い
ている。またこの2次燃焼室5には、2次空気を吹き込
むための2つの吹込管5bが接続されており、この吹込管
5bに続く吹込ノズルは炉内に延びている。A secondary combustion chamber 5 is connected to the tip of the primary combustion chamber 4. The axis of the secondary combustion chamber 5 is on the same line as the axis of the primary combustion chamber 4, and the blow-in port 5a is directed toward the molten steel level near the center of the furnace through the opening 1d of the furnace body 1a. Further, two blow pipes 5b for blowing secondary air are connected to the secondary combustion chamber 5, and the blow pipes are connected to each other.
The blowing nozzle following 5b extends into the furnace.
次に上記実施例装置において、第1発明の一実施例方法
を実施する場合について説明する。Next, a case where the method of the first embodiment of the present invention is carried out in the apparatus of the above embodiment will be described.
一次燃焼室4内に所定量の微粉炭(350kg/H)をバーナ4
cから空気吹込管4aを介して吹き込むとともに、空気吹
込管4aから1次空気を空燃比が例えば0.65になるように
吹き込む。するとこれにより1次燃焼室4内において上
記微粉炭は内壁に沿って旋回しながら次燃焼する。この
とき、質量の重い灰分は該1次燃焼室4の内壁に付着
し、灰ポット4bよって回収される。この空燃比0.65の1
次燃焼による燃焼排気ガスは2次燃焼室5において2次
空気が混合されて完全燃焼する。この完全燃焼によって
灰分の除去された高温の排気ガスが炉内の屑鉄等に吹き
付けられ、これにより屑鉄等は予熱溶解される。Burner 4 with a specified amount of pulverized coal (350 kg / H) in the primary combustion chamber 4
The air is blown from c through the air blowing pipe 4a, and the primary air is blown from the air blowing pipe 4a so that the air-fuel ratio becomes, for example, 0.65. As a result, the pulverized coal in the primary combustion chamber 4 swirls along the inner wall and is subsequently burned. At this time, the heavy ash content adheres to the inner wall of the primary combustion chamber 4 and is collected by the ash pot 4b. This air-fuel ratio of 0.65 1
The combustion exhaust gas generated by the secondary combustion is completely combusted in the secondary combustion chamber 5 with the secondary air mixed therein. The high-temperature exhaust gas from which ash has been removed by this complete combustion is blown onto scrap iron or the like in the furnace, whereby the scrap iron or the like is preheated and melted.
このように本実施例では、固体燃料を二段燃焼させるよ
うにしたので、完全燃焼が容易であり、熱効率のよい高
温の排気ガスを屑鉄に吹き付けてこれを効率良く予熱で
き、それだけ必要電力量を削減でき、電力原単位を大幅
に低減できる。また、この場合灰分は灰ポット4bに回収
させるから、溶鋼への灰分の悪影響をなくすことができ
る。As described above, in the present embodiment, the solid fuel is burned in two stages, so that complete combustion is easy, and it is possible to efficiently preheat it by blowing high-temperature exhaust gas with good thermal efficiency onto scrap iron, and the required power amount Can be reduced and the power consumption rate can be significantly reduced. Further, in this case, since the ash content is collected in the ash pot 4b, it is possible to eliminate the adverse effect of the ash content on the molten steel.
なお、上記実施例では、2次燃焼室5における2次空気
量として、未燃ガスを完全燃焼できる量を吹き込むよう
にしたが、この場合の2次空気量を空燃比が0.35以下と
することにより、2次燃焼による排気ガスを還元性ガス
にして電気炉1内に吹き込むことができる。このように
すれば、スラグ(Fe2O3)の生成を防止でき、C+Co2
2COによる電極6の酸化を防止できる効果がある。In the above embodiment, the amount of secondary air in the secondary combustion chamber 5 is set so that the unburned gas can be completely combusted. However, in this case, the amount of secondary air should be 0.35 or less. As a result, the exhaust gas produced by the secondary combustion can be converted into a reducing gas and blown into the electric furnace 1. By doing so, the formation of slag (Fe 2 O 3 ) can be prevented, and C + Co 2
It has an effect of preventing the oxidation of the electrode 6 due to 2CO.
第2図は上記実施例の変形例を示し、これは燃焼排気ガ
スを炉底から炉内に吹き込むようにした例である。FIG. 2 shows a modified example of the above embodiment, which is an example in which combustion exhaust gas is blown into the furnace from the bottom of the furnace.
図中第1図と同一符号は同一又は相当部分を示し、1次
燃焼室4と2次燃焼室5とは排ガス通路8で接続されて
おり、また2次燃焼室5の吹込口5aは炉底に形成された
開口1eに接続されている。In the figure, the same reference numerals as those in FIG. 1 indicate the same or corresponding parts, and the primary combustion chamber 4 and the secondary combustion chamber 5 are connected by an exhaust gas passage 8, and the blowing port 5a of the secondary combustion chamber 5 is a furnace. It is connected to the opening 1e formed in the bottom.
この変形例では、電極6から離れた通電されにくい位置
にある屑鉄等に排気ガスの熱を与えることができるとと
もに、溶鋼を撹拌できることから全体をより均一に加熱
できる効果がある。In this modified example, the heat of the exhaust gas can be applied to the scrap iron or the like that is located away from the electrode 6 and is difficult to be energized, and the molten steel can be agitated, so that the whole can be heated more uniformly.
なお、上記実施例では電気炉について説明したが、本発
明の電気炉に限らず、転炉にも適用できる。In addition, although the electric furnace has been described in the above embodiments, the present invention is not limited to the electric furnace of the present invention and can be applied to a converter.
以上のように、本発明に係る電気炉,転炉の固体燃料吹
込み方法及び吹込み装置によれば、固体燃料を二段燃焼
させるようにしたので、完全燃焼が容易であり、熱効率
の良い高温の排気ガスを電気炉又は転炉に吹き込むこと
ができ、固体燃料の有する顕熱を有効に利用して屑鉄等
を高温に予熱,溶解でき、電気炉では電力原単位を大幅
に低減できる効果があり、転炉では低コストの熱補償が
可能になる効果がある。As described above, according to the electric furnace, the method for injecting the solid fuel in the converter, and the injecting apparatus according to the present invention, since the solid fuel is burned in two stages, complete combustion is easy and thermal efficiency is good. High-temperature exhaust gas can be blown into the electric furnace or converter, and the sensible heat of solid fuel can be effectively used to preheat and melt scrap iron to a high temperature. Therefore, the converter has the effect of enabling low-cost thermal compensation.
第1図は本願の第2発明の一実施例による電気炉の固体
燃料吹込み装置を説明するための図であり、第1図
(a)はその断面側面図、第1図(b)はその1次燃焼
室の横断面図、第2図は上記実施例の変形例を示す断面
側面図、第3図は従来の電気炉の断面側面図、第4図
(a)はそのバーナの横断面図、第4図(b)はそのバ
ーナの縦断面図である。 図において、1は電気炉、4は1次燃焼室、5は2次燃
焼室である。FIG. 1 is a view for explaining a solid fuel injection device for an electric furnace according to an embodiment of the second invention of the present application, FIG. 1 (a) is a sectional side view thereof, and FIG. 1 (b) is A transverse sectional view of the primary combustion chamber, FIG. 2 is a sectional side view showing a modified example of the above embodiment, FIG. 3 is a sectional side view of a conventional electric furnace, and FIG. 4 (a) is a cross section of the burner. A plan view and FIG. 4 (b) are longitudinal sectional views of the burner. In the figure, 1 is an electric furnace, 4 is a primary combustion chamber, and 5 is a secondary combustion chamber.
Claims (6)
電気炉又は転炉において、上記原材料を固定燃料の吹込
みによって予熱,溶解する方法であって、固体燃料を炉
外で空燃比1.0以下で1次燃焼させ、炉入口付近におい
て、該未燃焼ガスに空気又は酸素を供給して2次燃焼さ
せ、該二段燃焼による排気ガスを上記原材料に吹き付け
るようにしたことを特徴とする電気炉,転炉の固体燃料
吹込み方法。1. A method for preheating and melting the raw material by blowing fixed fuel in an electric furnace or a converter for melting raw material such as scrap iron to produce molten steel, wherein the solid fuel is air-fuel ratio outside the furnace. It is characterized in that primary combustion is carried out at 1.0 or less, air or oxygen is supplied to the unburned gas in the vicinity of the furnace inlet to carry out secondary combustion, and exhaust gas by the second-stage combustion is blown to the raw materials. Solid fuel injection method for electric furnaces and converters.
原材料の上面から吹き込むことを特徴とする特許請求の
範囲第1項記載の電気炉,転炉の固体燃料吹込み方法。2. A solid fuel blowing method for an electric furnace or a converter according to claim 1, wherein the combustion exhaust gas is blown from an upper surface of a raw material in the electric furnace or the converter.
から吹き込むことを特徴とする特許請求の範囲第1項記
載の電気炉,転炉の固体燃料吹込み方法。3. The method for injecting solid fuel in an electric furnace or converter according to claim 1, wherein the combustion exhaust gas is blown from the bottom of the electric furnace or converter.
電気炉,又は転炉において、上記原材料を固定燃料の吹
込みによって予熱,溶解する装置であって、電気炉,又
は転炉の炉外に、固体燃料及び1次燃焼用空気が吹き込
まれ、固体燃料を空燃比1.0以下で1次燃焼させる1次
燃焼室を形成し、電気炉又は転炉の入口に、上記1次燃
焼室からの未燃焼ガスに2次燃焼用空気を供給して2次
燃焼させるとともに、該二段燃焼による排気ガスを電気
炉,又は転炉内に導入する2次燃焼室を形成したことを
特徴とする電気炉,転炉の固体燃料吹込み装置。4. An electric furnace or a converter for melting raw materials such as scrap iron to produce molten steel, which is an apparatus for preheating and melting the raw materials by blowing fixed fuel into the electric furnace or the converter. Solid fuel and primary combustion air are blown outside the furnace to form a primary combustion chamber for primary combustion of the solid fuel at an air-fuel ratio of 1.0 or less, and the primary combustion chamber is provided at the inlet of the electric furnace or converter. Secondary combustion air is supplied to the unburned gas from the secondary combustion chamber to perform secondary combustion, and a secondary combustion chamber for introducing the exhaust gas from the second stage combustion into the electric furnace or the converter is formed. Solid fuel injection device for electric furnaces and converters.
転炉内の原材料の上面に臨んでいることを特徴とする特
許請求の範囲第4項記載の電気炉,転炉の固体燃料吹込
み装置。5. The electric furnace according to claim 4, wherein the outlet of the secondary combustion chamber faces the upper surface of the raw material in the electric furnace or the converter, and the solid material of the converter. Fuel injection device.
は転炉の炉底内に臨んでいることを特徴とする特許請求
の範囲第4項記載の電気炉,転炉の固体燃料吹込み装
置。6. The solid of the electric furnace or the converter according to claim 4, wherein the outlet of the secondary combustion chamber faces the bottom of the electric furnace or the converter. Fuel injection device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11148986A JPH07107174B2 (en) | 1986-05-15 | 1986-05-15 | Solid fuel injection method and injection device for electric furnace and converter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11148986A JPH07107174B2 (en) | 1986-05-15 | 1986-05-15 | Solid fuel injection method and injection device for electric furnace and converter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62267407A JPS62267407A (en) | 1987-11-20 |
| JPH07107174B2 true JPH07107174B2 (en) | 1995-11-15 |
Family
ID=14562563
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11148986A Expired - Lifetime JPH07107174B2 (en) | 1986-05-15 | 1986-05-15 | Solid fuel injection method and injection device for electric furnace and converter |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07107174B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100380135B1 (en) * | 1998-12-16 | 2003-08-21 | 주식회사 포스코 | Refractory Thermal Burner |
-
1986
- 1986-05-15 JP JP11148986A patent/JPH07107174B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62267407A (en) | 1987-11-20 |
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