JP5194504B2 - Apparatus for injecting gas reducing material into blast furnace and operating method of blast furnace using the same - Google Patents

Apparatus for injecting gas reducing material into blast furnace and operating method of blast furnace using the same Download PDF

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JP5194504B2
JP5194504B2 JP2007074652A JP2007074652A JP5194504B2 JP 5194504 B2 JP5194504 B2 JP 5194504B2 JP 2007074652 A JP2007074652 A JP 2007074652A JP 2007074652 A JP2007074652 A JP 2007074652A JP 5194504 B2 JP5194504 B2 JP 5194504B2
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reducing material
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gas reducing
blast furnace
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JP2008231529A (en
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博 竹生
秀明 築地
富 山口
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JFE Steel Corp
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本発明は、高炉への気体還元材吹込装置に関し、特に、固体還元材(微粉炭・使用済みプラスチック等)と気体還元材(都市ガス等)の双方を高炉羽口より炉内に吹込む際に使用する高炉への気体還元材吹込装置及びこれを用いた高炉の操業方法に関するものである。   The present invention relates to a device for blowing a gas reducing material into a blast furnace, and in particular, when both a solid reducing material (pulverized coal, used plastic, etc.) and a gas reducing material (city gas, etc.) are blown into the furnace from a blast furnace tuyere. The present invention relates to an apparatus for injecting a gas reducing material into a blast furnace used for the blast furnace and a method for operating the blast furnace using the apparatus.

高炉において、高出銑比、低還元材操業を達成する手段として、天然ガスや都市ガス等の気体還元材(還元性ガス)の羽口からの吹き込みが行われている。しかし、例えば、5000m3クラス、羽口の送風圧力400Kpa以上、羽口の数40個前後の大型高炉で、この気体還元材の吹込みを行なう場合、熱風を熱風本管から高炉を取り巻く熱風環状管に送り、そこからさらに各羽口に設けられた送風ノズルに供給する熱風吹込装置を用いると、大型高炉は羽口の数も多いため、個々の羽口の吹込ガス量を均一になるように調整することが難しく、さらに、逆火を防止するためにある程度の吹込速度を確保しなければならないが、高炉が大きくなると炉内圧が大きくなるので、特に、吹込ガス量が少なくなった場合にこの吹込速度を確保することが困難となり、気体還元材の吹込みが容易でないと言う問題があった。このような問題を解決する装置として、高炉の炉体の外周に配設された複数のリング状還元性ガス供給管と、炉体の外壁に周状に配置された複数の羽口と、各リング状還元性ガス供給管から複数の羽口に接続する還元性ガス吹込管よりなる、高炉への還元性ガス吹込装置が知られている(例えば、特許文献1参照。)。各羽口への還元性ガス(気体還元材)の吹込量制御は、羽口ごとに個別に流量制御装置を設置すると、設備費が高く制御上も複雑なので、各リング管の元配管に設置された流調弁で一括実施している。
特開2006−206994号公報
In a blast furnace, as a means for achieving a high output ratio and a low reducing material operation, a gas reducing material (reducing gas) such as natural gas or city gas is blown from the tuyere. However, for example, when blowing this gas reducing material in a large blast furnace of 5000 m 3 class, a tuyere blowing pressure of 400 Kpa or more, and around 40 tuyere, hot air is blown around the blast furnace from the hot air main. When using a hot air blowing device that is sent to a pipe and then supplied to a blowing nozzle provided at each tuyere, the large blast furnace has a large number of tuyere, so that the amount of gas blown into each tuyere is uniform. In order to prevent backfire, it is necessary to secure a certain blowing speed.However, as the blast furnace becomes larger, the pressure inside the furnace becomes larger, especially when the amount of blown gas decreases. It was difficult to ensure the blowing speed, and there was a problem that the blowing of the gas reducing material was not easy. As an apparatus for solving such a problem, a plurality of ring-shaped reducing gas supply pipes arranged on the outer periphery of the furnace body of the blast furnace, a plurality of tuyere arranged circumferentially on the outer wall of the furnace body, 2. Description of the Related Art A reducing gas blowing device for a blast furnace is known that includes a reducing gas blowing tube connected to a plurality of tuyere from a ring-shaped reducing gas supply tube (see, for example, Patent Document 1). Control of the amount of reducing gas (gas reductant) injected into each tuyere is installed in the original pipe of each ring pipe because the equipment cost is high and the control is complicated if a flow control device is individually installed for each tuyere. It is carried out at once with the flow control valve.
JP 2006-206994 A

特許文献1に記載の高炉への還元性ガス吹込装置を用いることで、大型高炉であっても、気体還元材を容易に円周バランスよく安定して吹込むことができ、吹込量を調節することもできる。   By using the reducing gas blowing device to the blast furnace described in Patent Document 1, even in a large blast furnace, the gas reducing material can be easily and stably blown in a balanced manner, and the amount of blowing is adjusted. You can also.

一方で、通常の高炉操業においては微粉炭等の羽口吹込みが行なわれている。羽口から固体還元材(微粉炭・使用済みプラスチック等)と気体還元材の両方を吹き込む操業を行なう場合、通常は固体還元材吹込み用と、気体還元材吹込み用のランスを1本ずつ各羽口に設置するが、固体還元材吹込み用のランスは、粉体の吹込みであるため、ランス先端の閉塞等により、吹込みを停止しなければならなくなる場合がある。   On the other hand, in normal blast furnace operation, tuyeres such as pulverized coal are injected. When performing operations in which both solid reducing material (pulverized coal, used plastic, etc.) and gas reducing material are blown from the tuyere, usually one lance for blowing solid reducing material and one for gas reducing material. Although it is installed at each tuyere, the lance for blowing the solid reducing material is powder blowing, and therefore it may be necessary to stop the blowing due to blockage of the tip of the lance or the like.

微粉炭が吹込み不可能になった羽口では、羽口先端の理論燃焼温度が他の羽口より200〜300℃上昇し、高炉炉内コークスの熱衝撃による劣化を助長し、高炉炉況悪化を招く。   At tuyere where pulverized coal can no longer be blown, the theoretical combustion temperature at the tuyere's tip increases by 200-300 ° C over other tuyere and promotes the deterioration of coke in the blast furnace due to thermal shock. Deteriorating.

炉況悪化を回避するためには、微粉炭の吹込みが不可能になった羽口のランス取替作業を行なうことになるが、これは休風作業となり、実施する場合は大減産(2000〜3000t)となる。   In order to avoid the deterioration of the furnace condition, the lance replacement work for the tuyere where pulverized coal can no longer be blown is performed. ~ 3000t).

したがって本発明の目的は、このような従来技術の課題を解決し、羽口から固体還元材と気体還元材の両方を吹き込む高炉操業を行なう際に、固体還元材の吹込みランスの吹き込みを停止した際にも、高炉炉況を悪化させることなく、高炉の操業を継続可能とする高炉への気体還元材吹込み装置及びこれを用いた高炉の操業方法を、低コストで提供することにある。   Therefore, the object of the present invention is to solve such a problem of the prior art and stop the blowing of the blowing lance of the solid reducing material when performing the blast furnace operation in which both the solid reducing material and the gaseous reducing material are blown from the tuyere. In this case, it is to provide a gas reducing material injection device to the blast furnace that can continue the operation of the blast furnace without deteriorating the blast furnace condition, and a blast furnace operating method using the same. .

このような課題を解決するための本発明の特徴は以下の通りである。
(1)、固体還元材と気体還元材とを羽口より炉内に吹込む操業を行なう高炉に設置して使用する気体還元材吹込み装置であって、高炉の炉体の外周に配設された複数のリング状気体還元材供給管と、該リング状気体還元材供給管と前記羽口に設置した気体還元材吹き込み用ランスとを接続する気体還元材吹込み管と、前記リング状気体還元材供給管に気体還元材を供給する気体還元材供給本管と、該気体還元材供給本管から分岐して前記各リング状気体還元材供給管に気体還元材を供給する気体還元材供給管とを有し、さらに、高炉の炉体の外周に配設された固体還元材吹き込み停止時専用リング状気体還元材供給管と、該固体還元材吹き込み停止時専用リング状気体還元材供給管と前記気体還元材吹き込み用ランスとを接続する固体還元材吹き込み停止時専用気体還元材吹込み管と、前記固体還元材吹き込み停止時専用リング状気体還元材供給管に気体還元材を供給する固体還元材吹き込み停止時専用気体還元材供給管よりなる、高炉への気体還元材吹込装置。
(2)、(1)に記載の装置を用い、固体還元材と気体還元材とを羽口より炉内に吹込む操業を行なう高炉において、当該羽口から固体還元材の吹き込みを停止した際に、当該羽口の気体還元材吹き込み用ランスへのリング状気体還元材供給管からの気体還元材の供給を停止し、固体還元材吹き込み停止時専用リング状気体還元材供給管から前記気体還元材吹き込み用ランスに気体還元材を供給する高炉の操業方法。
(3)、固体還元材の吹き込み停止前にリング状気体還元材供給管から供給していた気体還元材の流量よりも、固体還元材吹き込み停止時専用リング状気体還元材供給管から気体還元材吹き込み用ランスに供給する気体還元材の流量を増加させる、(2)に記載の高炉の操業方法。
The features of the present invention for solving such problems are as follows.
(1) A gas reducing material blowing device that is installed and used in a blast furnace in which a solid reducing material and a gas reducing material are blown into a furnace from a tuyere, and is disposed on the outer periphery of the furnace body of the blast furnace A plurality of ring-shaped gas reducing material supply pipes, a gas reducing material blowing pipe connecting the ring-shaped gas reducing material supply pipe and a gas reducing material blowing lance installed in the tuyere, and the ring-shaped gas A gas reducing material supply main for supplying the gas reducing material to the reducing material supply pipe, and a gas reducing material supply for supplying the gas reducing material to each of the ring-shaped gas reducing material supply pipes by branching from the gas reducing material supply main A ring-shaped gas reducing material supply pipe dedicated to when the solid reducing material blowing is stopped, and a ring-shaped gas reducing material supply pipe dedicated to when the solid reducing material blowing is stopped. And solid reduction connecting the gas reducing material blowing lance A blast furnace consisting of a dedicated gas reducing material blowing pipe when the blowing is stopped and a dedicated reducing gas supply pipe when the solid reducing material blowing is stopped for supplying the gaseous reducing material to the ring-shaped gas reducing material supply pipe when the solid reducing material is stopped. Gas reducing material blowing device.
(2) When using the apparatus described in (1) and stopping the blowing of the solid reducing material from the tuyere in the blast furnace in which the solid reducing material and the gaseous reducing material are blown into the furnace from the tuyere In addition, the supply of the gas reducing material from the ring-shaped gas reducing material supply pipe to the lance for blowing the gas reducing material at the tuyere is stopped, and the gas reduction is performed from the dedicated ring-shaped gas reducing material supply pipe when the solid reducing material blowing is stopped. Blast furnace operation method for supplying gas reducing material to lance for blowing material.
(3) From the flow rate of the gas reducing material supplied from the ring-shaped gas reducing material supply pipe before stopping the blowing of the solid reducing material, the gas reducing material is supplied from the ring-shaped gas reducing material supply pipe at the time of stopping the solid reducing material blowing. The blast furnace operating method according to (2), wherein the flow rate of the gas reducing material supplied to the blowing lance is increased.

本発明によれば、固体還元材が吹込み不可能になった羽口に対して、個別に気体還元材の流量を制御して吹込むことが可能となり、これにより羽口先端の理論燃焼温度を一定に保つことができるので、高炉炉況悪化を防止できる。また、固体還元材吹き込み用のランスが閉塞するたびに、ランス取替作業のために高炉の操業を停止する必要がないので、高炉の生産性が増加する。   According to the present invention, it becomes possible to individually control the flow rate of the gas reducing material to the tuyere where the solid reducing material cannot be blown, and thereby the theoretical combustion temperature at the tip of the tuyere Can be kept constant, so that blast furnace conditions can be prevented from deteriorating. Further, every time the lance for injecting the solid reducing material is closed, it is not necessary to stop the operation of the blast furnace for the lance replacement work, so that the productivity of the blast furnace is increased.

本発明者らは、羽口から固体還元材と気体還元材の両方を吹き込む高炉操業を行なう際に、ある羽口において固体還元材の吹込みを停止する場合、その羽口の先端での理論燃焼温度を他の羽口と同レベルにするためには、気体還元材の流量を増加させることで対処可能であると考えた。この場合気体還元材の流量は、通常の約2倍程度必要となる。   When performing the blast furnace operation in which both the solid reducing material and the gas reducing material are blown from the tuyere, the present inventors, when stopping the blowing of the solid reducing material at a certain tuyere, the theory at the tip of the tuyere In order to make the combustion temperature the same level as other tuyere, we thought that it was possible to cope by increasing the flow rate of the gas reducing material. In this case, the flow rate of the gas reducing material is required to be about twice the normal flow rate.

尚、固体還元材の吹き込みを停止する場合とは、固体還元材吹き込み用ランスが閉塞した場合や、閉塞には至らないまでもランス先端の異常等により所定量の固体還元材を吹き込むことができなくなった場合、配管の設備トラブルで固体還元材を吹き込むことができなくなった場合等が挙げられる。   Note that when the blowing of the solid reducing material is stopped, a predetermined amount of the solid reducing material can be blown when the lance for blowing the solid reducing material is blocked or when the lance tip is not closed. When it disappears, the case where it becomes impossible to blow a solid reducing material by the equipment trouble of piping, etc. are mentioned.

以降は、固体還元材吹き込み停止の典型的な例として、固体還元材吹き込み用ランスが閉塞した場合を一実施態様として説明する。   Hereinafter, as a typical example of the solid reducing material blowing stop, a case where the solid reducing material blowing lance is blocked will be described as one embodiment.

図2、3に、従来技術である特許文献1に記載の還元性ガス(気体還元材)吹込み装置を示す。図2が還元性ガス吹込み装置、図3は図2の装置を高炉に取り付けた状態である。図2、3において、還元性ガスは4つのリング管から吹込み管を通じて高炉内に吹込まれる。還元性ガスの吹込量制御は、各リング管の元配管に設置された流調弁で一括実施している。例えば、羽口38本の高炉においては、流調弁1台で、9〜10羽口分の流量を一括調整するものである。したがって、図2、3に記載の装置を用いる場合、固体還元材が吹込み不可能になった羽口のガス流量のみを増加させることは不可能である。尚、固体還元材は気体還元材とは別の経路で、羽口に設置した固体還元材吹込み用ランスから搬送ガスとともに高炉内に吹込まれる。   2 and 3 show a reducing gas (gas reducing material) blowing device described in Patent Document 1 which is a conventional technique. FIG. 2 shows a reducing gas blowing device, and FIG. 3 shows a state where the device of FIG. 2 is attached to a blast furnace. 2 and 3, the reducing gas is blown into the blast furnace from the four ring pipes through the blow pipes. Control of the amount of reducing gas injected is carried out in a lump using flow control valves installed in the original pipe of each ring pipe. For example, in a blast furnace with 38 tuyere, the flow rate of 9 to 10 tuyere is collectively adjusted with one flow control valve. Therefore, when the apparatus shown in FIGS. 2 and 3 is used, it is impossible to increase only the gas flow rate at the tuyere where the solid reducing material cannot be blown. The solid reducing material is blown into the blast furnace together with the carrier gas from a solid reducing material blowing lance installed in the tuyere through a different path from the gas reducing material.

気体還元材のガス流量を羽口毎に調整可能とするためには、各羽口毎に単独の配管を設置して、羽口数と同一数の流調弁と流量計を設置することで対処可能であるが、設備費が高額になり、制御的にも複雑になる。吹込み管に流調弁と流量計を設置する手段もあるが、現実の設備では配置上、設置不可能な場合もあり、また、高温・ダスト・ガス雰囲気の羽口周辺に流調弁や流量計を設置することになるため、設備費だけでなく、耐久性の面でも問題がある。   In order to make it possible to adjust the gas flow rate of the gas reducing material for each tuyere, a single pipe is installed for each tuyere and the same number of flow control valves and flow meters as the number of tuyere are installed. Although it is possible, the equipment cost becomes high and the control becomes complicated. There is a means to install a flow control valve and a flow meter in the blowing pipe, but there are cases where it cannot be installed due to the arrangement in the actual equipment, and there is a flow control valve around the tuyere of high temperature, dust and gas atmosphere. Since a flow meter will be installed, there is a problem not only in equipment cost but also in durability.

そこで、本発明者らは、固体還元材が吹込み不可能になり気体還元材を通常の2倍程度吹込みたい羽口用の、固体還元材吹き込み停止時専用リング状気体還元材供給管及び流量計、流調弁からなる固体還元材吹き込み停止時専用ラインを設置することで、個別の羽口のガス流量の調整が可能な設備とすることができることを見出し、本発明を完成した。この固体還元材吹き込み停止時専用ライン使用時は、羽口廻りに設置された弁で通常使用している吹込み管を閉止し、固体還元材吹き込み停止時専用ライン側からのみ気体還元材を供給する。固体還元材の吹込み不可能となった羽口への気体還元材供給量は、通常の約2倍であり、羽口間で異なるものではないので、微粉炭吹込み不可能な羽口が数本ある場合にも対応して、同時に気体還元材を供給可能である。   Therefore, the present inventors have provided a ring-shaped gas reducing material supply pipe and a flow rate dedicated to a tuyere for when the solid reducing material cannot be blown and the gas reducing material is blown about twice as much as usual. The present invention has been completed by finding that an installation capable of adjusting the gas flow rate of the individual tuyere can be made by installing a dedicated line for stopping the blowing of the solid reducing material consisting of a flow control valve. When using the dedicated line at the time of stopping the solid reducing material blowing, close the blowing pipe normally used by the valve installed around the tuyere and supply the gaseous reducing material only from the dedicated line side when stopping the solid reducing material blowing To do. The amount of gas reductant supplied to the tuyere where the solid reductant can no longer be blown is about twice that of a normal tuyere and does not differ between tuyere. Corresponding to the case where there are several, the gas reducing material can be supplied simultaneously.

尚、本発明で用いる気体還元材とは、還元性ガスであり、メタン、プロパン、都市ガス、天然ガス、また、高炉、コークス、転炉等から発生する製鉄所内副製ガス等のガスである。また、本発明で用いる固体還元材とは、上記のように、微粉炭、廃プラスチック等の固体炭素含有物質である。   The gas reducing material used in the present invention is a reducing gas, such as methane, propane, city gas, natural gas, and gas such as by-product gas in a steelworks generated from a blast furnace, coke, converter, etc. . Moreover, the solid reducing material used in the present invention is a solid carbon-containing substance such as pulverized coal or waste plastic as described above.

図1を用いて、本発明を詳しく説明する。図1は本発明の高炉への気体還元材吹込み装置の一実施形態の概略図であり、図3と同様に高炉に設置して使用する。気体還元材吹込み装置1は、複数(本実施形態においては4本)のリング状気体還元材供給管2a〜2dと、リング状気体還元材供給管2から羽口に設置した気体還元材吹き込み用ランス3に接続する気体還元材吹込み管4と、リング状気体還元材供給管2に気体還元材を供給する気体還元材供給本管5aと、気体還元材供給本管5aから分岐して各リング状気体還元材供給管2にガスを供給する気体還元材供給管5b〜5eと、さらに、固体還元材吹き込み停止時専用リング状気体還元材供給管6と、固体還元材吹き込み停止時専用リング状気体還元材供給管6から気体還元材吹き込み用ランス3に接続する固体還元材吹き込み停止時専用気体還元材吹込み管7と、固体還元材吹き込み停止時専用リング状気体還元材供給管6に気体還元材を供給する固体還元材吹き込み停止時専用気体還元材供給管8とからなり、気体還元材供給本管5aと、固体還元材吹き込み停止時専用気体還元材供給管8とは、それぞれ流量計9、流調弁10とを有している。11は弁、12は逆止弁、13はフレキシブルホースである。図1において、気体還元材吹き込み用ランス3は1本のみを示したが、実際には羽口の数のランスがあり、それぞれについて、リング状気体還元材供給管2a〜2dのいずれかに気体還元材吹込み管4を介して、および、固体還元材吹き込み停止時専用リング状気体還元材供給管6に固体還元材吹き込み停止時専用気体還元材吹込み管7を介して、接続されている。気体還元材吹き込み用ランス3を設置する羽口は、各リング状気体還元材供給管2a〜2dに対して均等な数で、ほぼ等間隔になるように配置する。   The present invention will be described in detail with reference to FIG. FIG. 1 is a schematic view of an embodiment of the apparatus for injecting a gas reducing material into a blast furnace according to the present invention. The gas reducing material blowing device 1 includes a plurality of (in the present embodiment, four) ring-shaped gas reducing material supply pipes 2a to 2d and a gas reducing material blowing apparatus installed in the tuyere from the ring-shaped gas reducing material supply pipe 2. Branching from the gas reducing material blowing pipe 4 connected to the lance 3, the gas reducing material supply main pipe 5a for supplying the gas reducing material to the ring-shaped gas reducing material supply pipe 2, and the gas reducing material supply main pipe 5a. Gas reducing material supply pipes 5b to 5e for supplying gas to each ring-shaped gas reducing material supply pipe 2, and further, a ring-shaped gas reducing material supply pipe 6 dedicated to when the solid reducing material blowing is stopped and a solid reducing material blowing dedicated to stopping. A solid reducing material blowing pipe 7 that is connected to the lance 3 for blowing the gas reducing material from the ring-shaped gas reducing material supply pipe 6 and a dedicated ring-shaped gas reducing material supply pipe 6 that is used when the solid reducing material blowing is stopped. Gas reducing material The gas reducing material supply pipe 8 includes a gas reducing material supply main pipe 5a and a gas reducing material supply pipe 8 used when the solid reducing material blowing is stopped. And the valve 10. 11 is a valve, 12 is a check valve, and 13 is a flexible hose. In FIG. 1, only one gas reducing material blowing lance 3 is shown, but there are actually lances of the number of tuyere, and each of them has gas in any of the ring-shaped gas reducing material supply pipes 2 a to 2 d. It is connected via the reducing material blowing pipe 4 and to the ring-shaped gas reducing material supply pipe 6 dedicated to when the solid reducing material blowing is stopped via the dedicated gas reducing material blowing pipe 7 when the solid reducing material blowing is stopped. . The tuyere on which the lance 3 for blowing the gas reducing material is installed is arranged in an equal number with respect to each of the ring-shaped gas reducing material supply pipes 2a to 2d so as to be substantially equally spaced.

複数のリング状気体還元材供給管と固体還元材吹き込み停止時専用リング状気体還元材供給管は、高炉の炉体の外周に配設する。図1においては、固体還元材吹き込み停止時専用リング状気体還元材供給管6の径がリング状気体還元材供給管2a〜2dより大きく示されているが、全て同じ径として、図2、3に示すように高炉の異なる高さ位置に配設することができる。   A plurality of ring-shaped gas reducing material supply pipes and a ring-shaped gas reducing material supply pipe dedicated to stopping the solid reducing material blowing are arranged on the outer periphery of the furnace body of the blast furnace. In FIG. 1, the diameter of the dedicated ring-shaped gas reducing material supply pipe 6 when the solid reducing material blowing is stopped is shown to be larger than the diameter of the ring-shaped gas reducing material supply pipes 2 a to 2 d. Can be arranged at different height positions in the blast furnace.

図1の装置を用いて、高炉炉体の外壁に周状に38の羽口が配置され、各羽口には固体還元材として微粉炭吹き込み用と、気体還元材として都市ガス吹込み用のランスが1本ずつ設置されており、微粉炭比(PCR)80kg/溶銑t、都市ガス(LNG)比30kg/溶銑t程度の吹込みを実施している際に、固体還元材の吹込み用ランスが閉塞した場合の操業方法を説明する。   Using the apparatus of FIG. 1, 38 tuyere are arranged on the outer wall of the blast furnace body, and each tuyere is used for blowing pulverized coal as a solid reducing material and for blowing city gas as a gas reducing material. One lance is installed at each time, and it is used to inject solid reductant when pulverized coal ratio (PCR) 80kg / molten metal t and city gas (LNG) ratio 30kg / molten metal t The operation method when the lance is blocked will be described.

固体還元材の吹込み用ランスが閉塞した羽口の先端での理論燃焼温度を他の羽口と同レベルにするために、気体還元材の流量を通常の約2倍程度とする。まず手動ボール弁11aを閉じ、通常ラインからの都市ガスの吹込みを中止する。同時に手動ボール弁11bを開き、固体還元材吹き込み停止時専用気体還元材供給管8、固体還元材吹き込み停止時専用リング状気体還元材供給管6、固体還元材吹き込み停止時専用気体還元材吹込み管7を介して都市ガスを気体還元材吹き込み用ランス3に供給する。この際に、流調弁10を調整して、都市ガス比(LNG)60kg/溶銑t程度の吹込みを行なう。これによりランスが閉塞した羽口先温度の上昇は防止され、安定操業を継続できる。   In order to make the theoretical combustion temperature at the tip of the tuyere where the lance for blowing the solid reducing material closes the same level as the other tuyere, the flow rate of the gas reducing material is set to about twice the normal flow rate. First, the manual ball valve 11a is closed, and the blowing of city gas from the normal line is stopped. At the same time, the manual ball valve 11b is opened, the dedicated gas reducing material supply pipe 8 when the solid reducing material blowing is stopped, the dedicated ring-shaped gas reducing material supply pipe 6 when the solid reducing material blowing is stopped, and the dedicated gas reducing material blowing when the solid reducing material blowing is stopped. The city gas is supplied to the gas reducing material blowing lance 3 through the pipe 7. At this time, the flow control valve 10 is adjusted to perform blowing at a city gas ratio (LNG) of about 60 kg / molten metal t. This prevents the tuyere tip temperature from increasing when the lance is blocked, and stable operation can be continued.

固体還元材の吹込み用ランスが閉塞した羽口が複数発生している場合にも本発明の設備で対応できるが、ランスの閉塞が4ヶ所を超えた場合には、高炉の操業を停止して、ランスの交換作業を行なうことが望ましい。ランスの閉塞が4ヶ所以内であれば、固体還元材吹き込み停止時専用リング状気体還元材供給管から固体還元材吹き込み停止時専用気体還元材吹込み管への吹込み量が各羽口間で変動することも少なく、バランスの良い吹込みを実施できる。   The facility of the present invention can cope with the occurrence of a plurality of tuyere with a solid reducing material blowing lance blocked. However, when the lance is blocked in more than four places, the operation of the blast furnace is stopped. It is desirable to replace the lance. If the lance blockage is within 4 locations, the amount of air blown from the dedicated ring-shaped gas reducing material supply pipe when the solid reducing material blowing is stopped to the dedicated gas reducing material blowing pipe when the solid reducing material blowing is stopped is between each tuyere. There is little fluctuation, and well-balanced blowing can be performed.

体積約5000m3、羽口の数38個の大型高炉において、羽口から微粉炭(PC)と都市ガス(LNG)を吹込む操業を行なった。都市ガス成分は、CH4:88.0%、C2H6:5.8%、C3H8:4.5%、C4H8:1.7%であり、ガス比重は0.837kg/Nm3であった。 In a large blast furnace with a volume of about 5000 m 3 and a number of tuyere of 38, operation was performed in which pulverized coal (PC) and city gas (LNG) were blown from the tuyere. The city gas components were CH 4 : 88.0%, C 2 H 6 : 5.8%, C 3 H 8 : 4.5%, C 4 H 8 : 1.7%, and the gas specific gravity was 0.837 kg / Nm 3 .

ベースの操業条件は、羽口1個当たりで、送風量:7600Nm3/min、酸素流量:44000Nm3/H、微粉炭比:80kg/溶銑t、LNG比:30kg/溶銑t、であった。LNG吹き込み用ランスからの吹き込みガスの流量は500Nm3/H、流速は97.2m/sであった。 The operating conditions of the base were as follows: air volume: 7600 Nm 3 / min, oxygen flow rate: 44000 Nm 3 / H, pulverized coal ratio: 80 kg / molten iron t, LNG ratio: 30 kg / molten iron t per tuyere. The flow rate of the blown gas from the LNG blowing lance was 500 Nm 3 / H, and the flow rate was 97.2 m / s.

操業中に微粉炭吹込み用ランスの一本に詰まりが発生した。この場合の操業条件は、送風量:7600Nm3/min、酸素流量:44000Nm3/H、微粉炭比:0kg/溶銑t、LNG比:30kg/溶銑t、であった。ランスが詰まった羽口の羽口先端理論燃焼温度がベースの操業条件での2300℃程度に対して、約200℃上昇し、高炉炉内コークスの熱衝撃による劣化を助長し、高炉炉況悪化を招くので、ランス取替のために臨時休風を行った。これにより2000t程度減産する結果となった。 During operation, one of the lances for injecting pulverized coal became clogged. The operating conditions in this case were: blast volume: 7600 Nm 3 / min, oxygen flow rate: 44000 Nm 3 / H, pulverized coal ratio: 0 kg / molten metal t, LNG ratio: 30 kg / molten metal t. The theoretical combustion temperature at the tuyere tip of the tuyere clogged with lances increased by about 200 ° C compared to about 2300 ° C under the base operating conditions, which promoted deterioration of coke in the blast furnace due to thermal shock and deteriorated blast furnace conditions As a result, a temporary breeze was performed to replace the lance. This resulted in a reduction of about 2000 tons.

次に、操業中に微粉炭吹込み用ランスの一本に詰まりが発生した時に、本発明の気体還元材吹込み装置を用いてLNGの吹込み量を2倍にした。操業条件は、送風量:7600Nm3/min、酸素流量:44000Nm3/H、微粉炭比:0kg/溶銑t、LNG比:60kg/溶銑t、であり、LNG吹き込み用ランスからの吹き込みガスの流量は1000Nm3/H、流速は194.3m/sであった。微粉炭詰り羽口の羽口先端理論燃焼温度がベースの2300℃を一定に保つことで、高炉炉況悪化が回避された。ランス取替のための臨時休風は不要であった。 Next, when clogging occurred in one of the pulverized coal blowing lances during operation, the amount of LNG blown was doubled using the gas reducing material blowing device of the present invention. The operating conditions are blast volume: 7600 Nm 3 / min, oxygen flow rate: 44000 Nm 3 / H, pulverized coal ratio: 0 kg / molten metal t, LNG ratio: 60 kg / molten metal t, flow rate of blown gas from LNG blowing lance Was 1000 Nm 3 / H, and the flow rate was 194.3 m / s. The theoretical combustion temperature at the tuyere tip of the pulverized coal clogged tuyere was kept constant at 2300 ° C, thereby preventing the blast furnace from deteriorating. There was no need for a temporary wind break to replace the lance.

本発明の高炉への気体還元材吹込み装置の一実施形態の概略図。The schematic of one Embodiment of the gas reducing material injection apparatus to the blast furnace of this invention. 還元性ガス吹込み装置の概略図(従来技術)。Schematic of reducing gas blowing device (prior art). 図2の装置を高炉に取り付けた状態の概略図(従来技術)。FIG. 3 is a schematic view of a state in which the apparatus of FIG. 2 is attached to a blast furnace (prior art).

符号の説明Explanation of symbols

1 気体還元材吹込み装置
2(2a〜2d) リング状気体還元材供給管
3 気体還元材吹き込み用ランス
4 気体還元材吹込み管
5a 気体還元材供給本管
5b〜5e 気体還元材供給管
6 固体還元材吹き込み停止時専用リング状気体還元材供給管
7 固体還元材吹き込み停止時専用気体還元材吹込み管
8 固体還元材吹き込み停止時専用気体還元材供給管
9 流量計
10 流調弁
11 弁
12 逆止弁
13 フレキシブルホース
DESCRIPTION OF SYMBOLS 1 Gas reducing material blowing apparatus 2 (2a-2d) Ring-shaped gas reducing material supply pipe 3 Gas reducing material blowing lance 4 Gas reducing material blowing pipe 5a Gas reducing material supply main pipe 5b-5e Gas reducing material supply pipe 6 Dedicated ring-shaped gas reducing material supply pipe when solid reducing material blowing is stopped 7 Dedicated gas reducing material blowing pipe when solid reducing material blowing is stopped 8 Dedicated gas reducing material supply pipe when solid reducing material blowing is stopped 9 Flowmeter 10 Flow control valve 11 Valve 12 Check valve 13 Flexible hose

Claims (3)

固体還元材と気体還元材とを羽口より炉内に吹込む操業を行なう高炉に設置して使用する気体還元材吹込み装置であって、高炉の炉体の外周に配設された複数のリング状気体還元材供給管と、該リング状気体還元材供給管と前記羽口に設置した気体還元材吹き込み用ランスとを接続する気体還元材吹込み管と、前記リング状気体還元材供給管に気体還元材を供給する気体還元材供給本管と、該気体還元材供給本管から分岐して前記各リング状気体還元材供給管に気体還元材を供給する気体還元材供給管とを有し、さらに、高炉の炉体の外周に配設された固体還元材吹き込み停止時専用リング状気体還元材供給管と、該固体還元材吹き込み停止時専用リング状気体還元材供給管と前記気体還元材吹き込み用ランスとを接続する固体還元材吹き込み停止時専用気体還元材吹込み管と、前記固体還元材吹き込み停止時専用リング状気体還元材供給管に気体還元材を供給する固体還元材吹き込み停止時専用気体還元材供給管よりなる、高炉への気体還元材吹込装置。   A gas reducing material blowing device installed and used in a blast furnace that performs an operation of blowing a solid reducing material and a gas reducing material into a furnace from a tuyere, and a plurality of gas reducing material blowing devices disposed on an outer periphery of a furnace body of the blast furnace A ring-shaped gas reducing material supply pipe, a gas reducing material blowing pipe connecting the ring-shaped gas reducing material supply pipe and a gas reducing material blowing lance installed in the tuyere, and the ring-shaped gas reducing material supply pipe A gas reducing material supply main for supplying the gas reducing material to the pipe, and a gas reducing material supply pipe for branching from the gas reducing material supply main to supply the gas reducing material to the ring-shaped gas reducing material supply tubes. In addition, a ring-shaped gas reducing material supply pipe dedicated to stopping the blowing of the solid reducing material disposed on the outer periphery of the furnace body of the blast furnace, a ring-shaped gas reducing material supply pipe dedicated to stopping the blowing of the solid reducing material, and the gas reduction Solid reducing material blowing connecting the material blowing lance To the blast furnace, which consists of a dedicated gas reducing material blowing pipe at the time of stopping and a dedicated reducing gas supply pipe at the time of stopping the blowing of the solid reducing material for supplying the gaseous reducing material to the ring-shaped gas reducing material supply pipe dedicated to the stopping of the blowing of the solid reducing material Gas reducing material blowing device. 請求項1に記載の装置を用い、固体還元材と気体還元材とを羽口より炉内に吹込む操業を行なう高炉において、当該羽口から固体還元材の吹き込みを停止した際に、当該羽口の気体還元材吹き込み用ランスへのリング状気体還元材供給管からの気体還元材の供給を停止し、固体還元材吹き込み停止時専用リング状気体還元材供給管から前記気体還元材吹き込み用ランスに気体還元材を供給する高炉の操業方法。   In the blast furnace in which the solid reductant and the gas reductant are blown into the furnace from the tuyere using the apparatus according to claim 1, when the blowing of the solid reductant from the tuyere is stopped, The supply of the gas reducing material from the ring-shaped gas reducing material supply pipe to the lance for blowing the gas reducing material at the mouth is stopped, and the lance for blowing the gas reducing material from the ring-shaped gas reducing material supply pipe when the solid reducing material blowing is stopped is stopped. Of operating a blast furnace to supply gas reducing material to the furnace. 固体還元材の吹き込み停止前にリング状気体還元材供給管から供給していた気体還元材の流量よりも、固体還元材吹き込み停止時専用リング状気体還元材供給管から気体還元材吹き込み用ランスに供給する気体還元材の流量を増加させる、請求項2に記載の高炉の操業方法。   Compared to the flow rate of the gas reducing material supplied from the ring-shaped gas reducing material supply pipe before stopping the blowing of the solid reducing material, the dedicated ring-shaped gas reducing material supply pipe to the lance for blowing the gas reducing material when the solid reducing material blowing is stopped. The operating method of the blast furnace of Claim 2 which increases the flow volume of the gas reducing material to supply.
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JP4557156B2 (en) * 2005-01-31 2010-10-06 Jfeスチール株式会社 Reducing gas injection device to the blast furnace

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