JPH04123237U - Melting reduction furnace - Google Patents

Melting reduction furnace

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Publication number
JPH04123237U
JPH04123237U JP2696691U JP2696691U JPH04123237U JP H04123237 U JPH04123237 U JP H04123237U JP 2696691 U JP2696691 U JP 2696691U JP 2696691 U JP2696691 U JP 2696691U JP H04123237 U JPH04123237 U JP H04123237U
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pulverized coal
furnace
reforming
injection lance
gas
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JP2556619Y2 (en
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弘充 森寺
隆 中村
成行 矢動丸
雅夫 山内
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新日本製鐵株式会社
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Abstract

(57)【要約】 【目的】 溶融還元炉から発生する排ガスを改質するた
めに適性の高い粉炭吹込みランスを備えた溶融還元炉を
提供する。 【構成】 炉肩部の炉壁に、炉外側から炉内側に下向き
に傾斜する貫通孔を設け、この貫通孔に先端部に上向き
の粉炭吹出し口を形成する扇状の粉炭吹出しノズルを設
けたガス改質用粉炭吹込みランスを炉内に対して進退自
在に挿入し、必要に応じて、この粉炭吹込みランスをそ
の軸心を中心に回動自在にしたことを特徴とするもので
あり、ガス改質効果の大きい炉内排ガス領域に粉炭を効
果的に拡散、接触させ、排ガスに対する改質反応効率を
向上すると共に、スラグ浴への未反応粉炭の降下量を少
なくして、溶融還元反応効率の低下を防止する。
(57) [Summary] [Purpose] To provide a smelting reduction furnace equipped with a pulverized coal injection lance that is highly suitable for reforming exhaust gas generated from the smelting reduction furnace. [Structure] A through hole is provided in the furnace wall at the furnace shoulder, which slopes downward from the outside of the furnace to the inside of the furnace, and this through hole is equipped with a fan-shaped pulverized coal blowing nozzle that forms an upward pulverized coal blowing port at the tip. A pulverized coal injection lance for reforming is inserted into the furnace so that it can move forward and backward, and the pulverized coal injection lance can be rotated around its axis as necessary, The pulverized coal is effectively diffused and brought into contact with the flue gas area in the furnace where the gas reforming effect is large, improving the reforming reaction efficiency for the flue gas, and reducing the amount of unreacted pulverized coal falling into the slag bath, thereby promoting the smelting and reduction reaction. Prevent loss of efficiency.

Description

【考案の詳細な説明】[Detailed explanation of the idea]

【0001】0001

【産業上の利用分野】[Industrial application field]

本考案は、溶融還元に伴い生成する排ガスを予備還元装置の還元ガスとして用 いるための排ガス改質用の粉炭吹出みランスを備えた溶融還元炉に関するもので ある。 This invention uses the exhaust gas generated during smelting reduction as the reducing gas in the preliminary reduction device. This relates to a smelting reduction furnace equipped with a pulverized coal blowing lance for exhaust gas reforming. be.

【0002】0002

【従来の技術】[Conventional technology]

従来から、粉鉱石を予備還元装置によって予備還元し、これを溶融還元炉で溶 融還元して溶鉄を得る製鉄技術が知られている。 Conventionally, fine ore is pre-reduced using a pre-reducing device and then melted in a smelting reduction furnace. Iron manufacturing technology that obtains molten iron by melting and reducing is known.

【0003】 この技術においては、一般に溶融還元炉で生成された排ガスを予備還元装置の 還元ガスとして利用されるようになっており、その還元力を高めるために(CO2 +H2 O)/(CO2 +CO+H2 +H2 O) で表されるガスの酸化度(OD )を高めるガス改質が行われるのが通例となってきている。[0003] In this technology, the exhaust gas generated in the smelting reduction furnace is generally used as the reducing gas in the preliminary reduction device, and in order to increase its reducing power, (CO 2 + H 2 O)/( It has become common practice to carry out gas reforming to increase the degree of oxidation (OD) of the gas, expressed as CO 2 +CO + H 2 +H 2 O).

【0004】 このガス改質の手段としては、一般に排ガス中に石炭粉末を主体とするガス改 質剤を吹込み、排ガスの顕熱を反応(吸熱)の熱源として利用する方法が知られ ており、この改質剤の吹込みは例えば、特開昭63−140012号のように溶 融還元炉の上方に設けられた煙道や、特開昭63−140014号のように溶融 還元炉の炉壁から行われたり、あるいは、特開平1−116020号のように酸 素吹込みランスと兼用するランスから行うようにしたものが知られている。0004 As a means of reforming this gas, generally speaking, gas reforming mainly consisting of coal powder is used in the exhaust gas. A method is known in which the sensible heat of the exhaust gas is used as a heat source for the reaction (endothermic) by injecting a bulking agent into the reactor. For example, the injection of this modifier is carried out as in JP-A-63-140012. The flue installed above the fusion furnace and the melting It is carried out from the furnace wall of a reduction furnace, or it is carried out using an acid as in JP-A No. 1-116020. It is known that the process is performed using a lance that also serves as a plain blowing lance.

【0005】[0005]

【考案が解決しようとする課題】[Problem that the idea aims to solve]

上記のような溶融還元炉の排ガスの酸化度を低減させるための石炭粉によるガ ス改質においては、その改質効果は改質剤である石炭粉が有する気化物(VM) の気化特性、粒度等の性状と操業条件や、炉壁条件等によって変化し易い排ガス の温度、酸化度等排ガスの状態に左右されることが本考案者等の実験により判明 している。 Coal powder gas is used to reduce the degree of oxidation of flue gas from smelting reduction furnaces as described above. In coal powder reforming, the reforming effect is due to the vapors (VM) contained in the coal powder, which is the modifier. Exhaust gas tends to change depending on properties such as vaporization characteristics and particle size, operating conditions, furnace wall conditions, etc. Experiments conducted by the inventors revealed that the temperature and degree of oxidation depend on the condition of the exhaust gas. are doing.

【0006】 しかし、前記従来のガス改質においては、これらの変化を充分考慮したガス改 質剤の吹込みが行われているとは言い難く、溶融還元反応ゾーンにガス改質剤で ある石炭粉が入り、溶融還元効率が低下し、また、この石炭粉のガス改質剤への 寄与が低下するという問題点がある。[0006] However, in the conventional gas reforming mentioned above, gas reforming takes these changes into consideration. It is difficult to say that the injection of the modifier is being carried out, and the gas modifier is not being injected into the smelting reduction reaction zone. Some coal powder enters, reducing the smelting reduction efficiency, and this coal powder is also injected into the gas modifier. There is a problem in that the contribution decreases.

【0007】 本考案は、溶融還元炉の排ガス改質を効率的に行うために適性の高い粉炭吹込 みランスを設けた溶融還元炉を提供するものである。[0007] This invention is a highly suitable pulverized coal injection method for efficiently reforming exhaust gas in a smelting reduction furnace. The present invention provides a melting reduction furnace equipped with a safety check.

【0008】[0008]

【課題を解決するための手段】[Means to solve the problem]

本考案は、鉄浴面上方の炉肩部炉壁に下向きに傾斜した貫通孔を設け、この貫 通孔から炉内に対して進退自在に挿入され、その先端部に上向きの粉炭吹出し口 を扇状に形成したガス改質用粉炭吹込みランスを備えた溶融還元炉であり、必要 に応じて該ランスの軸心を中心として回動自在とすることを特徴とするものであ る。 In this invention, a downwardly sloping through hole is provided in the furnace wall at the furnace shoulder above the iron bath surface. It is inserted into the furnace through a through hole so that it can move forward and backward, and there is an upward pulverized coal outlet at its tip. This is a smelting reduction furnace equipped with a fan-shaped pulverized coal injection lance for gas reforming. The lance is characterized by being rotatable about the axis of the lance according to the Ru.

【0009】[0009]

【作用】[Effect]

本考案の溶融還元炉においては、炉況に応じて、粉炭の吹込み位置をガス改質 反応が効率的に行われる条件を備えた位置に調整自在であり、高温排ガス流に対 して、粉炭を上向きにかつ扇状に吹き出し、拡散させて、粉炭と排ガス流との接 触度を高め、ガス改質反応の向上を可能にする。 In the smelting reduction furnace of this invention, the injection position of pulverized coal can be adjusted with gas according to the furnace conditions. It can be adjusted to a position that provides conditions for efficient reaction, and is suitable for high-temperature exhaust gas flow. The pulverized coal is blown upward in a fan shape, dispersed, and brought into contact with the exhaust gas stream. It increases the viscosity and makes it possible to improve the gas reforming reaction.

【0010】0010

【実施例】【Example】

図1は、本考案の一実施例を示す転炉型の溶融還元炉の一部における縦断面説 明図であり、1は転炉型の溶融還元炉で、炉殻鉄皮2と、その内側に内張りされ た耐火れんが3からなる炉壁を有している。 Figure 1 shows a vertical cross-section of a part of a converter-type melting reduction furnace showing one embodiment of the present invention. 1 is a converter-type melting reduction furnace, with a furnace shell shell 2 and a lining inside it. The furnace wall is made of refractory bricks.

【0011】 この炉壁のトラニオン軸側の炉肩部には、炉外側から炉内側に約20°傾斜す る貫通孔4が設けられており、この貫通孔4には粉炭吹込みランス5が炉内に対 して進退自在でかつその軸心を中心として回動自在に挿入されている。[0011] The furnace shoulder on the trunnion shaft side of this furnace wall has a slope of approximately 20° from the outside of the furnace to the inside of the furnace. A through hole 4 is provided in which a pulverized coal injection lance 5 is inserted into the furnace. It is inserted so that it can move forward and backward and rotate freely around its axis.

【0012】 この粉炭吹込みランス5の先端部には、スリット状の粉炭吹出し口6を有する 扇状の粉炭吹出しノズル7が、図2に示すように、その軸心Jcが粉炭吹込みラ ンスの軸心Cと130°の角度で上向きに取り付けられている。0012 The tip of this powdered coal injection lance 5 has a slit-shaped powdered coal outlet 6. As shown in FIG. 2, the fan-shaped pulverized coal blowing nozzle 7 has its axis Jc aligned with the pulverized coal blowing lamp. It is attached upward at an angle of 130° with respect to the axis C of the appliance.

【0013】 この粉炭吹出しノズル7の粉炭吹出し口6は、図3に示すように、粉炭吹込み ランス5の軸心を中心として直角ではなく10°位傾斜して設けられている。[0013] As shown in FIG. It is not provided at right angles to the axis of the lance 5 but at an angle of about 10 degrees.

【0014】 これは、図4に示すように、粉炭吹込みランス5がトラニオン軸心Tcから若 干外れた位置に対向配置していることによるものであり、両側の粉炭吹込みラン ス5を炉心に向けて、正対して配置する場合には直角に設けても良い。[0014] As shown in FIG. 4, this is due to the fact that the pulverized coal injection lance 5 This is because the pulverized coal injection runs on both sides are placed opposite each other in dry areas. When the base 5 is disposed directly facing the reactor core, it may be provided at right angles.

【0015】 Pは粉炭吹込みランス5の先端と粉炭吹出しノズル7の粉炭導入口との間に設 けたポケット部で、粉炭吹出しノズル7に粉炭を導入する場合に、均一な粉炭拡 散流を形成し、粉炭吹込みランス5の先端を保護する機能を有する。[0015] P is installed between the tip of the pulverized coal injection lance 5 and the pulverized coal inlet of the pulverized coal blowing nozzle 7. When introducing pulverized coal into the pulverized coal blowing nozzle 7 in the pocket section, uniform pulverized coal is spread. It has the function of forming a scattered flow and protecting the tip of the pulverized coal injection lance 5.

【0016】 8は粉炭吹込みランス5にその軸方向にスライド自在に設けた歯車で、支持体 Fに設けられたランス回動モーター9により回転する歯車10と噛み合っている 。11は粉炭吹込みランス5に設けたラックで、支持体Fに設けられたランス進 退モーター12によって回転するピニオン13と噛み合っている。14は炉内中 心部に挿入された酸素吹込みランスである。[0016] 8 is a gear provided on the pulverized coal injection lance 5 so as to be able to slide freely in the axial direction of the lance 5; It meshes with a gear 10 that is rotated by a lance rotation motor 9 provided at F. . 11 is a rack provided on the pulverized coal injection lance 5, and the lance advance provided on the support F. It meshes with a pinion 13 rotated by a retraction motor 12. 14 is inside the furnace It is an oxygen-blowing lance inserted into the core.

【0017】 図1に示すような粉炭吹込み構造は、図4に示すように溶融還元炉1の炉壁に 対向して設けられており、この対向する両粉炭吹込みランス5から粉炭吹出しノ ズル7を経てその粉炭吹出し口6から吹き出された粉炭は、上下方向に約20° の広がりを持ち、平面的に見て左右に約30°の広がりを持って拡散し、上方の 炉中心部の酸素ランス14の先端(酸素吹出し口)より上方領域において、排ガ ス流と激しく接触混合する。この領域は、通常操業状態においては、図5の(a )に示すように、ガス流が上向きであり、同図の(b)に示すように、高温でか つ酸化度が高い。[0017] The pulverized coal injection structure shown in Fig. 1 is installed on the wall of the smelting reduction furnace 1 as shown in Fig. 4. The pulverized coal blowing lances 5 are provided facing each other, and the pulverized coal blowing lances 5 are provided facing each other. The pulverized coal blown out from the pulverized coal outlet 6 through the nozzle 7 is approximately 20° vertically. It has a spread of about 30 degrees to the left and right when viewed from above, and In the area above the tip (oxygen outlet) of the oxygen lance 14 in the center of the furnace, the exhaust gas Mix by vigorous contact with the gas stream. In normal operating conditions, this area is (a) in Figure 5. ), the gas flow is upward, and as shown in (b) of the same figure, the gas flow is at high temperature. High degree of oxidation.

【0018】 したがって、この領域に吹込まれた粉炭、は反応効果の小さい領域から、反応 効果の大きい領域にこの排ガス流の上昇流によって拡散、接触し、上昇しながら 排ガスと反応するので、接触飛行時間も長く、充分にガス改質に寄与する。[0018] Therefore, the powdered coal injected into this area will react from the area where the reaction effect is small. While spreading, contacting, and rising by this upward flow of exhaust gas flow in the area with a large effect. Since it reacts with the exhaust gas, the contact flight time is long and it fully contributes to gas reformation.

【0019】 したがって、ガス改質に寄与しないまま、スラグ浴中に降下して、溶融還元反 応を阻害する懸念も極めて少ないので、溶融還元効率も良好である。[0019] Therefore, the gas falls into the slag bath without contributing to gas reformation and reacts with smelting reduction. Since there is very little concern that the reaction will be inhibited, the melting reduction efficiency is also good.

【0020】 このガス改質はガス発生が多く、ガス改質効果の大きい排ガス状態、スラグレ ベルが安定状態にある安定操業状態下で行うことが望ましいが、これらの状態を 最適状態に維持する操業は難しく、変動するのが通例であるので、これらの状態 を把握して、これらの状態の変化に応じて、その状態で最適な粉炭吹込み条件を 得るため、粉炭の吹込みランスの挿入深度の調整、粉炭吹出し口の向きの調整、 粉炭の吹込み量の調整を行うことが必要である。[0020] This gas reforming generates a lot of gas, and the exhaust gas condition has a large gas reforming effect. It is preferable to carry out the operation under stable operating conditions when the bell is in a stable condition; Maintaining optimal operating conditions is difficult and fluctuations are common, so these conditions In response to changes in these conditions, we can determine the optimal pulverized coal injection conditions under those conditions. In order to obtain It is necessary to adjust the amount of pulverized coal injected.

【0021】 本考案においては、この粉炭吹込みランス5は炉内に対して、進退自在で、又 、粉炭吹出し口6の向きを調整自在であり、粉炭吹込み量の調整も容易にできる ようにすることによって、前述のような調整が容易にできる構造を有するもので ある。[0021] In the present invention, this pulverized coal injection lance 5 can move forward and backward into the furnace, and The direction of the pulverized coal outlet 6 can be adjusted freely, and the amount of pulverized coal injected can be easily adjusted. By doing so, it has a structure that allows for easy adjustment as described above. be.

【0022】 また、前記の炉内状態を検知する検知手段と組み合わせることによって、各検 知手段からの情報を処理して粉炭吹込みランスの深度、粉炭吹出し口の向き、粉 炭吹込み量等を自動的に調整することも容易である。[0022] In addition, by combining with the detection means for detecting the condition inside the furnace, each inspection The information from the knowledge means is processed to determine the depth of the pulverized coal injection lance, the direction of the pulverized coal outlet, and the It is also easy to automatically adjust the amount of charcoal injection.

【0023】 上記のような構造を有する本実施例の転炉型溶融還元炉において排ガスの改質 を行った場合の結果を、図1の溶融還元炉と同様の転炉型溶融還元炉で酸素吹込 みランスの外周に粉炭吹込み口を形成した従来例によって排ガスの改質を行った 場合の結果(比較例)と共に以下に説明する。[0023] Reforming of exhaust gas in the converter type smelting reduction furnace of this example having the structure as described above. The results obtained when oxygen was blown in a converter type melting reduction furnace similar to the melting reduction furnace shown in Figure 1. Exhaust gas was reformed using a conventional method in which a pulverized coal inlet was formed around the outer periphery of the mirance. This will be explained below along with the results of the case (comparative example).

【0024】 基本操業条件は、表1の通りで、本発明の実施例、比較例共に共通である。粉 炭の吹込みを行わない場合の排ガスの酸化度は44〜54%で平均では約50% である。[0024] The basic operating conditions are as shown in Table 1, and are common to both the examples of the present invention and the comparative examples. powder The degree of oxidation of exhaust gas without charcoal injection is 44 to 54%, with an average of about 50%. It is.

【0025】[0025]

【表1】 [Table 1]

【0026】 この基本条件で操業し、炉内への粉炭吹込みによる排ガス改質を行い、粉炭吹 込み開始直後から吹込み終了直後までの炉口からの排ガスをダクトを経て回収す る過程で酸化度限定装置を設け、酸化度を連続的に測定した結果、本考案の実施 例では、32〜40%の範囲にあり、平均では約35%となった。すなわち、本 考案では約30%排ガスの酸化度を低下させることができ、ほぼ、満足するガス 改質ができた。なお、本実施例ではスラグ浴面レベルは大巾な変動がなかったの で、粉炭吹込みランス、酸素吹込みランスの挿入深度、粉炭吹出し口の向きの調 整は行われなかった。[0026] Operating under these basic conditions, the exhaust gas is reformed by injecting powdered coal into the furnace, and the The exhaust gas from the furnace mouth from immediately after the start of injection to immediately after the end of injection is collected through the duct. During the process, an oxidation degree limiting device was installed and the oxidation degree was continuously measured. In the example, it was in the range of 32-40%, and the average was about 35%. i.e. book The idea is to reduce the degree of oxidation of exhaust gas by about 30%, which is almost satisfactory. The modification was completed. In addition, in this example, the slag bath level did not fluctuate widely. Adjust the insertion depth of the pulverized coal injection lance and oxygen injection lance, and the direction of the pulverized coal outlet. No adjustment was made.

【0027】 これに対して、比較例では酸化度は38〜48の範囲にあり、平均では42% となった。即ち、比較例では約16%排ガスの酸化度を低下できたが、これでは 充分なガス改質ができたとは言い難い。[0027] On the other hand, in the comparative examples, the oxidation degree was in the range of 38 to 48, with an average of 42%. It became. In other words, in the comparative example, the degree of oxidation of exhaust gas could be reduced by about 16%; It is difficult to say that sufficient gas reforming was achieved.

【0028】 この実施例と比較例におけるガス改質結果は、操業条件、炉壁状況、粉炭の性 状、吹込み条件等によって多少異なるが、概ね、上述のようなガス改質結果が得 られる。[0028] The gas reforming results in this example and comparative example depend on the operating conditions, furnace wall condition, and properties of powdered coal. Although it varies slightly depending on the condition, blowing conditions, etc., in general, the gas reforming results as described above can be obtained. It will be done.

【0029】 なお、本考案における粉炭吹込みランスの挿入角度については、該ランスへの スラグの流入を防止するため下向きとし、その先端部の粉炭吹出しノズルの粉炭 吹出し口からガス改質反応の良好なスラグ浴面上方の炉心部付近の領域に粉炭を 充分に拡散して到達させ、かつその飛行時間を長くして、排ガスとの接触を充分 にして、ガス改質反応効率を高める意味から、垂直線に対して20〜40°の範 囲に設定することが望ましい。[0029] In addition, regarding the insertion angle of the pulverized coal injection lance in this invention, The pulverized coal of the pulverized coal blowing nozzle at the tip of the pulverized coal is oriented downward to prevent the inflow of slag. Powdered coal is supplied from the outlet to the area near the reactor core above the slag bath surface where the gas reforming reaction is good. It diffuses sufficiently to reach the destination, and its flight time is extended to ensure sufficient contact with the exhaust gas. In order to increase the efficiency of the gas reforming reaction, It is desirable to set the

【0030】 また、粉炭吹込みランスの先端部に設けた粉炭吹出しノズルは、上向き、すな わち、粉炭吹出し口は粉炭を上向きに吹き出すように設けられており、その上向 きの角度については、、粉炭吹込みランスの挿入角度、挿入深度にも関係があり 、上述のように、粉炭をガス改質反応の良好な領域に拡散して到達させ、かつ、 その飛行時間を長くして排ガスとの接触を充分にして、ガス改質反応効率を高め る意味から、粉炭吹込みランスの軸線に対して90〜140°の範囲に設定する ことが望ましい。さらに、粉炭の吹き出し流の拡散角度は上下方向に10〜30 °、平面的に見て左右に20〜50°の範囲になるように粉炭吹出しノズルを設 計することが望ましい。[0030] In addition, the pulverized coal blowing nozzle installed at the tip of the pulverized coal injection lance is directed upward and downward. In other words, the pulverized coal outlet is installed to blow out the pulverized coal upward; The insertion angle is also related to the insertion angle and insertion depth of the pulverized coal injection lance. , as mentioned above, diffuse the pulverized coal to a region where the gas reforming reaction is favorable, and The flight time is increased to ensure sufficient contact with the exhaust gas, increasing the efficiency of the gas reforming reaction. Therefore, it should be set in the range of 90 to 140 degrees with respect to the axis of the pulverized coal injection lance. This is desirable. Furthermore, the diffusion angle of the pulverized coal blowout flow is 10 to 30 in the vertical direction. °, the pulverized coal blowing nozzle is set so that it is within the range of 20 to 50 degrees to the left and right when viewed from above. It is desirable to measure the

【0031】 なお、本実施例においては、粉炭吹込みランスをその軸心を中心に回動できる ようになっており、粉炭吹出しノズルは扇状に形成されたスリット状の粉炭吹出 し口を有しているが、このスリットの長さは短くして、即ち、拡散角度を小さく し、粉炭吹込みランスを回動して、拡散範囲を経時的に広げるようにしても良く 、この場合は、スリット状のほか、他の丸、角、三角、楕円、多角形状の吹き出 し口を複数並設しても良い。また粉炭吹込みランスは2本を対向設置したが、こ れは転炉型の溶融還元炉で傾動するため、傾動側には粉炭吹込みランスを挿入す ることは困難なためである。固定型の溶融還元炉の場合は、この粉炭吹込みラン スは、炉壁周方向にほぼ等間隔で複数本(通常3〜6本程度)挿入することが好 ましい。[0031] In addition, in this example, the pulverized coal injection lance can be rotated around its axis. The pulverized coal blowing nozzle is a slit shaped fan-shaped pulverized coal blowing nozzle. However, the length of this slit is shortened to reduce the diffusion angle. However, the pulverized coal injection lance may be rotated to widen the diffusion range over time. , in this case, in addition to slit-shaped speech bubbles, other round, square, triangular, oval, and polygonal speech bubbles A plurality of ports may be arranged in parallel. In addition, two pulverized coal injection lances were installed facing each other, but this Since this is a converter-type smelting reduction furnace that tilts, a pulverized coal injection lance is inserted on the tilting side. This is because it is difficult to For fixed smelting reduction furnaces, this pulverized coal injection run It is preferable to insert multiple screws (usually about 3 to 6) at approximately equal intervals around the furnace wall. Delicious.

【0032】 なお、この粉炭吹込みランスの上下方向の粉炭吹き出し位置や吹き出し方向等 をすべて同じにする必要はなく、たとえば、酸素吹込みランスの挿入位置が偏心 している場合等は、排ガス流分布が偏るので、この場合には等間隔でなくても良 く、またレベルは不揃いにすることが、ガス改質反応効率を上げる上で有効であ る。[0032] In addition, the vertical position and direction of the pulverized coal blowing lance of this pulverized coal injection lance, etc. They do not all have to be the same; for example, if the insertion position of the oxygen injection lance is In such cases, the exhaust gas flow distribution will be biased, so in this case, the intervals may not be equal. In addition, it is effective to increase the gas reforming reaction efficiency by making the levels uneven. Ru.

【0033】[0033]

【考案の効果】[Effect of the idea]

本考案においては、粉炭吹込みランスを炉内に下向きに傾斜して、炉内に対し て、その深度を調整でき、粉炭吹出し口をその先端部から上向きに調整可能にで きるようにしているので、ガス改質反応に大きな影響を与える炉内のガス状態の 変化に応じて最適な粉炭吹込み位置の調整ができ、排ガスに対して粉炭を充分に 拡散接触させて、吹込み粉炭の排ガス改質に対する反応効率を向上し、ガス改質 反応に寄与しない粉炭のスラグ中への混入を防止して、溶融還元反応効率も向上 させることができる。 In this invention, the pulverized coal injection lance is tilted downward into the furnace. The depth of the pulverized coal can be adjusted, and the pulverized coal outlet can be adjusted upward from its tip. The gas condition inside the furnace, which has a large effect on the gas reforming reaction, can be controlled. The optimal pulverized coal injection position can be adjusted according to changes, ensuring that sufficient pulverized coal is injected into the exhaust gas. Through diffusion contact, the reaction efficiency of blown pulverized coal for exhaust gas reforming is improved, resulting in gas reforming. Prevents the mixing of powdered coal that does not contribute to the reaction into the slag, improving the efficiency of the smelting reduction reaction. can be done.

【図面の簡単な説明】[Brief explanation of drawings]

【図1】本考案の溶融還元炉の縦断面説明図である。FIG. 1 is an explanatory longitudinal cross-sectional view of a melting reduction furnace of the present invention.

【図2】図1における粉炭吹込みランスの先端部の拡大
説明図である。
FIG. 2 is an enlarged explanatory view of the tip of the pulverized coal injection lance in FIG. 1;

【図3】図2の平面説明図である。FIG. 3 is an explanatory plan view of FIG. 2;

【図4】粉炭吹込みランスの対向配置を示す平面説明図
である。
FIG. 4 is an explanatory plan view showing the opposing arrangement of pulverized coal injection lances.

【図5】(a)は定常操業状態における炉内ガス流速分
布を示す説明図であり、(b)は定常操作状態における
炉内温度分布と酸化度分布を示す説明図である。
FIG. 5(a) is an explanatory diagram showing the gas flow rate distribution in the furnace in a steady operating state, and FIG. 5(b) is an explanatory diagram showing the in-furnace temperature distribution and oxidation degree distribution in the steady operating state.

【符号の説明】[Explanation of symbols]

1 溶融還元炉 2 炉殻鉄皮 3 耐火れんが 4 貫通孔 5 粉炭吹込みランス 6 粉炭吹出し口 7 粉炭吹出しノズル 8 歯車 9 ランス回動モーター 10 歯車 11 ラック 12 ランス進退モーター 13 ピニオン 14 酸素吹込みランス 1 Melting reduction furnace 2 Furnace shell 3 Firebrick 4 Through hole 5 Powdered coal injection lance 6 Powdered coal outlet 7 Powdered coal blowing nozzle 8 Gears 9 Lance rotation motor 10 Gears 11 rack 12 Lance forward/backward motor 13 Pinion 14 Oxygen injection lance

───────────────────────────────────────────────────── フロントページの続き (72)考案者 山内 雅夫 大阪府堺市築港八幡町1番地 新日本製鐵 株式会社堺製鐵所内 ──────────────────────────────────────────────── ─── Continuation of front page (72) Creator Masao Yamauchi Nippon Steel, 1 Chikko Yawatacho, Sakai City, Osaka Prefecture Inside Sakai Iron Works Co., Ltd.

Claims (2)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 炉肩部の炉壁に、炉外側から炉内側に下
向きに傾斜する貫通孔を設け、この貫通孔に、先端部に
上向きの粉炭吹出し口を形成する扇状の粉炭吹出しノズ
ルを設けたガス改質用粉炭吹込みランスを炉内に対して
進退自在に挿入したことを特徴とする溶融還元炉。
Claim 1: A through hole is provided in the furnace wall of the furnace shoulder portion, which slopes downward from the outside of the furnace to the inside of the furnace, and a fan-shaped pulverized coal blowing nozzle having an upward pulverized coal blowing opening at its tip is installed in this through hole. A smelting reduction furnace characterized in that a pulverized coal injection lance for gas reforming is inserted into the furnace so that it can move forward and backward.
【請求項2】 炉壁に設けた貫通孔に炉内に対して進退
自在に挿入されたガス改質用粉炭吹込みランスが、その
軸心を中心に回動自在であることを特徴とする請求項1
記載の溶融還元炉。
[Claim 2] A pulverized coal injection lance for gas reforming, which is inserted into a through hole provided in the furnace wall so as to be able to move forward and backward into the furnace, is rotatable around its axis. Claim 1
The described melting reduction furnace.
JP2696691U 1991-04-20 1991-04-20 Smelting reduction furnace Expired - Lifetime JP2556619Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2696691U JP2556619Y2 (en) 1991-04-20 1991-04-20 Smelting reduction furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2696691U JP2556619Y2 (en) 1991-04-20 1991-04-20 Smelting reduction furnace

Publications (2)

Publication Number Publication Date
JPH04123237U true JPH04123237U (en) 1992-11-06
JP2556619Y2 JP2556619Y2 (en) 1997-12-08

Family

ID=31911355

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2696691U Expired - Lifetime JP2556619Y2 (en) 1991-04-20 1991-04-20 Smelting reduction furnace

Country Status (1)

Country Link
JP (1) JP2556619Y2 (en)

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Publication number Publication date
JP2556619Y2 (en) 1997-12-08

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