JPS61204346A - Operating method for sintering where emission of nitrogen oxide is controlled - Google Patents

Operating method for sintering where emission of nitrogen oxide is controlled

Info

Publication number
JPS61204346A
JPS61204346A JP4586085A JP4586085A JPS61204346A JP S61204346 A JPS61204346 A JP S61204346A JP 4586085 A JP4586085 A JP 4586085A JP 4586085 A JP4586085 A JP 4586085A JP S61204346 A JPS61204346 A JP S61204346A
Authority
JP
Japan
Prior art keywords
sintering
limestone
water
raw material
moisture
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
Application number
JP4586085A
Other languages
Japanese (ja)
Inventor
Kiyoshi Kojima
清 小島
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP4586085A priority Critical patent/JPS61204346A/en
Publication of JPS61204346A publication Critical patent/JPS61204346A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To sharply reduce the quantity of NOx emitted, while maintaining high productivity, by pelletizing sintering material with specific water content by use of limestone having grains with <=1mm grain size in higher weight percentage than usual and by feeding the pelletized material into a continuous downward suction-type sintering machine so as to supply during combustion the surface of a sintering bed with a specific amount of water. CONSTITUTION:In the process of sintering operation, the limestone having >=60wt.% grains with <=1mm grain size is used with 4-6% water for pelletization to pelletize the sintering material. This sintering material is fed into the continuous downward suction-type sintering machine so that surface of the sintering bed where coke combustion reaction is in progress is supplied with water by 5-90L/t-(raw material).

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は製鉄業における焼結鉱の製造方法に係わるもの
である。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for producing sintered ore in the steel industry.

(従来の技術) 周知の如く、高炉法(−おいて高炉に投入する鉄鉱石は
焼結鉱(−することが望ましく、現在広く行わ几ている
(Prior Art) As is well known, in the blast furnace method, the iron ore to be charged into the blast furnace is preferably sintered ore, which is currently widely practiced.

また、その焼結鉱製造方法としては、鉄鉱石原料とコー
クス、石灰石粉などを必要に厄じて所定量配合し、水を
添加して擬似粒化した後、連続下方吸引式焼結機で焼結
することが一般的に行われていることも周知である。
In addition, the sintered ore manufacturing method involves mixing a predetermined amount of iron ore raw materials, coke, limestone powder, etc., adding water to form pseudo-granules, and then using a continuous downward suction sintering machine. It is also well known that sintering is a common practice.

ところで、焼結鉱を製造すゐ(二際し、焼結原料に混合
しtコークスの燃焼排ガス中にNOx−が存在し、環境
上大きな問題となっており、現在、NOxの発生を極力
抑えた焼結作業を行うことが必要となっている。
By the way, when manufacturing sintered ore, NOx exists in the combustion exhaust gas of t-coke mixed with the sintering raw material, which poses a major environmental problem. It is now necessary to carry out additional sintering work.

NOxの発生を抑制するための方法として、焼結原料C
;混甘せる石灰石粉を細粒化し、かつ生石灰または消石
灰を使用することが特開昭55−107739号公報(
を開示さnている。
As a method to suppress the generation of NOx, sintering raw material C
; JP-A-55-107739 discloses that the limestone powder to be mixed and sweetened is finely granulated and quicklime or slaked lime is used.
has been disclosed.

(本発明が解決、しようとする問題点)前記の石灰石を
細粒化する方法ではNOx発生量は低下するが、原料の
粒径が小さくなるために通気性が悪くなり、結果として
生産性が低下してしまう。また、こnに生石灰、消石灰
を組み会わせnば確かに生産性低下を回避でき、かつN
Ox抑制効果も助長さnるが、生石灰、消石灰は糎めて
高価であり、結果として焼結鉱製造コストヲ押し上げて
しまうという問題点がある。
(Problems to be solved by the present invention) Although the above-mentioned method of making limestone into finer particles reduces the amount of NOx generated, the particle size of the raw material becomes smaller, resulting in poor air permeability and, as a result, productivity decreases. It will drop. Also, if you combine quicklime and slaked lime, you can certainly avoid a drop in productivity, and
Although the Ox suppression effect is helpful, quicklime and slaked lime are relatively expensive, and as a result, there is a problem in that they increase the cost of producing sintered ore.

(問題点を解決するための手段及び作用)本発明では前
記の問題点を有利(=解決するために3つの技術的手段
を用いる。すなわち、第1点は、鉄鉱石、石灰石、コー
クスに水を添加して混含擬似粒化するに際し、該石灰石
の粒度として、通常の焼結操業では1■以下の重量割付
が30〜50Xのものを使用するのが一般的であるが、
こるが、こ′i″′Lを4,0〜6.OXの範囲に調整
、することである。第3点は、焼成反応進行中、焼結ベ
ッド上面から5.0〜9Q、0l/t−原料の水分を供
給することである。
(Means and effects for solving the problems) The present invention uses three technical means to advantageously solve the above problems. Namely, the first point is that iron ore, limestone, and coke are When adding limestone to create pseudo-granules, it is common to use limestone with a grain size of 30 to 50X with a weight distribution of 1 square or less in normal sintering operations.
However, it is necessary to adjust this 'i'''L to a range of 4.0 to 6.OX.The third point is that during the sintering reaction, 5.0 to 9Q, 0l/ t- To supply moisture to the raw material.

すなわち、本発明は、焼結操業方法において。That is, the present invention relates to a sintering operation method.

粒度1.0四以下が60重量に以上の石灰石を用い。Limestone with a particle size of 1.04 or less and a weight of 60 or more is used.

造粒水分を4.0〜6.0にとして焼結原料を造粒し焼
結原料を連続下方吸引式焼結機(;供給し、コークス燃
焼反応進行中の焼結ベッド表面へ5.0〜90、0l/
t−原料の水分を供給すること?特徴とする窒素酸化物
の発生を抑制した焼結操業方法である。
The sintering raw material is granulated with a granulation moisture content of 4.0 to 6.0, and the sintering raw material is fed to a continuous downward suction sintering machine (; and the sintering material is fed to the surface of the sintering bed where the coke combustion reaction is in progress. ~90,0l/
t- Supplying moisture to raw materials? This is a sintering operation method that suppresses the generation of nitrogen oxides.

とnら3つの手段の相互作用を述べる。まず、焼結層上
から供給する水分、すなわち水または水蒸気は、燃焼帯
に達した際に次の2つの反応(二よりH2を生成する。
and n et al. describe the interaction of the three means. First, when the moisture supplied from above the sintered layer, that is, water or steam, reaches the combustion zone, it undergoes the following two reactions (2) to generate H2.

Q + H,O→OO+ H3 O0+ H20→002+H2 この反応で生成しfF−H2の還元作用によj) NO
x発生量が低下するわけであり、更(二粒変の小さい石
灰石全使用することは上記HS生成反応を促進するとと
によりH2のNOx還元効果を高めようとするものであ
る。また、焼結ベッド上から供給した水分は燃焼帯の下
方に形成さnる水分翠1帯(=おける凝縮水分となり、
擬似粒子間の空隙の閉塞、さらには過剰水分による擬似
粒子の合体流動化現象を起こし、通気性の低下、コーク
ス燃焼反応の阻害を銹引し、NOx発生量を増加させて
しまう、そこで、原料の水分を、焼結ベッド上から供給
さn1水分凝縮帯(二て凝縮する水分に相当するだけ低
下させることにより、コークス燃焼反応阻害を防止し、
上記のH2によるNOx還元効果と相まってNOxを大
幅に低下させるのである。
Q + H, O→OO+ H3 O0+ H20→002+H2 Produced in this reaction and due to the reduction action of fF-H2 j) NO
In addition, the use of all limestone with small grain size promotes the above-mentioned HS production reaction and thereby increases the NOx reduction effect of H2. The moisture supplied from above the bed becomes condensed moisture in a zone of moisture that forms below the combustion zone.
The voids between pseudo-particles are blocked, and the pseudo-particles coalesce and fluidize due to excess moisture, which reduces air permeability, inhibits the coke combustion reaction, and increases the amount of NOx generated. By reducing the moisture in the n1 moisture condensation zone (which is supplied from above the sintering bed) by an amount corresponding to the moisture that condenses, inhibition of the coke combustion reaction is prevented.
Combined with the NOx reducing effect of H2 mentioned above, this significantly reduces NOx.

本発明者らが、以上の手段によりNOx発生量を低下さ
せるべく実験を行ったところ、まず焼結ベッド上からの
水分供給量としては901/を一原料が上限で、そn以
上では吸引ガス中のO3濃度が低下し、コークス燃焼を
阻害するため(二、かえってNOx発生量が増加してし
まうこと、および5L/を一原料以下の少量ではNOx
低減効果が得らfLないことがわかつ几。また、造粒水
分としては6Xが上限であジ、こn以上では湿潤帯での
凝縮水分が増し、前記理由(=よりNOx発生量の低下
幅は小さくなってしまう。下限値?4Nと規定した理由
は、そn以下では原料の擬似粒化が進まず、 NOx発
生量増加のみならず、生産性、歩留も極端(二悪化する
からである。
The present inventors conducted an experiment to reduce the amount of NOx generated by the above means, and found that the upper limit for the amount of moisture supplied from above the sintering bed was 901/ml per raw material; Because the O3 concentration in the coke decreases and inhibits coke combustion (2), the amount of NOx generated increases on the contrary, and if the amount is less than 5L per raw material, NOx
It turns out that no reduction effect can be obtained. In addition, the upper limit of granulation moisture is 6X, and if it is higher than this, the condensed moisture in the wet zone will increase, and the reduction in NOx generation will be smaller due to the above reason (=).The lower limit is specified as 4N. The reason for this is that below that n, the pseudo-granulation of the raw material does not proceed, and not only does the amount of NOx generated increase, but the productivity and yield are also extremely deteriorated.

石灰石粒度(=関しては、その粒度を1四以下重量割会
で60に以上にすることにより、 NOx低減量が大き
くなる。
Regarding the limestone particle size (=), by increasing the particle size to 14 or less or more than 60 in terms of weight ratio, the amount of NOx reduction increases.

第2図は石灰石虫■以下重量割會とNOx発生量の関係
を示したものであるが、石灰石中1m以下重量割合を6
0X以上とし、かつ水蒸気を噴霧することにより、単な
る石灰石粒度の細粒化以上(二大幅にNOxを低下させ
ることができる。この理由としては、微細な石灰石がコ
ークスの燃焼に触媒作用を及ぼし、H2の発生を促進す
ることにより、そのNOx還元作用(二よってNOx発
生量が抑制さ几るものと考えら几る。
Figure 2 shows the relationship between the weight ratio of limestone insects and the amount of NOx generated.
By increasing the temperature to 0X or more and spraying water vapor, it is possible to reduce NOx significantly more than simply reducing the particle size of limestone (2).The reason for this is that fine limestone has a catalytic effect on the combustion of coke, It is thought that by promoting the generation of H2, the NOx reduction effect (2) will suppress the amount of NOx generated.

水分、すなわち水および/まtは水蒸気等の供給の態様
は、一様に供給できる手段1例えば散布、塗布等でよく
、例えば水と水蒸気を混會rgK、霧散布することもで
きる。焼結初期の1内温度が十分上っていない部分はあ
まり効果がなく、H2Oが0または00  と反応する
部分、すなわちコークス燃焼中のみ供給することが効果
がある。
Moisture, ie, water and/or water vapor, may be supplied by any means capable of uniformly supplying, such as spraying or coating. For example, a mixture of water and steam or spraying may also be used. It is not very effective in the part where the internal temperature of 1 is not sufficiently high at the beginning of sintering, and it is effective to supply H2O only in the part where it reacts with 0 or 00, that is, during coke combustion.

(実施例) 原料条件として、鉄鉱石56.2N、返鉱30.0に、
蛇紋岩2.1Xおよび本発明(−規定する範囲の粒度に
調整した石灰石11.7Xf配合し、コークス3.6X
f外数として加え、本発明に規定する範囲の水分で造粒
した原料を、火格子面積280−のD賦下方吸引焼結機
(こよりl厚500■、吸引負圧140011IIH2
0で、焼結鉱ベッド上面より水または水蒸気を噴霧状に
して本発明(:規定する範囲の量を散布し穴。散布方法
を第1図で説明すると、1は湿潤帯、2は燃焼帯、3は
焼結完了帯であり、燃焼帯:電域上面に焼結機幅方向に
水分供給ノズル4f設首し、均等に噴霧散布した。その
結果と、比較例として従来の造粒水分と石灰石粒度で焼
結鉱ベッド上面に噴霧散水しtものを表1に示し念。
(Example) As raw material conditions, iron ore 56.2N, return ore 30.0,
Serpentine 2.1X and the present invention (- limestone 11.7Xf adjusted to the particle size within the specified range, coke 3.6X
The raw material granulated with moisture in the range specified in the present invention in addition to the outside number of
At 0, water or steam is sprayed from the top surface of the sintered ore bed in an amount within the specified range. , 3 is the sintering completion zone. Combustion zone: 4 f moisture supply nozzles were installed in the width direction of the sintering machine on the upper surface of the electric zone, and the water was evenly sprayed. The results are shown below, and as a comparative example, conventional granulation moisture and Table 1 shows the results of spraying water on the top surface of the sinter bed with limestone particle size.

表1から明らかの如く、本発明に規定する範囲に石灰石
粒度及び造粒水分を調整し、かつ焼結(=際し水または
水蒸気を噴霧散布したものは、従来の石灰石粒度、原料
水分で散水したものに比べ。
As is clear from Table 1, the limestone particle size and granulation water content are adjusted to the range specified in the present invention, and water or steam is sprayed during sintering (= water or steam is sprayed during sintering). Compared to what I did.

NOx f大幅に抑制し、かつ生産性を向上させること
ができた。
It was possible to significantly suppress NOx f and improve productivity.

(発明の効果) 以上説明した如く、本発明方法によnばNOx発生量を
大幅に低下させ、かつ生産性を同上させることが可能で
ある。
(Effects of the Invention) As explained above, according to the method of the present invention, it is possible to significantly reduce the amount of NOx generated and to improve productivity.

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

第1図は実施例における水分供給方法を説明する図、 第2図は石灰石粒度、造粒水分、焼結中の水分供給量と
NOx発生量、燃焼帯移動速度の関係を示す図である。 1・・・湿潤帯、2・・・燃焼帯、3・・・焼結完了帯
、4・・・水分供給ノズル。 代理人 弁理士 秋 沢 政 光 他2名
FIG. 1 is a diagram illustrating the moisture supply method in the example, and FIG. 2 is a diagram showing the relationship between limestone particle size, granulation moisture, the amount of moisture supplied during sintering, the amount of NOx generated, and the combustion zone movement speed. 1... Moist zone, 2... Combustion zone, 3... Sintering completion zone, 4... Moisture supply nozzle. Agent: Patent attorney Masamitsu Akizawa and 2 others

Claims (1)

【特許請求の範囲】[Claims] (1)焼結操業方法において、粒度1.0mm以下が6
0重量%以上の石灰石を用い、造粒水分を4.0〜6.
0%として焼結原料を造粒し、焼結原料を連続下方吸引
式焼結機に供給し、コークス燃焼反応進行中の焼結ベッ
ド表面へ5.0〜90.0l/t−原料の水分を供給す
ることを特徴とする窒素酸化物の発生を抑制した焼結操
業方法。
(1) In the sintering operation method, the particle size of 1.0 mm or less is 6
Using 0% by weight or more of limestone, the granulation moisture content is 4.0-6.
The sintering raw material is granulated as 0%, and the sintering raw material is supplied to a continuous downward suction type sintering machine, and the moisture content of 5.0 to 90.0 l/t of the raw material is delivered to the surface of the sintering bed during the coke combustion reaction. A sintering operation method that suppresses the generation of nitrogen oxides.
JP4586085A 1985-03-08 1985-03-08 Operating method for sintering where emission of nitrogen oxide is controlled Pending JPS61204346A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4586085A JPS61204346A (en) 1985-03-08 1985-03-08 Operating method for sintering where emission of nitrogen oxide is controlled

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4586085A JPS61204346A (en) 1985-03-08 1985-03-08 Operating method for sintering where emission of nitrogen oxide is controlled

Publications (1)

Publication Number Publication Date
JPS61204346A true JPS61204346A (en) 1986-09-10

Family

ID=12730963

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4586085A Pending JPS61204346A (en) 1985-03-08 1985-03-08 Operating method for sintering where emission of nitrogen oxide is controlled

Country Status (1)

Country Link
JP (1) JPS61204346A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015200000A (en) * 2014-04-10 2015-11-12 新日鐵住金株式会社 Sinter ore production method
JP2020085275A (en) * 2018-11-19 2020-06-04 日本製鉄株式会社 Sintering machine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015200000A (en) * 2014-04-10 2015-11-12 新日鐵住金株式会社 Sinter ore production method
JP2020085275A (en) * 2018-11-19 2020-06-04 日本製鉄株式会社 Sintering machine

Similar Documents

Publication Publication Date Title
JP5194378B2 (en) Method for producing sintered ore
JP5315659B2 (en) Method for producing sintered ore
US3043652A (en) Fluid bed process for granulating fine-grained materials
CN110104969A (en) A kind of production technology of active lime
JP5617766B2 (en) Carbon material reforming equipment
JPS61204346A (en) Operating method for sintering where emission of nitrogen oxide is controlled
US5254320A (en) Method for roasting sulphide ores
JPS627806A (en) Direct steel making method using vertical furnace
CN1248636A (en) Method for making pellet agglomerate used in iron-smelting
EP3433388B1 (en) Process and facility for thermal treatment of a sulfur-containing ore
JPS61204342A (en) Manufacture of sintered ore
JPH10226825A (en) Method for granulating sintering raw material
CN109371235B (en) Based on NH3Desulfurization method for iron ore shaft furnace pelletizing process by slow release of binder
JPS61204345A (en) Operating method for sintering where emission of nitrogen oxide is controlled
CN113005284A (en) Application method of titanium-containing sea sand in sinter production
US4443250A (en) Process of producing sponge iron by a direct reduction of iron oxide-containing materials
JPH03193828A (en) Production of sintering raw material and sintered ore
JPS6250419A (en) Manufacture of sintered ore
JPS63149331A (en) Production of burnt agglomerated ore
JP7533404B2 (en) Apparatus and method for producing granulated sintered raw material
KR900005431B1 (en) Process for mixing sintered materials
JPS61266526A (en) Manufacture of sintered ore by high temperature firing fuel
JPS6237328A (en) Manufacture of sintered ore
JPH10219361A (en) Treatment of sintering raw material
JPS5983727A (en) Preparation of iron ore stock material to be sintered