JPS58164734A - Sintering method of ore - Google Patents

Sintering method of ore

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Publication number
JPS58164734A
JPS58164734A JP4775582A JP4775582A JPS58164734A JP S58164734 A JPS58164734 A JP S58164734A JP 4775582 A JP4775582 A JP 4775582A JP 4775582 A JP4775582 A JP 4775582A JP S58164734 A JPS58164734 A JP S58164734A
Authority
JP
Japan
Prior art keywords
rdi
coke
sintering
sintered ore
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
JP4775582A
Other languages
Japanese (ja)
Inventor
Daisuke Oiyama
老山 大輔
Minoru Watanabe
実 渡辺
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.)
JFE Steel Corp
Original Assignee
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP4775582A priority Critical patent/JPS58164734A/en
Publication of JPS58164734A publication Critical patent/JPS58164734A/en
Pending legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To manufacture a sintered ore having stable quality at the minimum blending amount of coke by sintering after controlling the blending amount of coke in a sintering raw material on a continuously moving pallet corresponding to an atmospheric moisture. CONSTITUTION:In the operation of endless continuous sintering machine, factors such as C.Rkg/t coke unit, SiO2%, FeO%, Al2O3% in the product and Ng/Nm<3> moisture in the air sucked from the pallet bottom have a correlation of following multiple regression equation (RDI)=-0.132(C.R)-3.29(SiO2)-2.07(FeO)-14.93 (Al2O3)+0.353N+94.44 against a reduction decomposition index RDI indicating a sintered ore quality and the partial correlation coefficient of N is the highest to RDI. Thus, the coke unit C.R necessary for obtaining the desired RDI corresponding to the moisture N in the air is obtained from the above-mentioned equation and the blending amount of coke is controlled. Thereby, the sintered ore having the desired quality can be obtained stably.

Description

【発明の詳細な説明】 本発明は鉱石の焼結方法に係り、詳しくは、−焼結鉱製
造時O機側空気中O温分に対応して焼結原料中の:1−
クスの配合量を調整し1品質的に安定化しえ焼結鉱が製
造できる鉱石の焼結方法に係る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for sintering ore, and more specifically, the present invention relates to a method for sintering ore.
The present invention relates to a method for sintering ore, which can produce sintered ore with stabilized quality by adjusting the blending amount of sous.

一般に1無端式連続焼艙機t)Ik’lllにおいては
焼結鉱の品質としてジャツー−指数(以下、単ec8I
という。)、還元崩壊指数(以下1単KRDIという、
)1にどを管理し例えば、8I〉89X、ルD1〈40
XK保っている。しかし、この中でRDIの管理は難し
く、特KJILJ$8においては凡DIが増大し1M化
する傾向がありえ。
In general, in an endless continuous burner (1) Ik'lll, the quality of the sintered ore is determined by the Jatu index (hereinafter referred to as "EC8I").
That's what it means. ), reduction decay index (hereinafter referred to as 1-unit KRDI),
) 1. For example, 8I>89X, le D1<40
I'm keeping XK. However, it is difficult to manage RDI among these, and there is a tendency for DI to increase and reach 1M especially at KJILJ$8.

この原因は、所謂シーズンオア、つま!P1夏期に入手
できない原料1にいし、夏期に水分の多くなる原料ある
い#i勢期に入手でき−Ikい原料の影響であると云わ
れている。
The cause of this is the so-called season or tsuma! It is said that this is due to the influence of raw material 1, which is not available during the P1 summer season, and raw materials with high moisture content during the summer season, or raw materials that are available during the P1 season and have a high moisture content.

すなわち、夏、冬で原料の構成差により。In other words, due to the difference in the composition of raw materials in summer and winter.

人J、0.. Na、OlK、0(RDIへの悪影響因
子)、8i0.(RDIへの好影響因子)1にどや成分
変動が生じ、その結果、成品焼結鉱0RDIが悪化する
ことがあるとされている。この丸め、成品焼結鉱0Fe
O(マグネタイト)量を増してRDIを調整すぺ〈、:
I−クス配合量を増加するととKよって封部されている
。しかし、従来のこのような方法では、夏期OR,DI
II化を完全に解消することはできず、バラツキも多く
Person J, 0. .. Na, OlK, 0 (negative influence factor on RDI), 8i0. (Favorable influence factors on RDI) 1. It is said that the 0RDI of the finished sintered ore may deteriorate as a result of fluctuations in the sintered ore composition. This rounded product sintered ore 0Fe
Adjust the RDI by increasing the amount of O (magnetite).
When the amount of I-X added is increased, the area is sealed by K. However, with this conventional method, summer OR, DI
II cannot be completely eliminated, and there are many variations.

RDIIiF通の九めに過剰なコークスを投入しえすす
るので、焼結の燃料費も増大するという間醜があった。
The disadvantage of RDIIiF was that excessive coke was added, which increased the fuel cost for sintering.

そこで本発明者等は、更に%研究し九ところ、RDIC
)季節的変動は、シーズンオアO影響よ如もむしろ、大
気中の湿分変動がもたらすのである仁とを知見した。
Therefore, the present inventors conducted further research and found that RDIC
) It was discovered that seasonal fluctuations are caused by changes in atmospheric moisture rather than by seasonal effects.

本実11&!、上記知見事実にもとづいて成立した一〇
であって、具体的には、焼結原料層に吸引される空気中
081分を連続的K11l定し、それに会わせて的確に
コークス配合量を調整して常に品質が安定化し九焼結鉱
が得られる鉱石の焼結方法を提案する。
Honji 11&! , 10 was established based on the above knowledge and facts, and specifically, 081 minutes in the air sucked into the sintering raw material layer is continuously determined, and the amount of coke blended is adjusted accordingly. This paper proposes a method of sintering ore that always stabilizes the quality and yields nine sintered ores.

以下1本発明方法に一’)%/hて詳L〈説明する。The method of the present invention will be explained in detail below in terms of 1')%/h.

まず、従来から焼結鉱のRDIが夏期に曇化する傾向の
あることは一舊で認められている。
First, it has long been recognized that the RDI of sintered ore tends to become cloudy in the summer.

例えば、5tll(a)tらびK(14#i2ツo製鉄
所の焼結縁@におけるBDI4D経時変化(えだし。
For example, 5tll(a)tRabiK(14#i2tsuo BDI4D change over time at the sintered edge @ of the steelworks.

横軸は2年間の各月を示す、)を示すグラフであって、
いずれにおいて本夏期[RDIが墨化しでいる(数値と
して#i−%をオーバーする)ことがわかる、この理由
は、上記の如くである。
The horizontal axis indicates each month of two years.
In both cases, it can be seen that this summer [RDI is blackened (numerical value exceeds #i-%), and the reason for this is as described above.

そこで、両者O相関を求めると、11!IEIK示す如
(i[DIJと「篩結磯の吸引空気中の湿分(大気湿分
)」とO関に#i強い相関が得られる。
Therefore, when we calculate the correlation between the two, it is 11! As shown by IEIK, a strong correlation is obtained between DIJ, ``moisture in the suction air of the sea sieve (atmospheric moisture)'' and O.

すなわち1両者の関#IcF1強い相関があ)、大気湿
分OSい時KRDIが愚仕する。
In other words, when there is a strong correlation between the two (IcF1) and the atmospheric humidity is low, KRDI is ineffective.

□ 焼結鉱0RDI#/140X以上になると、その使
用先の高炉の炉況を曇化させるケースが多く、一般的に
は40X以下、バラツキを考えると38X以下に管理さ
れることが必要である。一方、RDI[対して相関を持
つ因子として従来、コークス配合比(若しくij:y−
クス原単位)、AJ、0.、  N@、Q、y、、()
、 Pea、  Tie、、  8i0.、風量、生産
率などが明らかにされている。従って、それらの中のい
くつかの重要と思われる因子を組み合わせて重回帰式を
設定し、各因子の変化に対応してRDIを制御しようと
することが広くなされてい為、その試みの一例を示すと
□ When the sintered ore reaches 0RDI#/140X or higher, it often clouds the furnace conditions of the blast furnace where it is used, and generally it needs to be controlled at 40X or lower, and considering the variation, it needs to be controlled at 38X or lower. . On the other hand, coke blending ratio (or ij:y-
unit consumption), AJ, 0. , N@,Q,y,,()
, Pea, Tie,, 8i0. , air volume, production rate, etc. have been clarified. Therefore, it is widely used to set up a multiple regression equation by combining some of the factors considered to be important, and to control the RDI in response to changes in each factor. To show.

次の過少である。The following is an underestimation.

まず、 RDI[fil、て、コークス原単位(以  
     、。
First, RDI [fil, te, coke consumption unit (hereinafter referred to as
,.

下%C0Rという。)、x1中のSin、、成品中のp
ea、成品中のム40m、を因子として重回帰式(1)
を求める。
It is called lower %C0R. ), Sin in x1, p in the product
Multiple regression equation (1) using ea, 40m of weight in finished product as factors
seek.

(RDI ) −−0,4011(C,R)−7,!I
I(slO,)−0,1mPe0)−418(ムロ0.
)+ 10716          −−−−−−(
1)j4D(1)式KThh−[、例えば8hO,=l
L11%、 PeO−五9X、尤401■1.8にO場
合【。
(RDI) --0,4011 (C,R)-7,! I
I(slO,)-0,1mPe0)-418 (Muro 0.
)+10716 --------(
1) j4D (1) Formula KThh-[, e.g. 8hO,=l
L11%, PeO-59X, 401 ■ 1.8 if O [.

RDI≦36Nとする丸めに社1 一040@(C,R)−7,311X&9−0.191
1X&11−− fL18 X L8+ 167J6≦
sa     −”・−(2)が成立し1.、C0,l
L≧37.8111/lが得られる。
Rounding with RDI≦36N 1040@(C,R)-7,311X&9-0.191
1X & 11-- fL18 X L8+ 167J6≦
sa −”・−(2) holds and 1., C0, l
L≧37.8111/l is obtained.

ツマリ、3−7xl[単位C0aは37.811e/を
以上とすれば良い仁ととell、このように−3−クス
を調整して焼結が行なわれえ。
Sintering can be carried out by adjusting the -3-x in this way.

しかし、この場合の重相間係数は0.71!09 (寄
与率は0SZ)で必ずしも高くなく、実際の制御上でも
対応はあまり良くtk%/h、つまh上記O如く想定さ
れる;−クヌ調整量が與Ill[IKは過少であった一
過剰であ−)えすするととに’lk*、その結果、操業
上の不安定(RDIのバラツキも太きV%)からコーク
スを多iiK妃会することKKなって、焼結工場で燃焼
比を低減させることが困難であつ九。このため、この理
論と実際との誤差につき研究し九とζろ、その大部分は
大気湿分罠帰因している仁とがわかったのである。
However, the coefficient between multiple phases in this case is 0.71!09 (contribution rate is 0SZ), which is not necessarily high, and even in actual control, the correspondence is not good at tk%/h, which is assumed as O above; The adjustment amount was too low (IK was too low and too much), and as a result, due to operational instability (RDI variation was also large V%), coke was increased. However, it is difficult to reduce the combustion ratio in a sintering factory. For this reason, we studied the errors between this theory and reality, and found that most of them were due to atmospheric moisture traps.

そこで大気湿分N (f/N、l )との関連で重回帰
式を求めたところ、(3)丈が求められた。
Therefore, when a multiple regression equation was calculated in relation to the atmospheric humidity N (f/N, l), (3) length was calculated.

(RD I ) −−0,132(C,R) −3,2
9(8轟0)−K07(Fed)−14,93(AJ、
 0.)+0358N(f/Nd)+94.44・・・
・・・(3) 中でRDI[対する偏相閤係数が最も高いもの#isは
大気湿分であるという結果も確認された。
(RD I) --0,132 (C,R) -3,2
9 (8 Todoroki 0) - K07 (Fed) - 14,93 (AJ,
0. )+0358N(f/Nd)+94.44...
(3) It was also confirmed that among them, the component #is with the highest partial phase bias coefficient for RDI [is] atmospheric moisture.

従って1本発明においては、(31式にも゛とづいて大
気湿分と相関させてコークスを配合させてRDIの推定
精度を向上させる。すなわち、操業上では焼結鉱につき
a’ RD I(36X6(する必要があるため、この
条件にするための;−クス原単位の推定制度を向上させ
為とと[fk如、ζのコークス原単位で操業して、操業
安定(ルDIのバラツキ減少)が得られ、必然的IIc
:I−クス配会は、必畳最少限で向上し、焼結工場の燃
料費低下に寄与できることに1にる。
Therefore, in the present invention, the estimation accuracy of RDI is improved by blending coke in correlation with atmospheric moisture based on equation 31. That is, in operation, a' RDI ( 36X6 (to achieve this condition because it is necessary to ) is obtained, and the necessary IIc
:I-X distribution can be improved to the minimum necessary, contributing to a reduction in fuel costs at the sintering plant.

更に、詳しく説明すると、(3)丈において。To explain in more detail, (3) length.

810、−5.flX、F@0=t9N、人J、0.−
1.11N。
810, -5. flX, F@0=t9N, person J, 0. −
1.11N.

大気湿分−13t/Ngdの時KRDI≦36%のえJ
6[dC,R〉34.31に#/l  &いう結果が得
られる。
KRDI≦36% when atmospheric humidity is -13t/Ngd
6[dC,R>34.31, the result is #/l&.

つま抄、大気湿分が年平均(11,6f/N−)よ)や
中高い時においてRDIを36x以下に管層しようとす
ると111KIIi、コークス原単位を3418に#/
1(中子余裕を亀えせ九ask#/l)あえ塾で操業す
れば十分である。
Tsumasho, if you try to reduce the RDI to 36x or less when the atmospheric humidity is the annual average (11.6f/N-) or medium to high, it will be 111KIIi and the coke consumption rate will be 3418#/
1 (Nakako margin 9 ask#/l) It is enough to operate at Aejuku.

次に、@施例についてl!明する。Next, @ about the example l! I will clarify.

まず、gas図に示T如、<、s和55年り月〜12月
までは大気湿分が変化する□にも拘らず、この影響を考
えずに操業しえ、このll0RDIが変動し%41ec
m 7〜9月までOMはRDIが一%を越え、この時に
は;−タヌ配合比を増tlaIIせて対処し九が、オー
バーアクシ盲ン気味であり、コークス節減が達成されな
かつえ。
First, as shown in the gas diagram, even though the atmospheric humidity changes from January to December 2015, operations can be carried out without considering this effect, and this ll0RDI fluctuates by %. 41ec
From July to September, the RDI of OM exceeded 1%, and at this time, the combination ratio was increased to deal with the problem, but the situation seemed to be overextended, and coke reduction was not achieved.

これに対して、昭和56年1り〜12月oaaa本発明
によ如大気湿分の影響を考慮し、と(K。
On the other hand, from January to December 1981, the influence of atmospheric humidity was taken into consideration according to the present invention (K.

夏期の如く大気湿分の上昇に応じて予防的に:1−クス
配合比の増加させて調整を行なって操業しえ、この結果
、必WiIk少限のコークスで成品のRDIも目標の3
6X以下に収めるととができた。
In response to the rise in atmospheric humidity, such as in the summer, the operation can be carried out by increasing the 1-cox blending ratio, and as a result, the RDI of the finished product can be maintained at the target of 3 with a small amount of coke.
When it was kept below 6X, a sharp edge was created.

この場合、平均のコークス配合比で言えば比較例の55
年度は255XであるOK対し1本発明の56年度はz
soXであり、 0.05%の節減が彩れ、これは焼結
原料使用量3万トン7日の製鉄所では約5ooo t/
年のコークス滅につながった。
In this case, the average coke blending ratio is 55 in the comparative example.
The year is 255X, which is OK, whereas the year 56 of the present invention is z
s
This led to the extinction of coke in 2017.

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

1111図(14ならび−(9)はそれぞれ各年0RD
I′1 の変化を示すグラフ%112図はRDIと大気湿分との
関係を示すグラフ、II3図は本発明法と比較例との操
業におけるコークス配合比、RDI。 大気湿分等の関係を示すグラブである。 第1図 ((2) (bン @2図 大気湿分(97Nuす
Figure 1111 (14 and -(9) are each year 0RD
Graph %112 showing the change in I'1 is a graph showing the relationship between RDI and atmospheric moisture, and Figure II3 shows the coke blending ratio and RDI in the operation of the method of the present invention and the comparative example. This is a graph showing the relationship between atmospheric humidity, etc. Figure 1 ((2) (b@Figure 2 Atmospheric humidity (97Nu)

Claims (1)

【特許請求の範囲】[Claims] パレット下部から吸引される機側空気中011分に対応
させて焼結原料中Oコークス配合量を調整し、この焼結
原料を連続的に移動するバレツF上で!lIa#IIす
ることを特徴とする鉱石の焼結方法。
The amount of O coke in the sintering raw material is adjusted to correspond to the 011 minutes in the machine side air sucked from the bottom of the pallet, and this sintering raw material is continuously moved on Barret F! A method for sintering ore, characterized by carrying out lIa#II.
JP4775582A 1982-03-25 1982-03-25 Sintering method of ore Pending JPS58164734A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4775582A JPS58164734A (en) 1982-03-25 1982-03-25 Sintering method of ore

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4775582A JPS58164734A (en) 1982-03-25 1982-03-25 Sintering method of ore

Publications (1)

Publication Number Publication Date
JPS58164734A true JPS58164734A (en) 1983-09-29

Family

ID=12784170

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4775582A Pending JPS58164734A (en) 1982-03-25 1982-03-25 Sintering method of ore

Country Status (1)

Country Link
JP (1) JPS58164734A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6713144B2 (en) 1999-12-28 2004-03-30 Nippon Shokubai Co., Ltd. Multilayer material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6713144B2 (en) 1999-12-28 2004-03-30 Nippon Shokubai Co., Ltd. Multilayer material

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