JPS5953636A - Method for producing sintered ore - Google Patents
Method for producing sintered oreInfo
- Publication number
- JPS5953636A JPS5953636A JP16413682A JP16413682A JPS5953636A JP S5953636 A JPS5953636 A JP S5953636A JP 16413682 A JP16413682 A JP 16413682A JP 16413682 A JP16413682 A JP 16413682A JP S5953636 A JPS5953636 A JP S5953636A
- Authority
- JP
- Japan
- Prior art keywords
- quicklime
- sintered ore
- activity
- degree
- ore
- 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.)
- Granted
Links
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- Manufacture And Refinement Of Metals (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
この発明は、焼結原料のれ′1化を促進し焼結鉱の生産
性向トを図った焼結鉱製直性に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to straightness of sintered ore production which promotes sintering raw material layering and improves the productivity of sintered ore.
焼結鉱の製造絹、従来・i冊バ1.J:々1てあろ粉鉄
鉱イー1、ミルスケール、高炉ゲスト、転炉ダストMj
の含鉄原料と副原ネミ1である粉石灰石:ISよひ焼結
用IJh燃利としての粉コークスクロを、所定割かで配
合し、これにバインダーとして生石灰を添加の1、ミキ
ーリーでイ昆合造:fli’/、 シ、この造)’+)
j物をわ゛ε結機によって焼結している。Manufacture of sintered ore silk, conventional/i-book version 1. J: 1 Tearo iron ore E 1, mill scale, blast furnace guest, converter dust Mj
The iron-containing raw material and the powdered limestone which is the secondary raw material 1: The powdered coke black as the IJh fuel for IS sintering are mixed in a specified proportion, and quicklime is added as a binder. :fli'/, し, this construction)'+)
The material is sintered using a wafer sintering machine.
上述した焼結原料に生石灰を添IJII−J′ることは
、原料のれl化を促進し、焼結鉱の生産性を同士せしめ
る」−て極めて効果的である。Adding quicklime to the above-mentioned sintered raw material is extremely effective in promoting the sludge formation of the raw material and increasing the productivity of the sintered ore.
第1図は焼結原料に対せる生石灰の配合工程図で゛ある
。1はロータリキルンて、石灰石をロークリキルン1内
で焼成して生石灰となし、この生石灰を破f、j、:機
2で5 mm以丁に破砕し/こ後、ホッパー3に貯蔵す
る。ポツパー3内の牛(1灰は適宜リノ出してトラック
等により焼4i!i上場に運搬し、焼結−1,J易内の
ホッパー4に供給する。Figure 1 is a diagram showing the process of adding quicklime to the sintering raw materials. 1 is a rotary kiln, and limestone is burned in the rotary kiln 1 to produce quicklime, and this quicklime is crushed into pieces of 5 mm or smaller by a crusher 2, and then stored in a hopper 3. The ashes of the cows (1) in the potspar 3 are taken out as appropriate and transported by truck etc. to the sintering 4i!i listing, and then supplied to the hopper 4 in the sintering 1 and JI.
5は主原料貯蔵ホッパー、G 61粉コークスlri蔵
ポツパー、7は石灰石貯蔵ボッ・に−で、−1−原1”
l、粉コークス、石灰石および生石灰U」、前記各ホノ
・9− 力・らその所定j11か切出さノ1.−C=+
ンベア8によってミキv −jl K fJt hr+
t し、ミA−+j −(−1−Qii合’fM枝さ、
fIろ。次いて1)Iノ記ミキヅー9で造粒された原本
1シj、:コンベア10によってす3’l結機11に二
j(1(ばれ、ナ1シ、結(幾11で・焼結が7丁なわ
れイ)。5 is the main raw material storage hopper, G61 powder coke lri storage hopper, 7 is the limestone storage hopper, -1-raw 1"
1, coke powder, limestone and quicklime U'', each of the above-mentioned holes, 9-forces, and the prescribed cutting-out 1. −C=+
Miki v −jl K fJt hr+
t and MiA-+j-(-1-Qii combined'fM branch,
fI. Next, 1) The original material granulated by the granulator 9 is transferred to the sintering machine 11 by the conveyor 10. 7 cho nawarei).
しかイ)に、l(ゴイ−i I!には、−般に・t5′
ε結1″ハ、1より離21に石灰1: Jjj、で製f
青され、ロータリギルン1で製造後、ミキーリ−−9に
装入されるま−C12〜:t11粁過1ろことか多い。For l(goi-i I!), -general・t5'
ε connection 1″ C, distance from 1 21 lime 1: Jjj, made with f
After being produced in the rotary tank 1, it is charged into the mill 9.
その結果、生石灰か風(11: tでその活性度が低1
・し、焼結鉱の11産率が劣化′Jイ)間穎かあつブこ
。As a result, the activity of quicklime or wind (11: t is low at 1
・The production rate of sintered ore has deteriorated.
本発明者等は、1−述した間j、lぞI4、・11イ決
し、11イit火の活・f’1度低トヲ防イT W(、
生鉱の’1+’(’>率向1: ’;si IXI Z
)へく、生石灰の風化状態について調べ’/iZ o第
1表はその調査結果である。The inventors of the present invention determined that between the above-mentioned times, 11 and 11, the fire activation and f'1 degree low temperature were prevented.
'1+' of raw ore ('> rate 1: ';si IXI Z
) Table 1 shows the results of the investigation on the weathering state of quicklime.
一1記のような活性度の低+4、牛イ1灰のf−″11
σ別に調ヘブこ。第2図(イ)(ロ)は生石1大の紅+
1、・1111数と活・V119との関係なノjり1グ
ラフて゛、1lil l:zl(イ)のり印&iオ′1
′/度が0〜5市の牛イi灰、同図(I])の(月−1
5はれ′1度か2〜5 mmの生石灰である。図面から
れかるように第2図(イ)におけ4)その′粒度かO〜
5 mmの生石灰より、同図(ロ)にJ−5け乙)その
t−1度か2〜5mmの7に石j大の方か、活性度の低
トかバしい。Low activity like 11th+4, f-″11 of beef i1 ash
Hebuko according to σ. Figure 2 (a) and (b) are one large raw stone red +
1, 1 graph of the relationship between the number 1111 and V119.
'/degree is 0 to 5 city cow II ash, same figure (I]) (month-1
5. It is quicklime with a 1 degree or 2 to 5 mm thickness. As can be seen from the drawing, in Figure 2 (a) 4) The grain size is O~
Compared to 5 mm of quicklime, the same figure (b) shows J-5.) It is either t-1 degree or 2 to 5 mm, which is the size of a stone, and the activity is low.
本発明者′″1はとの点に91ハで史に研究を進め、1
種造後の経φ“・目」数か2+1の生石灰につき、その
粒jc別の7Sロ4j(4と、1)11記J′m1度別
(7J) ’Ig (’i灰kc 、j ロ焼生鉱のl
(、産率ろ・rl、lへ/。−6第:31″!、1は1
゛九゛1度別のだ11〕1度ケ示−1グラフ、第71図
ケ、J、 ’(::1磨削の/Itイ1)火しυよイ)
i’fと生鉱牛産率を71(−ずグツ゛)である。The inventor'''1 has conducted research on this point since 1991, and
7S ro 4j (4 and 1) 11 J'm 1 degree (7J) 'Ig ('i ash kc, j L of sintered ore
(, Production rate ro・rl, to l/.-6th: 31″!, 1 is 1
゛9゛1 degree different 11〕1 degree showing - 1 graph, Figure 71 ke, J, '(::1 grinding/It 1) fire υyo)
i'f and raw cattle production rate are 71 (-zugutsu゛).
第;う図および第2I l’−jl li・られかイン
ように、生石灰のれ′1度か小となるeコとその1占1
/1度は高くなり、t’t’g結鉱の生生鉱も同士する
。そのL’l 1+は、生石灰の゛べ1度が小てあT5
ば、ホッパー内での貯蔵時にその貯蔵法f、jI、−4
か密となり、火気に制;れイ)ことが少なく石−乙)ブ
こめと、l−、jわ1)イ)。As shown in Figure 2 and 2, the amount of quicklime is 1 degree or less, and its 1 value is 1.
/1 degree becomes higher, and the raw ore of t't'g condensation is also the same. The L'l 1+ has a small amount of quicklime T5.
For example, when storing in a hopper, the storage method f, jI, -4
It becomes dense, and it is difficult to avoid fire.
この発明は、1、記知見に基づいてなされたものて、ハ
゛1.結原4”l中に、パイングーとしての生石灰を添
加して混合造1′\′lし、この造本i’7物なt’、
7.生機によって焼結する焼結鉱の製造方法において、
v[1記!(;石灰の活性度な、その粒度を調整するこ
とにより製造時の活性度に近い状態となし、この製造1
1.lrの活性度に近い状態の生石灰を前記j:l’U
結原」:1中に添加してM、合造れ°l−tろことに特
徴なイJ−Jろものである。This invention has been made based on the following findings: 1. Add quicklime as pine goo to 4"l of Yuhara, mix 1'\'l, and make this book.
7. In a method for producing sintered ore, which is sintered with a green machine,
v [1st article! (By adjusting the activity of lime and its particle size, the activity is close to that at the time of production, and this production 1
1. The quicklime in a state close to the activity of lr is added to the j:l'U
"Yuhara": It is a J-J product that is unique in that it is made by adding M to the mixture.
次に、この発明を実施例により図((1(と共に説明1
ろ。Next, this invention will be explained with reference to Examples ((1) and Explanation 1.
reactor.
第5図は製置後の経過日数か2ト1の生石灰につき、そ
の粒)qと活性度との関係を詳細に調へたグラフで′、
れ“1度か0.25mm以]パの生イ1灰は、その活性
度が、’(60cc / 4 N−■(c 12以十の
優れたイj(iを示した0第6図は牛イ1灰全体に対寸
イ)前ふ一’、 (+、25 rn7n以上の私″1度
の生石灰の割合と、焼結鉱の生産率との関係を示せグラ
フてあイ)。なお、生石灰の(3’l結原利にス・1−
する配合率は2.0%としA二。図面から明らかなよう
に、0.25 am以十のオ’、ti 10−のもの力
; 75 i、f’i: ::j(%以十含1れている
牛イ1灰を使用したとき―、わ°L結生鉱生産率を顕′
Plしく“向1させイ)こと力・−(きた。Figure 5 is a graph that examines in detail the relationship between the grains of quicklime (q) and the activity of the quicklime for the number of days that have passed since it was made.
The activity level of the fresh ash of 1 degree or more than 0.25 mm is '(60cc/4 N-■(c). (+, Show the relationship between the proportion of quicklime and the production rate of sintered ore over 25 rn7n). In addition, quicklime (3'l
The blending ratio is 2.0% and A2. As is clear from the drawing, 75 i, f'i:::j (10% of the ash containing 0.25 am or more was used. When the production rate of crystallized ore is revealed,
Pl's "direction 1") power - (came).
1述しブこことか【)、+:ya結II;(オ′、1の
混合造1′1“lに際1〜.0.25市以1・″のれ1
度のべ、のが25屯′L11%慶、I−含まれている生
イ1灰を前記・ハ′、′、結原オ′1に添Jll’l
iイ)ことにより、焼結鉱の生I)(−棒く向1を図/
′、ことがてきる。1 mentioned here and here [), +:ya connection II;
At the same time, 11% of the raw ash contained in the mixture was added to the above-mentioned 25 ton'L 11% ash.
i) By this, the raw sintered ore I) (-bar direction 1 /
', things will happen.
生石1火のねT9を、(1,25mm以1・のイ、の力
;25重宿%以十と4:るように14)ためには、「j
−タ’J −1=ルンで、j:Ilv成され/こ生石灰
を破砕機て破1i’l’した後、これをT11!! (
欠で篩分けし、1述しブこ才)′ノ度j、j、lj成と
な4)ように調整すノ1翰上い。In order to make raw stone 1 fire T9 (force of 1.25 mm or more; 25 times more than 10 and 4: 14),
-Ta'J -1 = Run, j:Ilv was made/After this quicklime was crushed by a crusher, it was crushed by T11! ! (
Sieve it by 1) and adjust it so that the degree of j, j, lj is 4) higher.
次に、この発明の他の実1jOi。例について説明する
。Next, another example of this invention is 1jOi. Let's discuss an example.
この実施例では前記第1図に示した一■稈図に:I3い
て、ポツノP −3からL;lI出さ、lz ・I:I
7;結」場Vcilf jl @ i%ブこ牛(if火
を、filシ(i174 k、′幾12においてilF
破1i’+! した後、ミA−リ−9に装入−Jろもの
てあ60 + ’、316破砕機12に送りこ斗〕する
牛イ1灰のホノ・ξ−てある。破砕機12は、例えば多
数の鉄棒からなる2つの(IJ筒筒状外体lIいに嵌合
しあつ″C逆回’ID、寸イ、こノニ眞より、前記篭体
内に供給された’I、f−i灰な破砕1′る今一ジミル
等か使用される。In this example, in the culm diagram shown in FIG.
7; Conclusion field Vcilf jl @ i%bukogyu(if fire, filshi(i174 k,' 12 in ilF
Break 1i'+! After that, the ashes of the cows are charged into the mill 9 and sent to the 316 crusher 12. The crusher 12 comprises, for example, two cylindrical outer bodies that are fitted into each other and are supplied into the housing from a number of iron rods. I, f-i, etc., are used for rough crushing.
この実施例に4゜いては、1−述しft pH< ll
(、(−j灰をミキーリーに装入−Jろ的「111に破
砕1ろものであるから、ミギツーに装入された牛イ1灰
には、前記破砕によって活性面か露出し、従ってその活
性I身を向1″さぜるこさができる。In this example, at 4°, 1-ft pH < ll
(, (-J ash is charged into Miquily - Jro's ``111'' is crushed, so the active surface of the ash charged into Migi2 is exposed due to the crushing, and therefore its active surface is exposed.) The active body can be stirred 1" in the direction.
第2図(イ)(ロ)には、i[1述した如く製造後の1
−1数の経過と共に活性度の低下し21こ生石灰((月
田)を、60メソシユ以Fに破砕した場合の活111度
が×印で示されている。図面から明らかなよ”)t/?
: z製造後2〜31−1紅過し活1ソ1度が著しく低
I・シ、フこ生石1火て゛も、これを破6/、’+4−
jることにより、製造IL’rに近い1古性度まで回復
させることがてきた。Figure 2 (a) and (b) show i [1 after manufacturing as described above.
The activity level decreases with the passage of time, and when 21 pieces of quicklime (Tsukita) is crushed to 60 degrees F or more, the activity level is 111 degrees, which is shown by the x mark.It is clear from the drawing. /?
: 2~31-1 red filtration after z production 1 degree is extremely low I・C, 1 fire stone also breaks this 6/, '+4-
By doing so, it has been possible to restore the antiquity to 1, which is close to the production IL'r.
第2表には破砕処理を実施しに場合と′−j′、施しな
い場合の生石灰の活性度と、この’l:イi灰を・焼結
原料に2.0%の率で配合したときの焙、生鉱の牛J栢
率とタンブラ−強度(T、1.>が示されている。Table 2 shows the activity of quicklime with and without crushing treatment, and the activity of quicklime with and without crushing treatment, and this ash mixed with the sintering raw material at a rate of 2.0%. The grain rate and tumbler strength (T, 1.) of the raw ore are shown.
なお、生石灰の焼結原料に対−する配合率は、前述した
ηII<2.0%千゛あるが、この配合’=f=−υま
ト記式%式%
によって表わされるものである。The blending ratio of quicklime to the sintering raw material is ηII<2.0%, as described above, and is expressed by the following formula: %=f=-υ.
含鉄原オ・1+石1火石」−生石灰−1−jス鉱−1−
述したことから、ハ“1、結反オτ)の’lJt’:合
造f:I′fに際し、焼結反aS+に添加1゛ろ生石灰
に破砕処理をIjqiぜば、焼結鉱の生産率を顕習に向
1−でぜろことがてきイ)。Iron-bearing raw mineral 1 + stone 1 flint” - quicklime - 1 - j-smine - 1 -
From the above, it can be seen that if 'lJt' of '1. If you want to learn the rate, you can get zero at 1-).
第13表に、この゛IC5明方法により、J:l’t、
結反Flに添加′Jる生石灰に対1.− CI述しfc
>′:を度構成J、/こは破砕処理を施した本発明の
場合と、このような処理を施さなV=従来の場aとの生
石灰の活゛1!1度、ミギサーによる造粒前とjsニー
41’7後の平均1′\′I径、43よひ、焼結鉱の生
産率・々ンブラー強1α(T、I)の比較を示す。Table 13 shows that J:l't,
Addition of 1. - CI description fc
>': is the degree configuration J, / is the case of the present invention subjected to crushing treatment, and V = conventional case a without such treatment. A comparison of the average 1'\'I diameter, 43yo, the production rate of sintered ore, and the tumbler strength 1α (T, I) before and after js knee 41'7 is shown.
第 3 表
上記第:3表から明らかなように、不発明方J<により
生石灰のl、:V′i、度を調整すればその1m個度は
高まり、焼結鉱の生産率・タンブラ−強度・を向上させ
ることかで゛きイ)。Table 3 As is clear from Table 3 above, by adjusting the l, :V′i, degree of quicklime, its 1m degree increases, and the production rate and tumbler of sintered ore increase. It is possible to improve strength.)
1−述したように、この発明方法により生石灰を篩分け
iたは破砕処理によりその粒度調整な?)なうときは、
その活性度を高め焼結鉱の生産率を向−1さぜることが
てきるが、ロータリー・1ルンて焼成し、ilI&砕槻
て破砕しa ll:石灰を、イ・活性ガス雰囲気の容器
中に貯l1Ij +、製造時の活性1σに近い状態に保
持してミキリ・−に装入するようにし7てイ、よい。第
21図(イ)(ロ)の11印は、このようにした生石灰
の活性度で・、製造r;63 If紅J静時もその17
i性度は製造時とは々んど変ることはなかった。1-As mentioned above, is it possible to adjust the particle size of quicklime by sieving or crushing it according to the method of this invention? ) When you are ready,
It is possible to increase its activity and increase the production rate of sintered ore by 1. It is possible to store l1Ij + in a container and maintain the activity at a state close to 1σ at the time of manufacture and charge it into a mill. The 11 marks in Figure 21 (a) and (b) indicate the activity of the quicklime made in this way.
The degree of ionicity did not change much from that at the time of manufacture.
1−述の説明において、活′[411度は、/IO°C
の水21K5F’1gの生石灰(Ca、O)を投入して
;う分間取で水和した11:石灰の1iを4 N −H
c l液で滴定し、使用したAN−HC1液のlI(で
)Jクシ/こ。まにタンブラ−強度(T、I)は、径!
l ] 4 mm、長さ/1577BH1)”ノさ6
mmのドラムの内周K)1(径JJ向にわブころlI5
0mm、I¥さ6 gの羽根2枚か取−(=Jけら°t
′lた回転1゛ラムを[要用し、前記回転ドラム内に1
0〜25mmの粒度の焼結鉱3kgな人t1.1分間2
71回の回転速度で2 (10回回転させに後に10m
m以1−の:1i57度をもつ焼結鉱かある割合て示し
k。ll4に生産率は、焼結機のパレット火格子] r
r+j当りの1時間における5 mm以1−の+:S’
l結鉱の生生鉱貸JてlI<シた。1- In the above explanation, active'[411 degrees is /IO°C
of water 21K5F' 1g of quicklime (Ca, O) was added;
Titrated with Cl solution and used AN-HC1 solution. Mani tumbler strength (T, I) is the diameter!
l ] 4 mm, length/1577BH1)" length 6
mm drum inner circumference K)1 (Wave roller lI5 in diameter JJ direction
0mm, I ¥ 6 g 2 blades
A rotating 1 inch ram is required, and a 1 inch rotating drum is required.
3 kg of sintered ore with a particle size of 0 to 25 mm per person 1.1 min 2
2 at a rotation speed of 71 times (10 m after 10 rotations)
The sintered ore having a temperature of 1-57 degrees is indicated by a certain percentage of k. ll4 production rate, pallet grate of sintering machine] r
+ of 5 mm or more in 1 hour per r+j: S'
I rent raw ore from condensate.
以1−説明したように、この発明方θ、ンこ、1−って
、・j尭結反利中に活・1f1゛度の高い生石灰′l?
−汀加−4゛ることにより、焼結鉱のll:産生が高め
ら111、l’、+l ’Jijj I”jの品1(、
)7の優才1にハ゛L生鉱をりI+ 4<高く製造し得
イ、−!7’ % 、、、1.’、業[優れた効宋か’
1)fcらされる。As explained above, this invention method θ, Nko, 1- is quicklime with a high degree of activity during the reaction.
By adding -4゛, the ll: production of sintered ore was increased.
) 7's advantage 1 can be manufactured with high L raw ore I+ 4 < high, -! 7'%,,,1. ', Work [Excellent effect Song?'
1) Be forced to fc.
第1図は焼結原料に剣1゛る生石灰の配合」、稈図、第
214(イン(ロ)は生石灰の紅過1ヨ数と活ツソ1″
1aとの関係を示−1グラフ、第3図は生石灰のね度と
活・V1度との関係を示1グラフ、第4図は/11石灰
のi::r、 I!3と・焼結骨、の牛p(率との関係
をlJ<1ダラ−)、第5図&」生石灰の粒度範囲別と
活性度との関係を示−ノ゛グラフ、第6図は生石灰中に
43ける(、) 、 2 !’l mm、 LJ、1・
の’141i j(1−のイ、ののa有’l’fi n
とハ′1、生鉱の生産活りの関係ろ・示イグラフである
。図面KJ3V/′1て、1 ロークリギルン、2・(
IIq砕機、3. /I、5゜0.7 ボンノ?−1
8,1(1・・−1ンベノ′、9 ミへ−→] − 、
1 1 灯ε 糸占機1、第2
、(イ)
(′O)
第、′3図 第4図
第1)図
209−
イL L (mm)
手続袖正書(自発)
illjl !1fζ 1 、□ 14ii′1・
冒′山長′11 オー′l 杉 +]l ノ、
1侵2 づ【=明の名称
焼結鉱の製造方法
3、 iii +1を一ノーる名
’il′lとの1几t 特許出願人
jl′111j 東京°都丁代[1J区丸の内−1
月11番、・じ[I、;、−1(F7.■)、)11木
鋼管株式会?1代表渚 金 Ff′
訂自 発
+11 明糸I11 ?+、ij+′r′白、発明の
rl’ III f(、:i(叫1ト”+珀、1から第
1 i+イ+’ fl、
[
!1イ1ト)(
とある41、
」
とfil’ ifする・・
(2) 明イ1101:、第10白、発明の檜π()
1な;i(1明の」■1.1かf、 P4′1.j l
・1J「1、[−□゛、1\7治−人J)、−1とある
を−[/;八に9を人IIs JとFil’ ilず
ろ」ソ、lFigure 1 shows the mixture of quicklime in the raw material for sintering, and culm diagram, Figure 214 (in (b) shows the amount of red 1" of quicklime and 1" of live lime.
-1 graph shows the relationship between 1a, Figure 3 shows the relationship between quicklime thickness and active V1 degree, and Figure 4 shows /11 lime i::r, I! Figure 5 shows the relationship between the particle size range of quicklime and the activity level, Figure 6 shows the relationship between the grain size range of quicklime and the activity level. 43 in quicklime (,), 2! 'l mm, LJ, 1・
'141i j (1-'s i, no's a'l'fin
This is a graph showing the relationship between raw ore production. Drawing KJ3V/'1, 1 Rokurigirun, 2・(
IIq crusher, 3. /I, 5°0.7 Bonno? -1
8,1 (1...-1 nbeno', 9 mihe-→] -,
1 1 Light ε Thread reading machine 1, 2nd, (A) ('O) No., '3 Fig. 4 Fig. 1) Fig. 209-I L L (mm) Procedural Sleeve Book (Spontaneous) illjl! 1fζ 1 , □ 14ii′1・
Exploring Yamacho'11 O'l Sugi +]l ノ,
1 in 2 zu [= Ming name method for producing sintered ore 3, iii +1 in the name 'il'l' Patent applicant jl'111j Tokyo ° Miyako [1J-ku Marunouchi-1]
Monthly No. 11, Ji [I, ;, -1 (F7. ■), ) 11 Wood Steel Pipe Co., Ltd.? 1st representative Kim Nagisa Ff'
Edited by +11 Akito I11? +, ij+'r'white, invention rl' III f(,:i(scream 1t"+珀, 1 to 1st i+i+'fl, [!1i1t)(Toaru 41,"fil' if... (2) Mei 1101:, 10th White, Invention Hinoki π ()
1na;i (1明の」■1.1kaf, P4'1.j l
・1J "1, [-□゛, 1\7ji-jin J), -1 and wo-[/; eight to nine people IIs J and Fil' il zuro" So, l
Claims (1)
混合造粒し、この造粒物を焼結機によって焼結づる°焼
結鉱の製造方法において、前記生石灰の活にト度を、そ
の粒度を、’i+、+1 =i脅−することにより製造
時の活性度に近い状態となし、この製造時の活性度に近
い状態の生石灰を前記焼結原料中に添加して混合潰’l
:j−′jることを特徴とする焼結鉱の製造方法。In the sintering raw material, a binder and 1. In the method for producing sintered ore, the quicklime is mixed and granulated, and the granulated product is sintered using a sintering machine. The activity is brought to a state close to that at the time of manufacture by stirring, and quicklime with an activity close to the time of manufacture is added to the sintered raw material and mixed and crushed.
A method for producing sintered ore, characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16413682A JPS5953636A (en) | 1982-09-22 | 1982-09-22 | Method for producing sintered ore |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16413682A JPS5953636A (en) | 1982-09-22 | 1982-09-22 | Method for producing sintered ore |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5953636A true JPS5953636A (en) | 1984-03-28 |
| JPS6142768B2 JPS6142768B2 (en) | 1986-09-24 |
Family
ID=15787426
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16413682A Granted JPS5953636A (en) | 1982-09-22 | 1982-09-22 | Method for producing sintered ore |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5953636A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04328A (en) * | 1990-04-18 | 1992-01-06 | Nippon Steel Corp | Manufacture of sintered ore |
| WO1999009224A1 (en) * | 1997-08-12 | 1999-02-25 | Voest-Alpine Industrieanlagenbau Gmbh | Method and equipment for processing iron- or oil-containing metallurgical waste |
| KR100504365B1 (en) * | 2000-08-19 | 2005-07-29 | 주식회사 포스코 | Manufacturing method of sinter ore in high combined water ore mixing |
-
1982
- 1982-09-22 JP JP16413682A patent/JPS5953636A/en active Granted
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04328A (en) * | 1990-04-18 | 1992-01-06 | Nippon Steel Corp | Manufacture of sintered ore |
| WO1999009224A1 (en) * | 1997-08-12 | 1999-02-25 | Voest-Alpine Industrieanlagenbau Gmbh | Method and equipment for processing iron- or oil-containing metallurgical waste |
| KR100504365B1 (en) * | 2000-08-19 | 2005-07-29 | 주식회사 포스코 | Manufacturing method of sinter ore in high combined water ore mixing |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6142768B2 (en) | 1986-09-24 |
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