JPS5950129A - Pretreatment of starting material for sintering - Google Patents

Pretreatment of starting material for sintering

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Publication number
JPS5950129A
JPS5950129A JP16017582A JP16017582A JPS5950129A JP S5950129 A JPS5950129 A JP S5950129A JP 16017582 A JP16017582 A JP 16017582A JP 16017582 A JP16017582 A JP 16017582A JP S5950129 A JPS5950129 A JP S5950129A
Authority
JP
Japan
Prior art keywords
sintering
pseudo
ore
dispersant
surfactant
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
JP16017582A
Other languages
Japanese (ja)
Inventor
Junsuke Haruna
春名 淳介
Mitsuru Yamashita
満 山下
Ichitami Suzuki
鈴木 一民
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.)
KOURIYUU KOGYO KK
Chiyoda Shoji Co Ltd
Nippon Steel Corp
Original Assignee
KOURIYUU KOGYO KK
Chiyoda Shoji Co Ltd
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 KOURIYUU KOGYO KK, Chiyoda Shoji Co Ltd, Nippon Steel Corp filed Critical KOURIYUU KOGYO KK
Priority to JP16017582A priority Critical patent/JPS5950129A/en
Publication of JPS5950129A publication Critical patent/JPS5950129A/en
Pending legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To obtain easily pseudo-granules of a starting material for sintering provided with suitable characteristics by using water contg. small amounts of a dispersant and a surfactant when the starting material is mixed and regulated to a prescribed water content. CONSTITUTION:A starting material for sintering prepared by combining fine iron ore with quick lime is blended with water contg. 0.01-1.0wt% dispersant and 0.001-0.1wt% surfactant, and they are mixed, regulated to a prescribed water content, and formed into pseudo-granules. Sodium acrylate, methacrylic acid hydroxyethylate, a methyl acrylate copolymer or the like is used as the dispersant, and a condensation product of naphthalenesulfonic acid with formaldehyde or the like is used as the surfactant. The pseudo-granules have a stable shape and superior mechanical strength, and they can ensure gas permeability when charged into a sintering machine. Accordingly, the productivity and yield of sintered ore can be improved.

Description

【発明の詳細な説明】 本発明は焼結原料の前処理方法に関する。[Detailed description of the invention] The present invention relates to a method for pretreating sintering raw materials.

焼結鉱は粉鉱石を部分溶融して塊成鉱としたものであり
、製鉄原料として大量に用層られている。
Sintered ore is made by partially melting fine ore to form agglomerated ore, and is used in large quantities as a raw material for iron manufacturing.

これは一般に原料である粉鉱石、返鉱粉、石灰石等に燃
料としての粉コークスを配合後、水を加えて調温造粒し
て得られる焼結原料疑似粒を焼結機に装入して焼成して
得られる。しかして一般に用いられる焼結機(ドワイト
ロイド式)では、点火炉内で上記原料粒の表層に点火し
、下向きに吸気して下層部迄燃焼させるものであり、装
入された原料粒層の通気性が焼結鉱製品の生産性を大き
く左右する。従って従来より焼結原料の造粒性を高め、
疑似粒化を改善し、原料粒層の通気性を確保する手段が
種々研究されている。その代表例としては生石灰、消石
灰等の所謂バイジター成分により微粉鉱その他の鉱石を
付着造粒させる方法が知られている。しかしながらこの
方法による場合、比較的多量の生石灰等の添加が必須と
なり、これは原料コストの上昇をきたし、生産性の向上
効果と相殺される。しかも一般に生石灰は水と接触して
消石灰となり、この時水和し、水をバイシダーとして粗
粒化するが、粗粒化した消石灰はもはや当初のバイ、、
/ター能を請失し、微粉鉱等の焼結原料の造粒性即ち疑
似粒子効果を奏し難くなる。
This is generally done by blending coke powder as a fuel with raw materials such as ore powder, return ore powder, and limestone, then adding water and granulating it at a controlled temperature.The resulting sintered raw material pseudo-granules are then charged into a sintering machine. It is obtained by firing. However, in the commonly used sintering machine (Dwight Lloyd type), the surface layer of the raw material grains is ignited in an ignition furnace, and air is sucked downward to burn it to the lower layer. Air permeability greatly affects the productivity of sintered ore products. Therefore, the granulation properties of the sintered raw material have been improved compared to before, and
Various methods have been studied to improve the pseudo-granulation and ensure the permeability of the raw material grain layer. As a typical example, a method is known in which fine powder ore and other ores are adhered and granulated using a so-called visiter component such as quicklime or slaked lime. However, in this method, it is necessary to add a relatively large amount of quicklime, etc., which increases the raw material cost and offsets the productivity improvement effect. In addition, quicklime generally becomes slaked lime when it comes into contact with water, and at this time it becomes hydrated and becomes coarse grained by using water as bicedar, but the coarsened slaked lime no longer has the original bicarbonate.
/ performance is lost, and it becomes difficult to produce the granulation property of sintering raw materials such as fine powder ore, that is, the pseudo-particle effect.

本発明者らは上記現状に鑑み、焼結原料の疑似粒化を容
易且つ確実に、しかも生石灰等のバインターを非常に少
量用いるのみで実施でき各造粒粒子自体構造安定性及び
機械的強度に優れ、その取扱い性は勿論焼結機への装入
後の焼結原料層の通気性を確保でき、焼結鉱の生産性、
歩留シ等を向上できる焼結原料の前処理技術を確立する
ととを目的として鋭意研究を重ねた。その結果焼結原料
の混合、調湿及び擬似粒化に当り用いられる水中に、所
定量の分散剤及び(又は)界面活性剤を添加する時には
、上記目的が達成され優れた諸特性を具備する疑似粒化
品(造粒品)が収得でき、これは焼結鉱原料として極め
て好適であるという事実を発見した。
In view of the above-mentioned current situation, the present inventors have realized that pseudo-granulation of sintered raw materials can be easily and reliably carried out using only a very small amount of binder such as quicklime, and that each granulated particle itself has structural stability and mechanical strength. Not only is it easy to handle, but it also ensures the permeability of the sintered raw material layer after charging into the sintering machine, improving the productivity of the sintered ore.
We have conducted intensive research with the aim of establishing a pretreatment technology for sintering raw materials that can improve yields and other factors. As a result, when a predetermined amount of dispersant and/or surfactant is added to the water used for mixing, humidity conditioning and pseudo-granulation of sintering raw materials, the above objectives are achieved and excellent properties are achieved. It has been discovered that a pseudo-granulated product (granulated product) can be obtained and is extremely suitable as a raw material for sintered ore.

本発明は斯かる新しい事実の発見に基づいて完成された
ものである。
The present invention was completed based on the discovery of this new fact.

即ち本発明は、焼結原料を混合、調湿して擬似粒化する
に当り、0.01−1.0重量%の濃度の分散剤及び(
又は) 0.001〜0.1重量%の濃度の界面活性剤
を含有する水を用いることを特徴とする焼結原料の前処
理方法に係る。
That is, in the present invention, a dispersant with a concentration of 0.01-1.0% by weight and (
or) A method for pretreating a sintering raw material, characterized in that water containing a surfactant at a concentration of 0.001 to 0.1% by weight is used.

本発明方法によれば、焼結鉱原料として極めて好適な諸
特性を具備する焼結原料疑似粒重を容易にしかも生石灰
等のバインターを非常に少蕾用いるのみで収得すること
ができる。本発明方法により処理して得られる疑似核晶
は、形状が安定しており、機械的強度に優れ、焼結機内
に装入した際通気性を確保でき、焼結鉱の生産性、歩留
りを顕著に向上できる。また焼結工程への搬送中に振動
を受けても粒子相互の接合及び大塊への成長が惹起され
ず、部分的に接合しても潰砕することにより容易に個々
の疑似核晶に分離でき、焼結工程上例等の支障をきたす
ことはない。更に上記疑似核晶を用いて製造される焼結
鉱は、強度が向上する。
According to the method of the present invention, it is possible to easily obtain a sintered raw material pseudo particle weight having various characteristics extremely suitable as a sintered ore raw material, and only by using a very small amount of a binder such as quicklime. The pseudonucleus obtained by the method of the present invention has a stable shape, excellent mechanical strength, and can ensure air permeability when charged into a sintering machine, improving productivity and yield of sintered ore. It can be significantly improved. In addition, even if the particles are subjected to vibration during transportation to the sintering process, they will not bond to each other or grow into large lumps, and even if they are partially bonded, they will be easily separated into individual pseudo-nuclei crystals by crushing. This method does not cause any problems in the sintering process. Furthermore, the sintered ore produced using the pseudonucleated crystals has improved strength.

本発明に従い、上記所定量の分散剤及び(又は)界面活
性剤を利用することにより、かかる優れた諸特性を具備
する焼結原料疑似粒重が収得される理由は、尚解明され
てはいないが、界面活性剤のもつ湿潤性、浸透性、濡水
性等によって、焼結原料である鉄鉱石などの被濡水性が
向上され擬似粒子化が容易になシ、また分散剤のもっ晶
癖効果(結晶成長防止効果)と分散効果(表面電位調整
による粒子間の反撥効果)によって、パイ′Jターとす
る石灰粒子の微細化が企シ得、少量のバイジターを非常
健有効に利用して焼結原料の擬似粒子化性を向上させ得
るものと考えられる。また上記分散剤等は、鉄鉱石等の
焼結原料に付着含有されている粘土等をも水中に分散さ
せ、これをバインターとして機能させる働きがある。上
記により充分に拡散されたバイジター(石灰分)は、得
られる疑似粒品中に均一に分散され、焼結時に、5i0
2等と容易迅速に反応して焼結鉱中にまんべんなく溶は
込み、焼成鉱の強度向上、生産性向上にもつながる。い
ずれにせよ本発明は、従来この種焼結原料の擬似粒化に
当り用いられた例のない分散剤及び(又は)界面活性剤
を用いて、上記優れた特性を有する疑似核晶を容易に収
得できるものであシ、その実用的価値は絶大なものであ
る。
The reason why a sintered raw material pseudo particle weight having such excellent properties is obtained by using the above-mentioned predetermined amounts of dispersant and/or surfactant according to the present invention has not yet been elucidated. However, the wettability, permeability, water wettability, etc. of surfactants improve the wettability of iron ore, which is a raw material for sintering, and facilitate the formation of pseudo-particles. (crystal growth prevention effect) and dispersion effect (repulsion effect between particles due to surface potential adjustment), it is possible to make the lime particles finer by using a small amount of vigitr effectively. It is thought that this can improve the pseudo-particulate property of the coagulating material. Further, the above-mentioned dispersant and the like have the function of dispersing clay, etc. attached to sintering raw materials such as iron ore, in water, and making it function as a binder. Visitor (lime) sufficiently diffused in the above manner is uniformly dispersed in the obtained pseudo-granules, and during sintering, 5i0
It reacts easily and quickly with the sintered ore and penetrates evenly into the sintered ore, leading to improved strength and productivity of the sintered ore. In any case, the present invention uses a dispersant and/or surfactant, which have never been used in the past for pseudo-granulation of this type of sintering raw material, to easily produce pseudo-nucleated crystals having the above-mentioned excellent properties. It is something that can be obtained, and its practical value is enormous.

本発明に利用される分散剤及び(又は)界面活性剤とし
ては、石灰及び鉄鉱石に付着する粘土を水中に分散させ
得ることを前提として、従来よシ公知の各種のものがい
ずれも使用できる。分散剤として用いられる物質の代表
例としては、例えばアクリル酸重合体、アクリル酸−ア
クリル酸メチル共重合体、アクリル酸−アクリル酸メチ
ル−アクリル酸メチルしドロオ+シアル士レート共重合
体、マレイシ酸−イソづテシ共重合体、スチレシスルホ
シ酸重合体、アクリレートースチレシスルホシ酸コポリ
マのNα、K、MHI4塩及びアマイド(平均分子量2
000〜2−0000)、ビニルじリジニウム重合体(
平均分子量1000〜5000)、ビニルイミタソリン
重合体(平均分子量1500〜7000)、ホスホシ酸
(詳しくは2−ホスホノ−1,2,4−)リカルボシ酸
、アミノトリメチレンホスホシ酸、1−しドロ+シエタ
シ−]、I−,;の代表例としては、例えば脂肪酸(C
工2.、、□8)、高級アルコール(C8〜2゜)硫酸
エステル、アル+ル(C□。〜□5)ベンt!シスルホ
シ酸、アル士ル(C3〜4)ナフタレンスルホシ酸、ナ
フタレンスルホン酸ホルマリン縮合物、シアル牛ルスル
ホコハク酸、ポリオ士シエチレシサルフエートのNα、
K又はNJIt、i、ポリオ士シエチレシアル+ル(C
□。〜2゜)エーテル(HLBB以上)、ポリオ士シエ
チレシアル士ル(C8〜9)フェノールエーテル(II
 L B 7 以上)、ポリオ士シエチレンソルピタシ
脂肪酸エステル(HLB 10以上)、ポリオ+シエチ
レシアシル(C□2〜.8)エステル(HLB8以上)
、オ十シエチレンーオ+シづロヒレシづ0ツクポリマー
(平均分子量1000〜+0000)等を例示できる。
As the dispersant and/or surfactant used in the present invention, any of the various conventionally known ones can be used, provided that the clay adhering to lime and iron ore can be dispersed in water. . Typical examples of substances used as dispersants include acrylic acid polymers, acrylic acid-methyl acrylate copolymers, acrylic acid-methyl acrylate-methyl acrylate copolymers, and maleic acid. - Nα, K, MHI4 salts and amide of isodate copolymer, styrecysulfosic acid polymer, acrylate styrecysulfosic acid copolymer (average molecular weight 2
000-2-0000), vinyl diridinium polymer (
average molecular weight 1000-5000), vinylimitasoline polymer (average molecular weight 1500-7000), phosphosic acid (specifically 2-phosphono-1,2,4-)licarbosic acid, aminotrimethylenephosphosic acid, 1- Typical examples of fatty acids (C
Engineering 2. ,,□8), higher alcohol (C8~2゜) sulfuric ester, al+ru (C□.~□5) bent! Cisulfosic acid, Al (C3-4) naphthalene sulfosic acid, naphthalene sulfonic acid formalin condensate, sialyl sulfosuccinic acid, Nα of polyoxysilyl sulfosulfate,
K or NJIt, i, Poliochemistry + Ru (C
□. ~2゜) Ether (HLBB or higher), polyester (C8-9) phenol ether (II
L B 7 or more), polyoxyethylene solpitacyl fatty acid ester (HLB 10 or more), polio+thiethylene solpitacyl (C□2-.8) ester (HLB 8 or more)
, 100 ethylene oxide + 100 ethylene oxide polymer (average molecular weight 1000 to +0000).

上記分散剤及び界面活性剤は、焼結原料の疑似粒化に用
いられる水中に、分散剤は0.01−1.0重量%、好
ましくはO,1ffi量チ前後の濃度となる量で、界面
活性剤は0.001〜0.1重量%、好ましくは0.0
1重量%前後の濃度となる量で、夫々単独で使用される
か又は併用され、これによシ木発明所期の効果を奏し得
る。特に両薬剤は併用されるのが好適である。各薬剤の
使用濃度が、上記範囲より下回る場合、2等薬剤使用に
よる効果の発現は困難である。また上記範囲を越えて用
いる場合特に弊害はないが、効果の向上は見られず経済
的でない。
The above-mentioned dispersant and surfactant are added to the water used for pseudo-granulation of the sintering raw material in an amount such that the concentration of the dispersant is 0.01-1.0% by weight, preferably around 0.1ffi. The surfactant is 0.001 to 0.1% by weight, preferably 0.0%
Each of them can be used alone or in combination in an amount to give a concentration of about 1% by weight, and the desired effect of the invention can be achieved. In particular, it is preferable to use both drugs together. When the concentration of each drug used is lower than the above range, it is difficult to express the effect of using a second grade drug. Further, if it is used beyond the above range, there is no particular adverse effect, but no improvement in the effect is seen and it is not economical.

本発明方法は、焼結原料の疑似粒化に当り、上記特定濃
度の分散剤及び(又は)界面活性剤を含む水を用いるこ
とを除き、基本的には公知の疑似粒化(造粒)と同様の
手段により実施できる。特にその際バイジターとして用
いられる石灰の量を従来に比し%以下程度に減少させて
も、同様の焼結鉱の生産性、歩留り等を確保でき、従っ
て該石灰使用量の節約即ち省資源に役立ち、また製品コ
ストを低減できる利点がある。勿論上記石灰量を従来と
同程度とする時には、一層内上された生産性、歩留りを
もって焼結製品を収得できる。本発明方法では、通常使
用される水量をも低減でき、これにより焼結時のエネル
ギーを節減することもできる。
The method of the present invention is basically a known method of pseudo-granulation (granulation), except that water containing a dispersant and/or surfactant at the above-mentioned specific concentration is used for pseudo-granulation of the sintering raw material. This can be done by the same means as. In particular, even if the amount of lime used as a bisitor is reduced to less than % compared to the conventional one, the same productivity and yield of sintered ore can be maintained, and therefore the amount of lime used can be reduced, which means resource conservation. It is useful and has the advantage of reducing product costs. Of course, when the amount of lime is kept at the same level as before, sintered products can be obtained with even higher productivity and yield. The method of the invention can also reduce the amount of water normally used, thereby saving energy during sintering.

次に実験例を挙げて本発明についてよシ具体的に説明す
る。尚各側におけるチは、重量基準によるものとする。
Next, the present invention will be explained in detail with reference to experimental examples. Note that the dimensions on each side are based on weight.

実施例 第1表に示す組成を有する鉱石を適宜組み合せ用い、こ
れに第2表に示す粒径の生石灰0.5.1.0.1.5
又は2.0%と共に下記所定濃度となる量の分散剤及び
界面活性剤とを含む水(又は比較のため同量の水のみ)
を上記鉱石に対し7%となる量で添加し、これに成品焼
結鉱が第3表に示すような成分組成となるように蛇紋岩
、硅砂及び]−クスを適π配合して、疑似粒化1〜、こ
れを焼結なべ試験に供した。
Examples: Use ores having the composition shown in Table 1 in appropriate combinations, and quicklime 0.5.1.0.1.5 having the particle size shown in Table 2.
Or water containing 2.0% and an amount of dispersant and surfactant to achieve the specified concentration below (or just the same amount of water for comparison)
was added in an amount of 7% to the above ore, and serpentinite, silica sand, and ]-cus were mixed appropriately so that the finished sintered ore had the composition shown in Table 3. Granulation 1~, this was subjected to the sintering pot test.

第  1  表 第2表 供試生石灰の粒子分布 第3表 焼結鉱組成 〈分散剤及び界面活性剤〉 試料1   アクリル酸ソータ・メタクリル酸しドロ+
シエチし一ト・アクリル酸 メチル共重合体         1000 ppmナ
フタレシスルホシ酸ホルマリシ 縮合物              100 ppm試
料2   アクリレートスチレンスルホy酸コポリマー
           1000 PPMラウリル硫酸
ナトリウム      1007)P7rL試料3  
 アクリル酸ソータ・メタクリル酸しドロ+シエチレー
ト・アクリル 酸メチル共重合体         +000p7)ノ
nポリオ士シエチしジラウリル エーテル              + o o p
pm試料4  2−ホスホノー1,2.今一トリカルボ
シ酸           + o o o ppmド
ヂシルベシゼシスルホシ酸 すトリウム            + o o pp
m試料5   アクリレート・スチしシスルホシ酸コポ
リマー            1000 ppmポリ
オ士シエチレυオレイル エーテル               100P7)
虎上記各試料(試料1〜5)及び比較のため水のみを用
いた場合につき、生石灰の添加割合の変化に伴って、得
られる焼結鉱の生産率(T/hγ・7+t2)がどのよ
うに猿化するかを求めた結果を第1図に示す。第1図中
(1)は試料1の使用を、(2)は試料2の使用を、(
3)は試料3の使用を、(4)は試料4の使用を、(5
)は試料5の使用を、寸だ(6)は試料無添加(水のみ
)使用を夫々示す。
Table 1 Table 2 Particle distribution of sample quicklime Table 3 Sintered ore composition (dispersant and surfactant) Sample 1 Acrylic acid sorter/methacrylic acid sinter +
Siethyl styrene/methyl acrylate copolymer 1000 ppm Naphthalene sulfosic acid formalic acid condensate 100 ppm Sample 2 Acrylate styrene sulfo acid copolymer 1000 PPM Sodium lauryl sulfate 1007) P7rL sample 3
Acrylic acid sorta, methacrylic acid and methacrylate + thiethylate and methyl acrylate copolymer +000p7) Non-polyoxylated dilauryl ether + o o p
pm sample 4 2-phosphono 1,2. Imaichi tricarboxylic acid + o o o ppm Thorium dodicylbecizecis sulfosyate + o o pp
m Sample 5 Acrylate/styrene oleyl ether 100P7)
How does the production rate (T/hγ・7+t2) of the resulting sintered ore change as the addition ratio of quicklime changes for each of the above samples (samples 1 to 5) and when only water is used for comparison? Figure 1 shows the results of determining whether the animal turns into an ape. In Figure 1, (1) indicates the use of sample 1, (2) indicates the use of sample 2, (
3) uses sample 3, (4) uses sample 4, (5
) indicates the use of sample 5, and (6) indicates the use of no sample (only water).

第1図より本発明方法によれば、いずれの場合も顕著に
焼結鉱の生産率を向上できることが明らかである。
From FIG. 1, it is clear that according to the method of the present invention, the production rate of sintered ore can be significantly improved in any case.

また上記試験において、試料lを用いた場合の歩留を求
めた結果を第2図に示す。図中(1)は試料1を用いた
時の結果であり、(6)は比較として試料無添加(水の
み)の時の結果を示す。
Further, in the above test, the yield obtained when Sample 1 was used is shown in FIG. 2. In the figure, (1) shows the results when Sample 1 was used, and (6) shows the results when no sample was added (only water) for comparison.

該第2図から、本発明方法によれば歩留も亦上記生産率
と同様に顕著に向上できることが判る。
From FIG. 2, it can be seen that according to the method of the present invention, the yield can be significantly improved as well as the above-mentioned production rate.

更に上記試験において試料Iとして用いたと同の生産率
(T/hr −m” )を求めた。その結果は第3図に
示す通シであった。
Furthermore, the same production rate (T/hr - m") as used for Sample I in the above test was determined. The results were as shown in FIG.

実施例 鉱石の疑似粒化性に重大な影響を与える、鉱石表面の被
濡水性(吸水性)を試験した。即ち上記試料】に示す分
散剤及び界面活性剤を含む水と、之等を含まない水とを
供試水として用い、之等の夫々につき各種銘柄の鉱石を
浸透法(JIS  M8.105等に準する方法)によ
り試験した。用いた鉱石銘柄は夫々次の通りである。
Example The water wettability (water absorption) of the ore surface, which has a significant effect on the pseudo-granulation property of the ore, was tested. That is, water containing the dispersant and surfactant shown in [the above sample] and water not containing the above were used as test water, and various brands of ore were applied to each of the above by the infiltration method (JIS M8.105, etc.). The test was conducted using a method similar to the above. The ore brands used are as follows.

a・・・・・・マウシトニューマシ h・・・・・・ローづリバー C・・・・・・フオーメシト d・・・・・・サンタバーバラ 結果を第4図に示す。第4図中(W−1)は上記aの鉱
石を試料1を含む水(試験水)にて試験した場合を、及
び(a−2)は同磁石を試料1無添加水(対照水)にて
試験した場合を夫々示す。
a...Mausitonewmash h...Raw River C...Formecit d...Santa Barbara The results are shown in Figure 4. In Figure 4, (W-1) shows the case where the above ore a was tested in water containing sample 1 (test water), and (a-2) shows the case where the same magnet was tested with sample 1-free water (control water). The cases tested are shown below.

以下同様に(b−1)は鉱石りを試験水に、(b−2)
は鉱石すを対照水に、(C−])は鉱石Cを試験水に、
(C−2)は鉱石Cを対照水に、(d、−1)は鉱石d
を試験水に、(d−2)は鉱石dを対照水にて夫々試験
した場合を示す。
Similarly, (b-1) uses ore slag as the test water, and (b-2)
(C-]) uses ore C as control water, (C-]) uses ore C as test water,
(C-2) uses ore C as control water, (d, -1) uses ore d
(d-2) shows the case in which Ore d was tested in test water, and Ore d was tested in control water.

第4図より本発明に用いる分散剤及び界面活性剤を含む
水は、いずれの鉱石に対してもその吸水性(被濡水性)
を顕著に向上させることが明らかである。
From Figure 4, the water containing the dispersant and surfactant used in the present invention has a water absorbency (wetting property) for any ore.
It is clear that this significantly improves

実施例 下記第4表に示す鉱石100部に石灰石、珪石及びコー
クスの所定量を混合して焼結原料混合物各添加剤を含む
水を用いて得られた造粒品を、] 700 mx il
:aoの負圧下の試験鋼にて焼結して、焼結鉱を製造し
た。その時の生産率、焼結時間、成品歩留及び焼結鉱製
品の落下強度を求めた結果は、下記第6表の通りであっ
た。尚第6表には比較のため伺ら分散剤及び界面活性剤
を含1ない水のみを用いて同様にして得られた造粒品を
用いた結果を併記する。尚この比較例においては、前記
第4表に示す組成の焼結原料混合物では造粒困難なため
、石灰石配合量を11部に代えた焼結原料混合物を用い
た。
Example A granulated product was obtained by mixing 100 parts of the ore shown in Table 4 below with predetermined amounts of limestone, silica stone, and coke and using water containing each additive as a sintering raw material mixture.] 700 mx il
: Sintered ore was produced by sintering with test steel under negative pressure of AO. The results of determining the production rate, sintering time, product yield, and falling strength of the sintered ore products at that time are shown in Table 6 below. For comparison, Table 6 also shows the results using granulated products obtained in the same manner using only water containing no dispersant or surfactant. In this comparative example, since granulation was difficult with the sintering raw material mixture having the composition shown in Table 4, a sintering raw material mixture in which the limestone content was changed to 11 parts was used.

第  6  表 上記第6表より本発明方法により造粒された焼結原料混
合物を用いる時には、成品歩留の向上により、生産性が
アップでき、また生石灰を低減でき、更に水量をも低減
でき、工業的に非常に有利であることが判る。
Table 6 From Table 6 above, when using the sintered raw material mixture granulated by the method of the present invention, productivity can be increased by improving the product yield, and quicklime can be reduced, and the amount of water can also be reduced. It turns out that it is very advantageous industrially.

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

第1図は生石灰添加割合と生産率との関係を示す図、第
2図は生石灰添加割合と歩留との関係を示す図、第3図
は分散剤及び界面活性剤の添加量と生産率との関係を示
す図、並びに第4図は各種鉱石の吸水性試験結果を示す
図である。 (以 上) 第1「、1 第2図 164− 第3図 第4図 手続補正書輸発) 昭和57年12月13日 特許庁長官  若杉和夫   殿 1、事件の表示 昭和57年特 許 願第160175  号2、発明の
名称 焼結原料の前処理方法 3、補正をする者 事件との関係  特許出願人 新日本製作ズ株式会社 (ほか2名) 4、代理人 大阪市東区平野町2の10平和ビル内電話06−203
−0941(代)5、補正命令の日付        
         1−f自発 6、補正により増加する発明の数 別紙添附の通り 補  正  の  内  谷 (υ 明#lI書中の記載を下記正諒表の通シ訂正する
。 (2)第1図及び第3図を夫々別紙の通シ訂正する。 C以 上)
Figure 1 shows the relationship between quicklime addition ratio and production rate, Figure 2 shows the relationship between quicklime addition ratio and yield, and Figure 3 shows the addition amount of dispersant and surfactant and production rate. FIG. 4 is a diagram showing the results of a water absorption test of various ores. (Above) No. 1, 1 Figure 2 164 - Figure 3 Figure 4 Procedural amendments exported) December 13, 1980 Commissioner of the Japan Patent Office Kazuo Wakasugi 1. Indication of the case 1988 Patent application No. 160175 No. 2, Name of the invention: Pretreatment method for sintered raw materials 3, Relationship with the person making the amendment Patent applicant: Shin Nippon Manufacturing Co., Ltd. (and 2 others) 4: Agent: 2, Hirano-cho, Higashi-ku, Osaka City 10 Heiwa Building phone number 06-203
-0941 (generation) 5, date of correction order
1-f Spontaneous 6. The number of inventions to be increased by the amendment. As shown in the attached sheet, the description in the amendment is corrected in the following official note. (2) Figures 1 and 1 Correct the three figures in separate sheets. (C and above)

Claims (1)

【特許請求の範囲】[Claims] ■ 焼結原料を混合、調湿して疑似粒化するに当シ、0
.0 + −1,0重量%の濃度の分散剤及び(又は)
 0.001〜0,1重量%の濃度の界面活性剤を含有
する水を用いることを特徴とする焼結原料の前処理方法
■ When mixing and humidity controlling the sintering raw materials to make them into pseudo-granules,
.. Dispersant and/or at a concentration of 0 + -1,0% by weight
A method for pretreating sintering raw materials, characterized in that water containing a surfactant at a concentration of 0.001 to 0.1% by weight is used.
JP16017582A 1982-09-14 1982-09-14 Pretreatment of starting material for sintering Pending JPS5950129A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16017582A JPS5950129A (en) 1982-09-14 1982-09-14 Pretreatment of starting material for sintering

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16017582A JPS5950129A (en) 1982-09-14 1982-09-14 Pretreatment of starting material for sintering

Publications (1)

Publication Number Publication Date
JPS5950129A true JPS5950129A (en) 1984-03-23

Family

ID=15709465

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16017582A Pending JPS5950129A (en) 1982-09-14 1982-09-14 Pretreatment of starting material for sintering

Country Status (1)

Country Link
JP (1) JPS5950129A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002066688A1 (en) * 2001-02-22 2002-08-29 Nippon Steel Corporation Method of granulation treatment of raw material for iron making and granulation treatment agent for iron making
JP2003155524A (en) * 2001-09-07 2003-05-30 Nippon Steel Corp Granulation treatment agent for ironmaking, and granulation treatment method using the same
JP2003239023A (en) * 2002-02-14 2003-08-27 Nippon Steel Corp Method for pelletizing iron making raw material
EP2548978A1 (en) * 2011-07-21 2013-01-23 Clariant S.A., Brazil Binder composition for the agglomeration of fine minerals and pelletizing process using the same
JP2013170307A (en) * 2012-02-22 2013-09-02 Nippon Steel & Sumitomo Metal Corp Method for granulating iron-making dust or mixture of iron-making dust and iron ore fine and granulated substance

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002066688A1 (en) * 2001-02-22 2002-08-29 Nippon Steel Corporation Method of granulation treatment of raw material for iron making and granulation treatment agent for iron making
EP1367141A1 (en) * 2001-02-22 2003-12-03 Nippon Steel Corporation Method of granulation treatment of raw material for iron making and granulation treatment agent for iron making
AU2002233659B2 (en) * 2001-02-22 2004-07-22 Nippon Shokubai Co., Ltd. Method of granulation treatment of raw material for iron making and granulation treatment agent for iron making
EP1367141A4 (en) * 2001-02-22 2007-08-22 Nippon Steel Corp Method of granulation treatment of raw material for iron making and granulation treatment agent for iron making
JP2003155524A (en) * 2001-09-07 2003-05-30 Nippon Steel Corp Granulation treatment agent for ironmaking, and granulation treatment method using the same
JP2003239023A (en) * 2002-02-14 2003-08-27 Nippon Steel Corp Method for pelletizing iron making raw material
EP2548978A1 (en) * 2011-07-21 2013-01-23 Clariant S.A., Brazil Binder composition for the agglomeration of fine minerals and pelletizing process using the same
WO2013010629A1 (en) * 2011-07-21 2013-01-24 Clariant International Ltd Binder composition for agglomeration of fine minerals and pelletizing process
AU2012286206A1 (en) * 2011-07-21 2013-12-12 Clariant International Ltd Binder composition for agglomeration of fine minerals and pelletizing process
JP2014521831A (en) * 2011-07-21 2014-08-28 クラリアント・ファイナンス・(ビーブイアイ)・リミテッド Binder composition for agglomerating fine minerals and pelletizing method
EP2734653B1 (en) 2011-07-21 2015-12-09 Clariant International Ltd Binder composition for agglomeration of fine minerals and pelletizing process
AU2012286206B2 (en) * 2011-07-21 2016-12-08 Clariant International Ltd Binder composition for agglomeration of fine minerals and pelletizing process
AU2012286206C1 (en) * 2011-07-21 2017-09-07 Clariant International Ltd Binder composition for agglomeration of fine minerals and pelletizing process
US11124855B2 (en) 2011-07-21 2021-09-21 Clariant International Ltd. Binder composition for the agglomeration of fine minerals and pelletizing process
JP2013170307A (en) * 2012-02-22 2013-09-02 Nippon Steel & Sumitomo Metal Corp Method for granulating iron-making dust or mixture of iron-making dust and iron ore fine and granulated substance

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