JPH0310026A - Clayey Ni ore briquetting method - Google Patents
Clayey Ni ore briquetting methodInfo
- Publication number
- JPH0310026A JPH0310026A JP14289389A JP14289389A JPH0310026A JP H0310026 A JPH0310026 A JP H0310026A JP 14289389 A JP14289389 A JP 14289389A JP 14289389 A JP14289389 A JP 14289389A JP H0310026 A JPH0310026 A JP H0310026A
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- ore
- briquette
- raw material
- moisture content
- strength
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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】
〔産業上の利用分野〕
この発明は、粘土質NiK石の団鉱方法に関し、とくに
酸化Ni鉱石などを製錬してフェロニッケルを製造する
際の製団工程において、団鉱機(以下、これを「ブリケ
ットマシン」という)に供給する団鉱原料を、粘土骨な
らびに水分に着目して調整する新規な技術について提案
するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a briquetting method for clayey NiK stone, particularly in the briquetting process when producing ferronickel by smelting Ni oxide ore, etc. This paper proposes a new technology for adjusting the briquette raw material supplied to a briquette machine (hereinafter referred to as a "briquette machine") by focusing on clay bones and moisture.
一般に、オーステナイト系ステンレス鋼の製造に際して
用いられるNi (フェロニッケル)は、ガーニライト
などの珪酸Ni鉱石などを製錬して製造している。この
酸化Ni鉱石は粘性湿鉱石であり、多量の水分を含んで
いることから、通常、次のようにして製錬している。Generally, Ni (ferronickel) used in the production of austenitic stainless steel is produced by smelting Ni silicate ore such as garnilite. Since this Ni oxide ore is a viscous wet ore and contains a large amount of water, it is usually smelted as follows.
すなわち、全湿式法と呼ばれる方法は、まず、鉱石、炭
材、石灰石等の主原料ならびに副原料にそれぞれ多量の
水を添加して個別的にスラリー状として湿式粉砕し、そ
の後、これらの原料を混合し、この混合材料を脱水して
から、ベレットその他に製団する。その後、この製団物
を、例えばグレート式ロータリーキルン中に装入し、乾
燥、予熱、焼成することにより、Niなどの金属分を還
元すると共にルフペとして成長させた後、タリン力−と
して排出し、その後の処理によって、このタリンカーか
らフェロニッケルなどの合金鉄とする方法である。In other words, in the method called the all-wet method, first, a large amount of water is added to each of the main raw materials and auxiliary raw materials such as ore, carbonaceous material, and limestone, and each is wet-pulverized into a slurry form, and then these raw materials are The mixed material is dehydrated and formed into pellets or the like. Thereafter, this pellet is charged into, for example, a grate type rotary kiln, and is dried, preheated, and fired to reduce metals such as Ni and grow as a rufupe, and then discharged as a talin powder. Through subsequent processing, this talincar is made into a ferroalloy such as ferronickel.
しかしながら、この方法だと、主原料ならびに副原料に
多量の水分を添加し、スラリー状としてドラムフィルタ
等で水分を除去しているため、脱水が十分でなく、さら
に混合は各原料をスラリー状態で行うため、均一に原料
を混合することがむづかしく、とくに比重差の大きい炭
材を大量かつ均一に分散混合することがきわめてむづか
しいのが実情であった。However, with this method, a large amount of water is added to the main raw material and auxiliary raw materials, and the water is removed in the form of a slurry using a drum filter, etc., so dehydration is not sufficient, and furthermore, each raw material is mixed in a slurry state. Because of this, it is difficult to uniformly mix raw materials, and in particular, it is extremely difficult to uniformly disperse and mix large amounts of carbonaceous materials with large differences in specific gravity.
これに対し、このような欠点を克服すべく本出願人は、
先に特開昭62−23944号公報において、主原料の
酸化Ni鉱石を脱水性の良否によって2つに分け、その
うちの一方、つまり、脱水性が悪い鉱石は乾燥粉砕工程
を経て粉砕し、他方の鉱石、つまり、脱水性が良好な鉱
石を湿式粉砕工程を経て粉砕して混合原料を調整すると
いう方法を提案した。In order to overcome this drawback, the present applicant has
Previously, in Japanese Patent Application Laid-Open No. 62-23944, Ni oxide ore, which is the main raw material, is divided into two parts depending on the quality of dehydration. One of the ores, that is, the ore with poor dehydration properties, is pulverized through a dry pulverization process, and the other is We proposed a method in which a mixed raw material is prepared by pulverizing ore, that is, ore with good dewatering properties, through a wet pulverization process.
以下に、この先行提案にかかる技術を説明する。The technology related to this prior proposal will be explained below.
乾燥粉砕工程は、鉱石を乾燥状態で粉砕する工程で、鉱
石は通常径211内外程度に粉砕できれば何れにも構成
できるが、通常は、第1図に示す如く、自生粉砕ミル等
の摩砕機l、サイクロン2ならびにバッグフィルタ3を
連結して構成し、なかでも、摩砕機lには熱風炉4から
乾燥空気が送られている。従って、鉱石の一部は、通常
25〜40%程度の水を含みかつ径−300w程度であ
るが、ボールミル等の摩砕機l内で乾燥状態で粉砕され
、粒度−2鶴程度に調整すると共に水分10%以下程度
に乾燥される。The dry crushing process is a process of crushing ore in a dry state, and it can be configured in any way as long as the ore can be crushed into a diameter of about 211mm, but usually, as shown in FIG. , a cyclone 2 and a bag filter 3 are connected to each other, and dry air is sent from a hot blast furnace 4 to the attritor 1. Therefore, a part of the ore usually contains about 25 to 40% water and has a diameter of about -300 W, but it is ground in a dry state in a grinder such as a ball mill, and the particle size is adjusted to about -2 Tsuru. It is dried to a moisture content of less than 10%.
一方、湿式粉砕工程は、脱水性の良い鉱石をスラリー状
に処理する工程であって、通常は第1図に示す如く、湿
式チューブミル5、複数個のスラリータンク6から構成
し、これにドラムフィルタ7を連結する。つまり、脱水
性の良い鉱石(これにも通常20〜30%の水分を含み
、粒径も一300鰭程度である)には水分を添加して湿
式チューブミル5で粉砕し、水分50%程度を含むスラ
リーとし、このスラリーは一時的にスラリータンク6に
ストックされ、その後、順次にドラムフィルタ7で水分
28〜35%程度まで脱水し、ケーク状にする。On the other hand, the wet crushing process is a process of processing ore into a slurry with good dewatering properties, and usually consists of a wet tube mill 5, a plurality of slurry tanks 6, and a drum as shown in FIG. Connect the filter 7. In other words, ore with good dehydration properties (usually contains 20 to 30% water and has a particle size of about 1,300 fins) is milled with water in a wet tube mill 5, with a water content of about 50%. This slurry is temporarily stocked in a slurry tank 6, and then sequentially dehydrated in a drum filter 7 to a moisture content of about 28 to 35% and made into a cake.
次に、−2m程度の粒度に調整された各原料は、混合混
練工程において適当量ずつ混合し混練する。Next, each raw material adjusted to a particle size of about -2 m is mixed and kneaded in appropriate amounts in a mixing and kneading step.
この際の各原料の水分は、ブリケットの圧壊強度や後工
程の乾燥、予熱の熱エネルギーの節減等から10〜20
%、好ましくは15〜20%とする。The moisture content of each raw material at this time is 10 to 20% due to the crushing strength of the briquettes, drying in the post-process, and saving of thermal energy for preheating.
%, preferably 15 to 20%.
すなわち、後の製団工程において、ブリケット等の製団
物の強度を大きくするには、ある程度の水分が必要であ
り、一方、この水分量があまり多いと、製団性が損なわ
れるほか、予熱乾燥時に多量の熱エネルギーが必要で、
還元焼成時の排ガスによって十分に乾燥できないことも
あり、この点から上限は20%程度になる。In other words, a certain amount of moisture is required to increase the strength of the briquettes and other briquettes in the subsequent dough-making process.On the other hand, if this moisture content is too large, the dough-making properties will be impaired and the preheating process will be too high. Drying requires a large amount of thermal energy,
Sufficient drying may not be possible due to the exhaust gas during reduction firing, and from this point of view the upper limit is about 20%.
従来、混合原料は、主としてブリケットの成形性のみか
ら定性的に水分調整をしていたが、原料の混合特性やブ
リケットの強度に着目した場合、上述したような単純な
水分調整だけでは不十分なことが判った。Conventionally, the moisture content of mixed raw materials has been qualitatively adjusted mainly based on the moldability of the briquettes, but when focusing on the mixing characteristics of the raw materials and the strength of the briquettes, it has become clear that the simple moisture adjustment described above is not enough. It turned out that.
第2図は、各種の銘柄の鉱石の水分と圧壊強度との関係
を示すものである。この図から判るように、圧壊強度は
水分が低い程強くなるという点で、どの原料も同じ傾向
をもつことが明白である。FIG. 2 shows the relationship between moisture content and crushing strength of various brands of ore. As can be seen from this figure, it is clear that all raw materials have the same tendency, in that the lower the moisture content, the stronger the compressive strength.
しかしながら、原料の種類(銘柄)によっては、所期の
団鉱強度とするための望ましい適性水分の範囲というの
に著しい差があることが判り、水分コントロールは事実
上困難が多かった。However, it has been found that depending on the type (brand) of the raw material, there are significant differences in the desirable range of suitable moisture content for achieving the desired briquette strength, and moisture control has been difficult in practice.
本発明の目的は、こうした所期の団鉱強度を得るのに適
した混合原料が調整できないために、望ましい団鉱が製
造できないという従来技術の欠点を克服することができ
る技術を提案するところにある。The purpose of the present invention is to propose a technique that can overcome the drawbacks of the prior art in that a desired briquette cannot be produced because a mixed raw material suitable for obtaining the desired briquette strength cannot be adjusted. be.
上述の如き斯界技術の事情に鑑み、本発明では、圧壊強
度が安定しており、成形性(団鉱化)の優れた方法とし
て、
脱水性に応じて乾式もしくは湿式処理した粘土質Ni絋
鉱の粉を、所期の団鉱強度を得るのに必要な水分にすべ
く適量づつ混合調整し、このように水分調整された混合
原料を団鉱機を介して製団する方法において、
団鉱機に供給する前記混合原料の水分量を、混合する前
記鉱石のもつ平均粘土分に応じて調整し、かつこの混合
原料を十分混練養生させることにより均質化を図った後
製団することを特徴とする粘土質Ni鉱石の団鉱方法、
を提案する。In view of the above-mentioned state of the art, in the present invention, as a method with stable crushing strength and excellent formability (briquette formation), clayey Ni ore is processed dry or wet depending on the dewaterability. In the method, the powder is mixed and adjusted in an appropriate amount to have the moisture content necessary to obtain the desired briquette strength, and the mixed raw material with the moisture content adjusted in this way is made into briquettes using a briquette machine. The water content of the mixed raw material supplied to the machine is adjusted according to the average clay content of the ore to be mixed, and the mixed raw material is sufficiently kneaded and cured to homogenize it before making the dough. We propose a method for briquetting clayey Ni ore.
上記団鉱方法において、制御すべき混合主原料の水分量
は粘土分が高い程拡大するが、好ましい粘土分は各種の
鉱石を配合した状態において50%以上の粘土分が必要
である。In the above briquette method, the water content of the mixed main raw materials to be controlled increases as the clay content increases, but the preferred clay content is 50% or more when various ores are mixed.
一般に、団鉱の結合力は、バインダーを使うものの場合
は化学的結合力、また焼成、熱間団鉱を行うものの場合
は溶融による結合力が問題となる。In general, the bonding strength of briquettes is the chemical bonding force when a binder is used, and the bonding force due to melting when firing or hot briquettes are used.
これに対して、本発明のように、常温で単に加圧力のみ
によって成形する場合は、物理化学的結合力、すなわち
加圧により粒子間距離を縮めることにより粒子間引力を
増加させて結合力を得る。このような物理化学的結合力
は、原料粒度や圧縮力はもちろん、水分が重要なファク
ターとなるが、本発明者らが知見したところによれば、
鉱石、主としてガーニライト(珪苦ニッケル鉱)のよう
な粘土質Ni鉱石の場合、とりわけその鉱石の粘土分が
重要であることが判った。なおここで、鉱石の粘土分は
JIS A 1204あるいはJTS Z 2601の
鋳物砂の粘土分試験方法に基づいて求められる数値であ
る。On the other hand, when molding is performed simply by applying pressure at room temperature as in the present invention, the bonding force is increased by increasing the physicochemical bonding force, that is, the attractive force between particles by shortening the distance between particles by applying pressure. obtain. For such physicochemical bonding strength, moisture is an important factor as well as raw material particle size and compression force, but according to the findings of the present inventors,
In the case of ores, primarily clayey Ni ores such as garnilite (siliceous nickelite), it has been found that the clay content of the ore is particularly important. Note that the clay content of the ore is a value determined based on the clay content testing method for foundry sand of JIS A 1204 or JTS Z 2601.
何故なら、水分が団鉱強度に及ぼす影響は、第3図から
判るように、鉱石銘柄に応じて大きく変化し、同じレベ
ル、例えば17%の水分が常に適正なものとは言えない
のである。すなわち、同図のチオでは成形不能となり、
一方、成形の可能なナケチとボマラ、リオツバを比較す
ると後者の方が圧壊強度は高くなり、それぞれに適性値
は変化するのである。従って、最終的な目標団鉱強度を
得ようとすると、水分以外で、あるいはこの水分ととも
に他のパラメータで団鉱原料を調整しなければならない
ことが判る。This is because, as can be seen from Figure 3, the influence of moisture on briquette strength varies greatly depending on the brand of ore, and the same level of moisture, for example 17%, cannot always be said to be appropriate. In other words, the thio shown in the same figure cannot be molded,
On the other hand, when comparing Nakechi, Bomara, and Riotsuba, which can be molded, the latter has a higher crushing strength, and the appropriate value changes for each. Therefore, in order to obtain the final target briquette strength, it is found that the briquette raw material must be adjusted with other parameters other than or in addition to the moisture content.
そこで、鉱石の粘土分と適性水分との関係を団鉱強度と
して圧壊強度について調べ、適性水分の定量化について
考察した。Therefore, we investigated the relationship between the clay content and suitable moisture content of the ore, using the briquette strength as the crushing strength, and considered quantifying the suitable moisture content.
実験は、我々が得た下記第1表に示すような化学組成の
−211のチオ、ナケチ、ボマラ、リオツバの4種類の
鉱石を選び、これにやはり−2flの炭材1石灰石、ダ
ストを配合して所定量の水を加え、15%から23%ま
での各種団鉱水分試料を作成し、かかる湿潤試料を、−
度2.40の篩でこした後、ブレンド操作を加えつつ、
3日間養生し、その後3Lの荷重を与えながら40關φ
X20mmの団鉱に成形した。これを圧壊強度テストに
供した。For the experiment, we selected four types of ores - thio, nakechi, bomala, and riotuba, with chemical compositions as shown in Table 1 below, which we had obtained, and mixed them with -2 fl of carbonaceous material 1 limestone and dust. A predetermined amount of water is added to prepare various briquette moisture samples ranging from 15% to 23%, and the wet samples are -
After straining through a 2.40 degree sieve, while adding a blending operation,
After curing for 3 days, it was heated to 40mm while applying a load of 3L.
It was formed into a briquette of 20mm x 20mm. This was subjected to a crushing strength test.
圧壊強度テストの結果はすでに第2図として示した。圧
壊強度は、秤の関係で30kgまでしか測定できなかっ
たが、前記ポマラ鉱、リオツバ鉱については低水分側に
おいてスケールオーバーが認められたものの、いずれの
銘柄も高水分になる程強度の低下傾向を示し、特に低粘
土扮鉱は全体に強度が低く、しかもかなり低水分側から
団鉱成形時に水の滲出が認められ(図中X印をもって表
示)、こうした団鉱は9〜10kg以下の極めて弱い団
鉱となることが判った。The results of the crushing strength test are already shown in Figure 2. The crushing strength could only be measured up to 30 kg due to the scale, but although scale over was observed for the Pomalaite and Riotubaite on the low moisture side, the strength of all brands tended to decrease as the moisture content increased. In particular, low-clay briquettes have low overall strength, and water oozes out during briquette formation from the considerably low moisture side (indicated by the X mark in the figure). It turned out to be a weak briquette.
以上の結果から、団鉱の圧壊強度については、原料中の
水の存在状態が大きな影響を与えることが判った。すな
わち、原料粒子間に遊離水が現れるようになると団鉱強
度は著しく減少する。これは、遊離水が存在すると、団
鉱構成粒子が水を潤滑剤として動き易くなるためと考え
られる。From the above results, it was found that the presence of water in the raw material has a large effect on the crushing strength of briquettes. That is, when free water appears between raw material particles, the briquette strength decreases significantly. This is thought to be because the presence of free water makes it easier for the briquette constituent particles to move using water as a lubricant.
こうした遊離水については、鉱種により現われ易いもの
と、現われづらいものとがあり、それは鉱石の粘土分に
関係していることを本発明者らはつきとめた。すなわち
、試料鉱石を一1OOメツシュに粉砕し、その粘土分と
遊離水の有無を調べた結果を第3図に示したが、団鉱強
度を上げるためには少なくとも図中実線で示されるより
も以下に原料水分を抑えるべきことが判る。このことは
、例えば団鉱水分として18%を選んだ場合、原料鉱石
の一100メツシュ標準試料の粘土分は約55%以上を
確保することが必要となる。The present inventors have found that such free water is more likely to appear depending on the type of ore, while others are less likely to appear, and that this is related to the clay content of the ore. In other words, the results of pulverizing the sample ore to 1100 mesh and examining the presence of clay content and free water are shown in Figure 3. In order to increase the briquette strength, at least more than the solid line in the figure is required. It is clear from the following that the moisture content of raw materials should be suppressed. This means that, for example, if 18% is selected as the briquette moisture content, it is necessary to ensure that the clay content of the 1,100-mesh standard sample of raw material ore is approximately 55% or more.
なお、各種鉱石とも低水分試料(<14%)については
、団鉱成形時、鋳型への原料のかみ込みが認められた。In addition, for the low moisture samples (<14%) of various ores, it was observed that the raw materials were caught in the mold during briquette molding.
また、鉱石の粘土分が多くなり過ぎても、逆に原料は鋳
型に居着き易くなるので、上限は80%程度と考えられ
る。Furthermore, even if the clay content of the ore becomes too large, the raw material tends to stick to the mold, so the upper limit is thought to be about 80%.
以上説明したように、目標の団鉱強度を得るための粘土
分と水分との関係は第3図に示すとおりであり、この図
の実線で囲む範囲内において原料の適性水分を決定すれ
ば、望ましい団鉱が可能となる。As explained above, the relationship between clay content and moisture to obtain the target briquette strength is as shown in Figure 3, and if the appropriate moisture content of the raw material is determined within the range surrounded by the solid line in this figure, Desirable briquettes are possible.
次に、本発明はブリケットマシンに供給する混合原料に
ついては、混練養生させて均質化を図ることが必要であ
る。なぜなら、本発明の場合、鉱石の脱水性に応じて湿
式処理のものと乾式処理のものと併せた半乾式で原料処
理をしているために、混合すべき前記混合原料の水分が
著しく異なり、短時間では均一混合が困難だからである
。Next, in the present invention, it is necessary to knead and cure the mixed raw materials supplied to the briquette machine to make them homogeneous. This is because, in the case of the present invention, raw materials are processed using a semi-dry method, including wet processing and dry processing, depending on the dehydration properties of the ore, so the moisture content of the mixed raw materials to be mixed is significantly different. This is because uniform mixing is difficult in a short time.
その解決のために本発明では、混合時間を長時間かける
か、ロッドミルの負荷を大きくすることにより十分に混
練養生し、混合原料の均質化を図ることとした。In order to solve this problem, the present invention attempts to homogenize the mixed raw materials by sufficiently kneading and curing them by increasing the mixing time or by increasing the load of the rod mill.
すなわち、混合混練工程では、上述したように、主原料
の他に多量の炭材を配合し、しかも、水分は上記の如く
調整するが、その上で、これらの混合原料は均一に分散
させる必要がある。すなわち、原料の混練後、径20〜
30fl程度のとロー型又はアーモンド型ブリケットに
製団するが、このとき水分および内装原料が不均一に存
在すると、ブリケット強度の低下を招来する。このため
、混練は従来例に比べてさらに混練する必要がある。こ
の点から、本発明法では、第1図に示す如く、パグミル
等の混合機10とロッドミル等の混練機11とを直列に
結合する。このように予めパグミル等の混合機10で混
合してから、ロッドミル等の混練機11で僅かに粗砕す
ると同時に混練すると、すでに破砕された各原料中の粒
子はロッドミル等の混練機11による粗砕によって更に
調粒されると共に、均一に攪拌混練され、水分及び炭材
は均一に分散し、製団性が高められる。That is, in the mixing and kneading process, as mentioned above, a large amount of carbonaceous material is blended in addition to the main raw materials, and the moisture content is adjusted as described above, but on top of that, these mixed raw materials need to be uniformly dispersed. There is. That is, after kneading the raw materials, the diameter is 20~
The briquettes are made into raw or almond-shaped briquettes of about 30 fl, but if moisture and interior materials are unevenly present at this time, the strength of the briquettes decreases. Therefore, it is necessary to perform further kneading than in the conventional example. From this point of view, in the method of the present invention, as shown in FIG. 1, a mixer 10 such as a pug mill and a kneader 11 such as a rod mill are connected in series. If the raw materials are mixed in advance in the mixer 10 such as a pug mill and then slightly crushed and kneaded in the kneader 11 such as a rod mill, the particles in each raw material that have already been crushed will be crushed by the kneader 11 such as a rod mill. The particles are further refined by crushing, and the mixture is stirred and kneaded uniformly, so that water and carbonaceous materials are uniformly dispersed, and the granulation properties are improved.
なお、均一に混練された混線材料は一時的に原料ヤード
12にストックされ、所要に応じて次の製団工程に送ら
れる。Note that the uniformly kneaded mixed wire material is temporarily stocked in the raw material yard 12 and sent to the next making process as required.
第1表に示す各鉱石を、第2表に示す配合割合で混合し
た主原料に対し、副原料として炭材を5〜15wt%、
石灰石粉を6〜10IAlt%、その他、戻りダストl
O〜20−L%を加えた団鉱原料を調整した。5 to 15 wt% of carbonaceous material is added as an auxiliary raw material to the main raw material obtained by mixing each of the ores shown in Table 1 in the proportions shown in Table 2.
Limestone powder 6-10Alt%, other return dust l
A briquette feedstock containing O~20-L% was prepared.
この団鉱原料を、ブリケットマシン(能力27t/l1
r)にて、ゲート開度50〜1501m、ロールクリア
ランス1〜41m、ロール加圧力80〜150 Kg/
cm”、ロール回転速度10〜15rpmで製団した。This briquette raw material is processed using a briquette machine (capacity 27t/l1).
r), gate opening 50-1501m, roll clearance 1-41m, roll pressure 80-150 Kg/
cm" and roll rotation speed of 10 to 15 rpm.
その結果を第3表に示す。The results are shown in Table 3.
第3表
この結果から判るように、満足のゆく強度をもったブリ
ケットが高歩留りで得られた。Table 3 As can be seen from the results, briquettes with satisfactory strength were obtained at a high yield.
以上説明したように本発明によれば、団鉱強度を常に一
定以上に制御でき、成形歩留まりが向上し、とりわけ成
形不能や粉化を著しく少なくすることができるので、焼
成炉(キルン)の操業が安定する。As explained above, according to the present invention, the briquette strength can always be controlled above a certain level, the molding yield can be improved, and in particular, the unmoldability and powdering can be significantly reduced, so that the kiln operation can be improved. becomes stable.
第1図は、本発明方法を実施する際のフローシート、
第2図は、団鉱原料の水分含有量と圧壊強度との関係を
示すグラフ、
第3図は、団鉱の水分含有量と粘土粉ならびに団鉱強度
との関係を示すグラフである。
l・・・摩砕機、2・・・サイクロン、3・・・バッグ
フィルタ、4・・・熱風炉、5・・・湿式チューブミル
、6・・・スラリータンク、7・・・ドラムフィルタ、
8・・・ロッドミル、 3′、9・・・貯蔵槽、lO・
・・混合機、 11・・・混練機、 12・・・原料ヤ
ード、13・・・グレード、13’・・・製団機、14
・・・排鉱シュート、15・・・ロータリーキルン、1
6・・・バーナ。Figure 1 is a flow sheet for carrying out the method of the present invention, Figure 2 is a graph showing the relationship between the moisture content of briquette raw materials and crushing strength, and Figure 3 is a graph showing the relationship between moisture content and crushing strength of briquette raw materials. It is a graph showing the relationship between clay powder and briquette strength. l... Attritor, 2... Cyclone, 3... Bag filter, 4... Hot stove, 5... Wet tube mill, 6... Slurry tank, 7... Drum filter,
8...Rod mill, 3', 9...Storage tank, lO・
...Mixer, 11...Kneading machine, 12...Raw material yard, 13...Grade, 13'...Dumpling machine, 14
...Ore discharge chute, 15...Rotary kiln, 1
6...Burna.
Claims (1)
i鉱石の粉を、所期の団鉱強度を得るのに必要な水分に
すべく適量づつ混合調整し、このように水分調整された
混合原料を団鉱機を介して製団する方法において、 団鉱機に供給する前記混合原料の水分量を、混合する前
記鉱石のもつ平均粘土分に応じて調整し、かつこの混合
原料を混練養生させることにより均質化を図った後製団
することを特徴とする粘土質Ni鉱石の団鉱方法。[Claims] 1. Clay N treated dry or wet depending on dehydration properties
In a method of mixing ore powder in an appropriate amount at a time to have the moisture content necessary to obtain the desired briquette strength, and forming the mixed raw material with the moisture content adjusted in this way using a briquette machine, The moisture content of the mixed raw material supplied to the briquetting machine is adjusted according to the average clay content of the ore to be mixed, and the mixed raw material is kneaded and cured to homogenize it before briquetting. Characteristic briquette method for clayey Ni ore.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1142893A JPH0781168B2 (en) | 1989-06-07 | 1989-06-07 | Clay Ni ore briquette method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1142893A JPH0781168B2 (en) | 1989-06-07 | 1989-06-07 | Clay Ni ore briquette method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0310026A true JPH0310026A (en) | 1991-01-17 |
| JPH0781168B2 JPH0781168B2 (en) | 1995-08-30 |
Family
ID=15326048
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1142893A Expired - Lifetime JPH0781168B2 (en) | 1989-06-07 | 1989-06-07 | Clay Ni ore briquette method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0781168B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015168849A (en) * | 2014-03-06 | 2015-09-28 | 株式会社日向製錬所 | Method for manufacturing briquette |
| WO2020218170A1 (en) * | 2019-04-23 | 2020-10-29 | 株式会社神戸製鋼所 | Method for producing iron ore pellet |
| JP2020180371A (en) * | 2019-04-23 | 2020-11-05 | 株式会社神戸製鋼所 | Manufacturing method of iron ore pellet |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6223944A (en) * | 1985-07-22 | 1987-01-31 | Nippon Yakin Kogyo Co Ltd | Refining method for nickel oxide or the like |
-
1989
- 1989-06-07 JP JP1142893A patent/JPH0781168B2/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6223944A (en) * | 1985-07-22 | 1987-01-31 | Nippon Yakin Kogyo Co Ltd | Refining method for nickel oxide or the like |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015168849A (en) * | 2014-03-06 | 2015-09-28 | 株式会社日向製錬所 | Method for manufacturing briquette |
| WO2020218170A1 (en) * | 2019-04-23 | 2020-10-29 | 株式会社神戸製鋼所 | Method for producing iron ore pellet |
| JP2020180371A (en) * | 2019-04-23 | 2020-11-05 | 株式会社神戸製鋼所 | Manufacturing method of iron ore pellet |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0781168B2 (en) | 1995-08-30 |
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