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JPS5933646B2 - Manufacturing method of sintered raw material - Google Patents
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JPS5933646B2 - Manufacturing method of sintered raw material - Google Patents

Manufacturing method of sintered raw material

Info

Publication number
JPS5933646B2
JPS5933646B2 JP7293081A JP7293081A JPS5933646B2 JP S5933646 B2 JPS5933646 B2 JP S5933646B2 JP 7293081 A JP7293081 A JP 7293081A JP 7293081 A JP7293081 A JP 7293081A JP S5933646 B2 JPS5933646 B2 JP S5933646B2
Authority
JP
Japan
Prior art keywords
raw material
water
powder
sintered
sintering
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.)
Expired
Application number
JP7293081A
Other languages
Japanese (ja)
Other versions
JPS57188628A (en
Inventor
悌二 渋谷
汎 斉藤
亜男 中尾
信一 黒沢
光男 野沢
吉史 松永
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 Engineering Corp
Original Assignee
Nippon Kokan Ltd
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 Kokan Ltd filed Critical Nippon Kokan Ltd
Priority to JP7293081A priority Critical patent/JPS5933646B2/en
Publication of JPS57188628A publication Critical patent/JPS57188628A/en
Publication of JPS5933646B2 publication Critical patent/JPS5933646B2/en
Expired legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】 本発明は焼結原料、特にブレンディング粉鉄の製造方法
に関するものであり、焼結工程中における通気性を向上
させ、焼結鉱自体の還元粉化性を向上させると共に、生
産性を向上させることをその目的とするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing sintering raw materials, particularly blending powdered iron, which improves air permeability during the sintering process, improves the reduction and pulverizability of the sintered ore itself, and , its purpose is to improve productivity.

従来から高炉原料の予備処理方法として焼結法が広く知
られている。
The sintering method has been widely known as a pretreatment method for blast furnace raw materials.

この方法は一般に第1図に示すごとく、まず配合槽1に
ブレンディング粉鉄(B粉)、石灰石、粉コークス、返
鉱を別々に装入し、それぞれの配合槽から各原料を適量
切出して配合した後、それを1次ミキサ2に送って水分
添加、混合、造粒を行ない、必要に応じて2次ミキサ3
でさらに造粒する。
Generally, as shown in Figure 1, this method first charges blending powder iron (B powder), limestone, coke powder, and return ore separately into a blending tank 1, and then cuts out appropriate amounts of each raw material from each blending tank and blends them. After that, it is sent to the primary mixer 2 for water addition, mixing, and granulation, and then sent to the secondary mixer 3 as necessary.
Further granulation is performed.

こうして造粒された原料をホッパ4から焼結機5のエン
ドレス状パレットに装入すると共に、点火炉6により原
料中に混合されているコークスに点火させ、焼結機下方
に設置された風箱より強制的に吸引通風することによっ
て原料の焼結を行なっているものである。
The raw material granulated in this way is charged from the hopper 4 to the endless pallet of the sintering machine 5, and the coke mixed in the raw material is ignited by the ignition furnace 6. The raw material is sintered by more forced suction and ventilation.

しかし、このような方法においては原料は焼結機5に装
入される直前に主として1次ミキサ2で散水造粒される
ものであるから、バインダーとしての水分が原料に完全
かつ均一に浸透せず、通気性(造粒性)が悪くなり、生
産性も劣ると共に成品の品質指数である還元粉化指数が
悪く、これを改善するため燃料である粉コークスの使用
量が多くなるといった問題がある。
However, in such a method, the raw material is mainly water granulated in the primary mixer 2 immediately before being charged into the sintering machine 5, so water as a binder does not completely and uniformly permeate the raw material. First, the permeability (granulation) is poor, the productivity is poor, and the reduction pulverization index, which is a quality index of the finished product, is poor, and in order to improve this, the amount of coke powder used as fuel has to be increased. be.

これに加え各焼結原料は焼結鉱の品質の基礎ともなり、
その管理が必要となるが、資源としての推移や需給のバ
ランスから、必ずしも最適条件の原料が得られるもので
はなく、不良銘柄については積極的にその弱点をカバー
するような操業技術、処理技術の開発が要望されている
In addition to this, each sintering raw material also serves as the basis for the quality of sintered ore.
However, due to resource trends and the balance of supply and demand, it is not always possible to obtain raw materials with optimal conditions. Development is required.

本発明は、このような現状に鑑みて検討を重ねた結果提
案されたものであり、特に前記配合槽に装入される前の
焼結原料にあらかじめ水分を添加して造粒することによ
って、造粒性を高め焼結工程中の通気性を向上させ、か
つ生産性の向上を図らんとするものである。
The present invention was proposed as a result of repeated studies in view of the current situation, and in particular, by adding water in advance to the sintering raw material before charging it into the mixing tank and granulating it, The purpose is to improve granulation properties, improve air permeability during the sintering process, and improve productivity.

以下本発明を焼結原料としてのブレンディング粉鉄(B
紛)を例にとって説明すると、一般に焼結に供される粉
原料は本船からアンローダより粗鉱ヤードに山積みした
後、他の別銘柄の原料と適当な割合で混合してB粉を得
、これを第1図の配合槽1に装入しているものである。
The present invention will be described below as a blending powder iron (B) as a sintering raw material.
Taking powder powder as an example, powder raw materials used for sintering are generally piled up at the rough ore yard from the ship via an unloader, and then mixed with other brands of raw materials in an appropriate ratio to obtain powder B. is charged into the blending tank 1 shown in FIG.

しかして本発明では前記粉原料をこの配合槽1に装入す
る前にあらかじめ水分を添加し、造粒することをその厚
木的な特徴とする。
However, the present invention is characterized in that water is added in advance to the powder raw material before it is charged into the blending tank 1, and the powder is granulated.

第2図ぽその概略図を示したもので、粉原料を本船10
から搬送コンベア11,12を通して粗鉱ヤード13に
貯蔵する際、その途中に調湿ミキサ14を設置し、散水
ノズル15から散水造粒しているものである。
Figure 2 shows a schematic diagram of Poso, in which powder raw materials are
When the coarse ore is stored in a yard 13 through conveyors 11 and 12, a humidity control mixer 14 is installed in the middle of the process, and granulation is performed by spraying water from a water nozzle 15.

また粗鉱ヤード13に貯蔵された各原料は所定割合で混
合した後ブレンディングヤード16に貯蔵されることに
なるが、本発明では前記調湿ミキサ14に代えまたはこ
れと併用して搬送コンベア17,1Bの間に他の調湿ミ
キサ19を設置し、ここにおいても散水ノズル20*か
ら散水造粒してもよい(なお、第2図において21はブ
レンデインダスカッターである)。
Further, each raw material stored in the rough ore yard 13 is mixed in a predetermined ratio and then stored in the blending yard 16, but in the present invention, the conveyor 17, Another humidity control mixer 19 may be installed between 1B and granulation may be performed by spraying water from the water spray nozzle 20* here as well (note that 21 in FIG. 2 is a blender dust cutter).

このように配合槽に装入される原料をあらかじめ調湿ミ
キサで造粒すると、第3図に示すごとく、各種銘柄の造
粒指数は著しく向上することがわかる。
As shown in FIG. 3, it can be seen that when the raw materials charged into the blending tank are granulated in advance using a humidity control mixer, the granulation index of various brands is significantly improved.

なお、第3図において、SKF指数、SP指数はそれぞ
れ下式で示される。
In addition, in FIG. 3, the SKF index and the SP index are each expressed by the following formulas.

PS指数−100 (完全乾燥粒度の−0,25朋) =()X100 6′″″″、、 *n# FJ門 (−(j十( 粒度の合 の合計 −0,25mm 一方、本発明では、上記調湿ミキサにおいて添加する水
分が造粒に最適な量となるようコントロールされること
になる。
PS index -100 (-0,25 mm of completely dry particle size) = () Then, the amount of water added in the humidity control mixer is controlled to be the optimum amount for granulation.

その具体例を第1表及び第4図に示す。Specific examples are shown in Table 1 and FIG.

これらのデータにもみられるように添加される適正水分
は銘柄によって異なり、Aは3.2〜4.5%、Bは3
.8〜5.4%、Cは5.0〜7.2%が最適である。
As seen in these data, the appropriate amount of moisture added varies depending on the brand, with A being 3.2 to 4.5% and B being 3.
.. The optimum content is 8 to 5.4%, and the optimum content of C is 5.0 to 7.2%.

即ち、適正水分は各銘柄の最大通気度水分×(0,7〜
1.0)の範囲にコントロールすればよいことになる。
In other words, the appropriate moisture content is the maximum air permeability moisture of each brand x (0,7~
1.0).

第5図はこうした水分コントロールを行なうためのシス
テムの一例を示したものであり、原料搬送コンベア30
.31の中間にホッパー32を設け、このホッパー32
に中性子水分計等の水分計33を設けると共に、コンベ
ア31の中間に秤量装置34を設置し、これにより持込
み水分量と原料搬送量とから適正水分となるよう調湿ミ
キサ40の散水ノズル41の散水量を調整するものであ
る。
Figure 5 shows an example of a system for controlling moisture content, in which the raw material conveyor 30
.. A hopper 32 is provided in the middle of 31, and this hopper 32
A moisture meter 33, such as a neutron moisture meter, is installed in the conveyor 31, and a weighing device 34 is installed in the middle of the conveyor 31. This adjusts the amount of water sprinkled.

また他の例として調湿ミキサ40の出側コンベア35,
36の間に水分計37の付いた中間ホッパ38を設置し
、調湿ミキサ40から搬出される原料が所定水分量とな
るよう散水ノズル41にフィードバックするようにして
もよい。
In addition, as another example, the outlet conveyor 35 of the humidity control mixer 40,
An intermediate hopper 38 equipped with a moisture meter 37 may be installed between the humidity control mixer 40 and the moisture control mixer 40 to provide feedback to the water spray nozzle 41 so that the raw material carried out from the humidity control mixer 40 has a predetermined moisture content.

他方、本発明においては調湿ミキサでの造粒時に、生石
灰、消石灰のバインダーを添加すると通気性(造粒性)
が著しく向上することになる。
On the other hand, in the present invention, adding binders such as quicklime and slaked lime during granulation using a humidity control mixer improves air permeability (granulation properties).
will be significantly improved.

こうしたバインダーは第5図に示すごとく、調湿ミキサ
40の入側に設けられたホッパ39から切出してもよく
、あるいは水に溶して散水ノズル41から散水するよう
にしてもよい。
As shown in FIG. 5, such a binder may be cut out from a hopper 39 provided on the inlet side of the humidity control mixer 40, or it may be dissolved in water and sprayed with water from a water spray nozzle 41.

第6図はこのバインダー添加効果を示したもので、図中
a = dの条件は下表の通りである。
FIG. 6 shows the effect of this binder addition, and the conditions of a=d in the figure are as shown in the table below.

このバインダーの添加量は特に限定されるものではない
が通常1〜3%添加される。
The amount of this binder added is not particularly limited, but it is usually added in an amount of 1 to 3%.

この場合第5図の秤量装置34とバインダー供給ホッパ
39とを連動させて原料搬送量に対し常に所定割合とな
るようにコントロールしてもよい。
In this case, the weighing device 34 shown in FIG. 5 and the binder supply hopper 39 may be linked to control the feed amount to always be at a predetermined ratio to the amount of raw material conveyed.

なお本発明では、添加される水分を温水とすればより効
果的である。
In the present invention, it is more effective if the water added is warm water.

この場合の水温は50℃以上好ましくは80〜90℃が
推奨される。
In this case, the water temperature is recommended to be 50°C or higher, preferably 80 to 90°C.

以上説明したような本発明によれば、得られた焼結用原
料は焼結工程中の通気性が向上し、同時に還元粉化率が
向上すると共に、生産性がアップする管種々のすぐれた
効果が得られるものである。
According to the present invention as explained above, the obtained sintering raw material has improved air permeability during the sintering process, and at the same time, the reduction powdering rate has been improved, and the productivity has been increased. It is effective.

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

第1図は一般的な焼結工程を示した概略図、第2図は本
発明法を説明するための概略図、第3図は本発明におい
て調湿ミキサで造粒した場合の効果を示すグラフ、第4
図は各種銘柄の造粒適正水分を示すグラフ、第5図は本
発明において水分コントロールを行なうためのシステム
を示した概略図、第6図はバインダーの添加効果を示す
グラフである。 図中1は配合槽、13は粗鉱ヤード、14゜19.40
は調湿ミキサ、15,20,41は散水ノズルである。
Figure 1 is a schematic diagram showing a general sintering process, Figure 2 is a schematic diagram for explaining the method of the present invention, and Figure 3 is a diagram showing the effect of granulation using a humidity control mixer in the present invention. graph, 4th
The figure is a graph showing the appropriate moisture content for granulation of various brands, FIG. 5 is a schematic diagram showing a system for controlling moisture content in the present invention, and FIG. 6 is a graph showing the effect of adding a binder. In the figure, 1 is a blending tank, 13 is a rough ore yard, 14°19.40
1 is a humidity control mixer, and 15, 20, and 41 are water nozzles.

Claims (1)

【特許請求の範囲】 1 焼結に供される粉原料を1次ミキサの手前に設置さ
れた配合槽に装入する前にあらかじめ水分を添加して造
粒することを特徴とする焼結原料の製造方法。 2 焼結に供される粉原料を1次ミキサの手前に設置さ
れた配合槽に装入する前にあらかじめ水分及びバインダ
ーを添加して造粒することを特徴とする焼結原料の製造
方法。 3 水分を添力目するに際し、粉原料の銘柄に応じて造
粒に最適な水分に制御することを特徴とする前記第1項
又は第2項記載の焼結原料の製造方法64 水分が温水
であることを特徴とする前記第1項又は第2項記載の焼
結原料の製造方法。
[Claims] 1. A sintering raw material characterized in that water is added in advance to the powdered raw material to be sintered and the powder is granulated before being charged into a mixing tank installed before a primary mixer. manufacturing method. 2. A method for producing a sintering raw material, which comprises adding moisture and a binder in advance and granulating the powdered raw material to be sintered before charging it into a mixing tank installed before a primary mixer. 3. Method for producing a sintered raw material according to item 1 or 2 above, characterized in that when adding moisture, the moisture content is controlled to be optimal for granulation according to the brand of the powder raw material. The method for producing a sintered raw material according to the above item 1 or 2, characterized in that:
JP7293081A 1981-05-15 1981-05-15 Manufacturing method of sintered raw material Expired JPS5933646B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7293081A JPS5933646B2 (en) 1981-05-15 1981-05-15 Manufacturing method of sintered raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7293081A JPS5933646B2 (en) 1981-05-15 1981-05-15 Manufacturing method of sintered raw material

Publications (2)

Publication Number Publication Date
JPS57188628A JPS57188628A (en) 1982-11-19
JPS5933646B2 true JPS5933646B2 (en) 1984-08-17

Family

ID=13503564

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7293081A Expired JPS5933646B2 (en) 1981-05-15 1981-05-15 Manufacturing method of sintered raw material

Country Status (1)

Country Link
JP (1) JPS5933646B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0261818U (en) * 1988-10-26 1990-05-09

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5130477B2 (en) * 2007-05-30 2013-01-30 新日鐵住金株式会社 Granulation method of iron ore raw material containing fine powder
JP5817644B2 (en) * 2012-05-24 2015-11-18 新日鐵住金株式会社 Method of adding binder to sintering raw material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0261818U (en) * 1988-10-26 1990-05-09

Also Published As

Publication number Publication date
JPS57188628A (en) 1982-11-19

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