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JPH0112554B2 - - Google Patents
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JPH0112554B2 - - Google Patents

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Publication number
JPH0112554B2
JPH0112554B2 JP23952183A JP23952183A JPH0112554B2 JP H0112554 B2 JPH0112554 B2 JP H0112554B2 JP 23952183 A JP23952183 A JP 23952183A JP 23952183 A JP23952183 A JP 23952183A JP H0112554 B2 JPH0112554 B2 JP H0112554B2
Authority
JP
Japan
Prior art keywords
iron powder
crusher
flow path
classification
switching device
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
JP23952183A
Other languages
Japanese (ja)
Other versions
JPS60132684A (en
Inventor
Hiroyuki Yamamoto
Kotaro Ookawa
Eiji Hatsuya
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 JP23952183A priority Critical patent/JPS60132684A/en
Publication of JPS60132684A publication Critical patent/JPS60132684A/en
Publication of JPH0112554B2 publication Critical patent/JPH0112554B2/ja
Granted legal-status Critical Current

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  • Disintegrating Or Milling (AREA)
  • Combined Means For Separation Of Solids (AREA)

Description

【発明の詳細な説明】 本発明は、仕上還元後の鉄粉の分級装置に関す
る。さらに詳しくは、鉄粉の分級系統のオーバー
サイズを、解砕機を経て分級系統に還流する系統
と、これを系外に排出する系統とを設け、この両
系統を切り替える切替装置を解砕機の負荷電流値
によつて切り替えるようにした、製品歩留の高い
分級装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for classifying iron powder after finish reduction. More specifically, the oversized iron powder classification system is equipped with a system that returns the iron powder to the classification system via the crusher and a system that discharges it outside the system, and a switching device that switches between the two systems is used to load the crusher. This invention relates to a classification device that switches according to the current value and has a high product yield.

第1図、第2図は従来の鉄粉の分級フローを示
したものである。予め、ある見掛密度に整えられ
た粗還元鉄粉は、仕上還元炉1において、アンモ
ニア分解ガス雰囲気、800〜1000℃にて脱炭、脱
酸、脱窒される。同時に鉄粉は仕上還元炉1で、
弱い焼結作用を受けて粒子同志が結合しケーキ状
で連続的に排出される。このケーキ状の鉄粉は解
砕機9で1mm以下程度に解砕された後、貯蔵切出
し装置10を介して一定量づつ鉄粉分級装置の空
気分級配管2内に供給される。
Figures 1 and 2 show the conventional classification flow of iron powder. The crude reduced iron powder, which has been prepared in advance to a certain apparent density, is decarburized, deoxidized, and denitrified in a finishing reduction furnace 1 in an ammonia decomposition gas atmosphere at 800 to 1000°C. At the same time, iron powder is processed in finishing reduction furnace 1.
Due to the weak sintering effect, the particles bond together and are continuously discharged in the form of a cake. After this cake-like iron powder is crushed into pieces of about 1 mm or less in a crusher 9, it is supplied in fixed amounts into the air classification pipe 2 of the iron powder classification apparatus via a storage/cutting device 10.

分級装置はブロワ8、空気分級配管2、遠心式
空気分級機3、サイクロン7等から成る空気分級
装置と、一次篩4、二次篩5等から成る篩分装置
とから成つている。
The classification device consists of an air classification device consisting of a blower 8, an air classification pipe 2, a centrifugal air classifier 3, a cyclone 7, etc., and a sieving device consisting of a primary sieve 4, a secondary sieve 5, etc.

貯蔵切出し装置10から空気分級配管2内に供
給された鉄粉は、空気輸送されて遠心式空気分級
機3に至り、比較的大きな大部分の粒子は遠心式
空気分級機3で捕集されて篩分装置4,5に入
り、小さな粒子は空気流とともにさらにサイクロ
ン7に至り、ここで捕集された後ホツパ6Eに貯
蔵される。サイクロン7を出た清浄空気はブロワ
8へ再循環される。
The iron powder supplied from the storage/cutting device 10 into the air classification pipe 2 is pneumatically transported to the centrifugal air classifier 3, where most of the relatively large particles are collected. The small particles enter the sieving devices 4 and 5, and then travel with the airflow to the cyclone 7, where they are collected and stored in the hopper 6E. The clean air leaving the cyclone 7 is recirculated to the blower 8.

遠心式空気分級装置3で捕集された鉄粉は、一
次篩4において、例えば+90メツシユ、90〜100
メツシユ、−100メツシユに分離され、続いて−
100メツシユの鉄粉は二次篩5で篩分けられ、各
粒度別にホツパ6A,6B,6C,6Dに収納さ
れる。
The iron powder collected by the centrifugal air classifier 3 is passed through the primary sieve 4, for example, +90 mesh, 90 to 100 mesh.
mesh, separated into −100 meshes, and then −
100 mesh iron powder is sieved by a secondary sieve 5 and stored in hoppers 6A, 6B, 6C, and 6D according to particle size.

一方一次篩のオーバーサイズ鉄粉(+90メツシ
ユ)はコンテナ12に貯蔵される。この後鉄粉は
製品の要求仕様に合わせてホツパ6A〜6Eから
それぞれ所要量を切出し、混合、秤量、梱包工程
を経て製品として出荷される。
On the other hand, the oversized iron powder (+90 mesh) of the primary sieve is stored in the container 12. Thereafter, the required amount of iron powder is cut out from the hoppers 6A to 6E according to the required specifications of the product, and is shipped as a product through mixing, weighing, and packaging steps.

コンテナ12に貯蔵された+90メツシユのオー
バーサイズ鉄粉は擬似粒子が大部分を占め、再解
砕を行えば製品となるので、このままでは歩留低
下となる。また後日再解砕を行うのは多くの人力
を必要とするという問題があつた。
Most of the +90 mesh oversized iron powder stored in the container 12 is pseudo-particles, and if it is crushed again, it will become a product, so if it continues as it is, the yield will decrease. Another problem was that re-crushing at a later date required a lot of manpower.

そこで第2図に示すような解砕機11を設け、
この解砕機11に一次篩からのオーバーサイズ鉄
粉を供給してその解砕物を空気分級配管2に還流
させることが行われていた。このように解砕機1
1を設けた場合には、オーバーサイズ鉄粉が循環
する閉回路(11→2→3→4→11)ができ、 (1) やがてこの閉回路を流れる鉄粉が多量となり
解砕機11の解砕能力を越えて解砕できなくな
る、 (2) 繰り返し解砕を受けることで鉄粉の物性値、
例えば見掛密度、ラトラー値、圧粉密度などが
悪化する、 などの問題が生じる。
Therefore, a crusher 11 as shown in FIG. 2 is installed,
Oversized iron powder from the primary sieve was supplied to the crusher 11 and the crushed material was returned to the air classification pipe 2. In this way, the crusher 1
1, a closed circuit (11 → 2 → 3 → 4 → 11) is created in which oversized iron powder circulates, and (1) eventually a large amount of iron powder flows through this closed circuit, causing the disintegration of the crusher 11. (2) Repeated crushing causes the physical properties of iron powder to change,
For example, problems such as apparent density, Rattler value, green density, etc. may deteriorate.

本発明はこのような問題を解決した鉄粉の分級
装置を提供することを目的とするものである。
The object of the present invention is to provide an iron powder classification device that solves these problems.

第3図は本発明の一実施例を示す系統図で、符
号1〜10は第1図、第2図と同様である。
FIG. 3 is a system diagram showing an embodiment of the present invention, and reference numerals 1 to 10 are the same as in FIGS. 1 and 2.

本発明は、鉄粉製造における仕上還元後の鉄粉
ケーキを分級する装置において、分級工程からの
オーバーサイズ鉄粉の排出流路を、解砕機11を
経て分級工程に還流させる系統と、系外に排出す
る系統とに分岐し、該分岐点に前記解砕機の負荷
電流値に応じて切替自在な流路切替装置12を設
けたことを特徴とする鉄粉の分級装置である。
The present invention provides an apparatus for classifying iron powder cake after finishing reduction in iron powder production, including a system for returning oversized iron powder from the classification process to the classification process via a crusher 11, and a system outside the system. This iron powder classification apparatus is characterized in that it branches into a system for discharging iron powder and a system for discharging iron powder, and is provided with a flow path switching device 12 at the branch point that can be switched freely according to the load current value of the crusher.

一次篩4のオーバーサイズ鉄粉は流路切替装置
12を介して解砕機11に入り、さらに空気分級
配管2へ送られ循環処理される系と、流路切替装
置12にて系外に排出され、コンテナ13へ貯蔵
される系とに分けられる。
The oversized iron powder from the primary sieve 4 enters the crusher 11 via the flow path switching device 12 and is further sent to the air classification piping 2 where it is circulated and then discharged to the outside of the system through the flow path switching device 12. , and a system stored in a container 13.

流路切替装置12としては、例えばシリンダ等
によつて前記分岐点に設けた切替ダンパを切替え
る方式でもよく、また第4図に示すように排出管
14の先端に設けた切替え回動シユート15をシ
リンダ16によつて切替えるようにしてもよい。
The flow path switching device 12 may be, for example, a system in which a switching damper provided at the branch point is switched using a cylinder or the like, or a switching chute 15 provided at the tip of the discharge pipe 14 as shown in FIG. The switching may be performed using the cylinder 16.

前記流路切替装置の切替は、解砕機11の駆動
モータ17の負荷電流を検出する電流計18に設
定電流値を与えておき、設定電流値になれば警報
を出力するかあるいは表示をするようにしてお
き、この設定負荷電流値によつて行う。すなわち
設定電流値以下であれば流路切替装置を解砕、分
級系側として鉄粉の歩留向上を図り、設定電流値
以上になれば、流路切替装置を排出系側に切替え
るとともに貯蔵切出し装置10から供給を中止
し、鉄粉の物性(見掛け密度等)の悪化を防止す
る。
To switch the flow path switching device, a set current value is given to the ammeter 18 that detects the load current of the drive motor 17 of the crusher 11, and when the set current value is reached, an alarm is output or displayed. This is done using this set load current value. In other words, if the current is below the set current value, the flow switching device is switched to the crushing and classification system side to improve the yield of iron powder, and when the current is higher than the set current value, the flow switching device is switched to the discharge system side and stored. The supply from the device 10 is stopped to prevent deterioration of the physical properties (apparent density, etc.) of the iron powder.

この切替操作は、前記警報により手動で切替操
作盤を操作してもよく、また設定負荷電流と検出
負荷電流とを比較する比較器を電流計測系統に組
み込み、その出力を流路切替装置の制御器に入力
し、自動的に流路切替制御をさせることもでき
る。
This switching operation may be performed by manually operating the switching operation panel in response to the above-mentioned alarm, or by incorporating a comparator into the current measurement system to compare the set load current and the detected load current, and using its output to control the flow path switching device. It is also possible to input the information into the device and automatically control the flow path switching.

上記切替制御によつて、やがて閉回路の鉄粉は
一次篩4、二次篩5の篩下となつてホツパ6A〜
6Dに貯蔵されるか、または流路切替装置12に
よつて系外に排出されてコンテナ13に貯えら
れ、解砕機11を通過する鉄粉は零となる。この
時の解砕機11の無負荷電流を捕えて再び貯蔵切
出装置10を起動し、流路切替装置12を解砕機
11側に接続する。
By the above switching control, the iron powder in the closed circuit will eventually reach the bottom of the primary sieve 4 and the secondary sieve 5, and the hopper 6A~
The amount of iron powder that is stored in the iron powder 6D or discharged outside the system by the flow path switching device 12 and stored in the container 13, and passes through the crusher 11 becomes zero. The no-load current of the crusher 11 at this time is captured and the storage/cutting device 10 is activated again, and the flow path switching device 12 is connected to the crusher 11 side.

系外排出時には、仕上還元炉1、解砕機9を経
て空気分級配管2へ入るニユーフイードの鉄粉は
貯蔵切出装置10に貯えられており、閉回路内の
鉄粉だけが系外に排出されることになる。従つ
て、鉄粉の物性を変えることなく、その歩留向上
を図ることができる。
At the time of discharge outside the system, the iron powder of the new feed that enters the air classification pipe 2 through the finishing reduction furnace 1 and the crusher 9 is stored in the storage/cutting device 10, and only the iron powder in the closed circuit is discharged outside the system. That will happen. Therefore, it is possible to improve the yield without changing the physical properties of the iron powder.

なお、本発明は、空気分級方式で説明したが貯
蔵切出装置10からバケツトコンベア等を介して
分級する装置に供給する方式でも同様に実施する
ことができる。
Although the present invention has been described using an air classification system, it can be similarly implemented using a system in which the air is supplied from the storage/cutting device 10 to a classification device via a bucket conveyor or the like.

本発明は以上のように構成されているので、極
めて製品歩留の高い鉄粉の分級を行うことができ
る。
Since the present invention is configured as described above, it is possible to classify iron powder with extremely high product yield.

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

第1図、第2図は従来の鉄粉分級装置のフロー
を示す系統図、第3図は本発明の実施例の系統
図、第4図は流路切替装置の模式側面図である。 1……仕上還元炉、2……空気分級配管、3…
…遠心式空気分級機、4……一次篩、5……二次
篩、6(6A,6B,6C,6D,6E)……ホ
ツパ、7……サイクロン、8……ブロワ、9……
解砕機、10……貯蔵切出装置、11……解砕
機、12……流路切替装置、13……コンテナ、
14……排出流路、15……回動シユート、16
……シリンダ、17……解砕機モータ、18……
電流計。
1 and 2 are system diagrams showing the flow of a conventional iron powder classifier, FIG. 3 is a system diagram of an embodiment of the present invention, and FIG. 4 is a schematic side view of a flow path switching device. 1... Finish reduction furnace, 2... Air classification piping, 3...
...Centrifugal air classifier, 4...Primary sieve, 5...Secondary sieve, 6 (6A, 6B, 6C, 6D, 6E)...Hotsupa, 7...Cyclone, 8...Blower, 9...
Crushing machine, 10...Storage and cutting device, 11...Crushing machine, 12...Flow path switching device, 13...Container,
14... Discharge channel, 15... Rotating chute, 16
...Cylinder, 17...Crusher motor, 18...
Ammeter.

Claims (1)

【特許請求の範囲】[Claims] 1 鉄粉製造における仕上還元後の鉄粉ケーキを
分級する装置において、分級工程からのオーバー
サイズ鉄粉の排出流路を解砕機を経て分級工程に
還流させる系統と系外に排出する系統とに分岐
し、該分岐点に前記解砕機の負荷電流値に応じて
切替自在な流路切替装置を設けたことを特徴とす
る鉄粉の分級装置。
1. In an apparatus for classifying iron powder cake after finishing reduction in iron powder production, the discharge flow path for oversized iron powder from the classification process is divided into a system for returning it to the classification process via a crusher and a system for discharging it outside the system. 1. An apparatus for classifying iron powder, characterized in that the flow path is branched, and a flow path switching device that can be switched according to the load current value of the crusher is provided at the branch point.
JP23952183A 1983-12-19 1983-12-19 Classifier of iron powder Granted JPS60132684A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23952183A JPS60132684A (en) 1983-12-19 1983-12-19 Classifier of iron powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23952183A JPS60132684A (en) 1983-12-19 1983-12-19 Classifier of iron powder

Publications (2)

Publication Number Publication Date
JPS60132684A JPS60132684A (en) 1985-07-15
JPH0112554B2 true JPH0112554B2 (en) 1989-03-01

Family

ID=17046032

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23952183A Granted JPS60132684A (en) 1983-12-19 1983-12-19 Classifier of iron powder

Country Status (1)

Country Link
JP (1) JPS60132684A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63169898A (en) * 1987-01-07 1988-07-13 Haaman:Kk Remote controller
JPS63111983U (en) * 1987-01-08 1988-07-19
CN103501588B (en) * 2011-02-10 2016-09-07 同和电子科技有限公司 Metal coating material

Also Published As

Publication number Publication date
JPS60132684A (en) 1985-07-15

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