JPH05168899A - Device for distributing and supplying raw material in vibrating granulator - Google Patents

Device for distributing and supplying raw material in vibrating granulator

Info

Publication number
JPH05168899A
JPH05168899A JP35653791A JP35653791A JPH05168899A JP H05168899 A JPH05168899 A JP H05168899A JP 35653791 A JP35653791 A JP 35653791A JP 35653791 A JP35653791 A JP 35653791A JP H05168899 A JPH05168899 A JP H05168899A
Authority
JP
Japan
Prior art keywords
raw material
hopper
vibrating granulator
container
granulator
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.)
Withdrawn
Application number
JP35653791A
Other languages
Japanese (ja)
Inventor
Kiyoshi Ogata
清志 緒方
Shoji Nitta
昭二 新田
Akira Suemori
▲あきら▼ 末森
Noribumi Fujii
紀文 藤井
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 JP35653791A priority Critical patent/JPH05168899A/en
Publication of JPH05168899A publication Critical patent/JPH05168899A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015Feeding of the particles in the reactor; Evacuation of the particles out of the reactor

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

PURPOSE:To efficiently mass-produce a granular product which is uniform in grain diameter and homogeneous. CONSTITUTION:A device 50 for distributing and supplying a raw material in a vibrating granulator 5 is constituted by providing both a belt conveyor 51 for carrying and introducing the wet raw material and a hopper 52 which is arranged in the going side of the velt conveyor 51 and capable of being rocked on the raw material introducing region of a vessel 35. Further, two pieces of belt conveyors 61, 61 for carrying out the raw material are oppositely arranged on the inside surface of the hopper 52. The interval between the descending parts 61A, 61A transferring toward the lower parts of both conveyors 61, 61 is narrowed toward the lower parts thereof.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、例えば微粉状の鉄鉱石
を粉状化するために用いられる等の振動造粒機に原料を
均等に分配して供給するための原料分配供給装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a raw material distribution and supply device for evenly distributing and supplying a raw material to a vibrating granulator such as used for pulverizing fine iron ore.

【0002】[0002]

【従来の技術】製鉄業においては、微粉状の鉄鉱石(以
下これを原料と称する)を粉状化することによって、品
質の良好な焼結鉱にするための工程がある。本出願人
は、この工程において、効率良く原料を粉状化させるた
め、特願平 3-207285 〜特願平3-207289の如くにより、
振動造粒法と呼ばれる方式を用いた振動造粒機を提案し
た。
2. Description of the Related Art In the iron-making industry, there is a process for pulverizing finely powdered iron ore (hereinafter referred to as a raw material) into a sinter having a good quality. In order to efficiently powder the raw material in this step, the present applicant applies the method described in Japanese Patent Application No. 3-207285 to Japanese Patent Application No. 3-207289.
We proposed a vibration granulator using a method called vibration granulation.

【0003】この振動造粒機は、例えば図6に示す如
く、一端に原料投入部1、他端に原料排出部2を形成
し、水平面内に配置された 2本の同位相で、かつ同振幅
で実線矢印で示す方向に回転駆動される 2本の偏芯軸3
上に積載されたトラフ状容器4を、上下方向に複数段、
横方向に複数列密接して並設した構造になっている。
This vibrating granulator has, for example, as shown in FIG. 6, a raw material feeding portion 1 at one end and a raw material discharging portion 2 at the other end. Two eccentric shafts 3 that are driven to rotate in the direction indicated by the solid arrow with amplitude 3
The trough-shaped containers 4 loaded on the top are arranged in a plurality of stages in the vertical direction,
It has a structure in which a plurality of rows are closely arranged side by side in the lateral direction.

【0004】このような構造の振動造粒機において、容
器4は 2本の偏芯軸3の実線矢印方向への回転によっ
て、これのどの部分においても矢印で示すような円振動
を与えられる。これにより、容器4の供給口1から装入
された、所要の湿り程度に加湿混合された湿潤原料は、
容器4の円振動の働きによって上方向に放り上げられ、
そして落下し、更に自転運動を繰り返し与えられなが
ら、排出口2の側に移送されていき、この間に原料は粒
状化し、最後に粒の形状をした製品となって排出口2か
ら排出される。
In the vibrating granulator having such a structure, the container 4 is given a circular vibration as shown by an arrow at any portion thereof by the rotation of the two eccentric shafts 3 in the directions of solid arrows. As a result, the wet raw material charged from the supply port 1 of the container 4 and humidified and mixed to a required degree of wetness is
It is thrown up by the action of the circular vibration of the container 4,
Then, it falls and is further transferred to the discharge port 2 side while being repeatedly rotated, and during this time, the raw material is granulated, and finally the product in the form of particles is discharged from the discharge port 2.

【0005】[0005]

【発明が解決しようとする課題】然るに、上述の如くの
振動造粒機においては、供給口1に挿入する原料の量
を、縦横に複数本並んでいるいずれの容器4にも均等
に、然も連続した略一定量で安定して分配供給してやる
ことが、粒径の揃った均質な粒状の製品を効率良く、然
も多量に生産するために不可欠な条件である。
However, in the vibrating granulator as described above, the amount of the raw material to be inserted into the supply port 1 is evenly distributed in any of the containers 4 arranged in the vertical and horizontal directions. In order to efficiently produce a uniform granular product having a uniform particle size in an efficient manner, it is indispensable to stably supply and supply a continuous and substantially constant amount.

【0006】然しながら、上述の振動造粒機で扱われる
加湿混合された湿潤原料は非常に流動性が悪く、然も極
めて壁面に付着し易いといった非常に扱い難い性質を有
している。
However, the humidified and mixed wet raw material used in the above-described vibrating granulator has very poor fluidity and has a very unwieldy property that it is extremely likely to adhere to the wall surface.

【0007】例えば、従来用いられているような、貯蔵
部5が下部に行くにしたがって狭くなった図7に示すよ
うな、所謂ホッパーと呼ばれる供給装置6においては、
これの上部から装入され充満された原料を、これの下部
から取出すような場合、原料はいとも簡単に壁面7に付
着し、原料の流動性が悪いこともあって図示する如くの
ブリッジを形成して閉塞状態となり使用不能に陥ってし
まう。
[0007] For example, in a conventional feeding device 6 shown in FIG. 7, in which the storage portion 5 becomes narrower toward the bottom, a so-called hopper is used.
When the raw material charged from the upper part of this is taken out from the lower part of it, the raw material easily adheres to the wall surface 7, and the fluidity of the raw material is poor, so that a bridge is formed as shown in the figure. Then it becomes blocked and unusable.

【0008】また、たとえ供給装置6の下部から原料が
排出されたとしても、この原料を容器4の広範な原料投
入領域の全域に均等に配分することは極めて困難であ
る。そして、供給装置6の下部から排出される原料を例
えば図示する如くに供給装置6の下方に設けた分配板8
によって配分する方法では、原料の流動性が悪く、然も
これが均一状態で流れないために、所要の目的を達成す
ることができない。
Further, even if the raw material is discharged from the lower portion of the supply device 6, it is extremely difficult to evenly distribute the raw material in the entire raw material charging area of the container 4. The raw material discharged from the lower part of the supply device 6 is provided below the supply device 6 as shown in FIG.
In the method of allocating by the method, the fluidity of the raw material is poor, and since it does not flow in a uniform state, the desired purpose cannot be achieved.

【0009】更に、このような供給装置6では、貯蔵部
5の中に在留する原料の量の多少、即ち原料自重の大小
の影響によって原料の排出量が大幅に変動してしまい、
一定量の原料を安定的に供給することができない。
Further, in such a supply device 6, the discharge amount of the raw material largely fluctuates due to the influence of the amount of the raw material staying in the storage section 5, that is, the weight of the raw material.
A certain amount of raw material cannot be stably supplied.

【0010】上述したような理由により、従来の原料供
給装置は振動造粒機に適応できず、振動造粒機を効果的
に稼働させるための原料分配供給装置の技術開発が急が
れていた。
Due to the above-mentioned reasons, the conventional raw material supplying device cannot be applied to the vibrating granulator, and the technical development of the raw material distributing and supplying device for effectively operating the vibrating granulator has been urgently required. ..

【0011】本発明は、振動造粒機の原料投入領域の全
域に、原料を均等に、かつ連続した略一定量で安定的に
分配供給することにより、粒径の揃った均質な粒状の製
品を効率良く、然も多量に生産可能とすることを目的と
する。
The present invention provides a uniform granular product having a uniform particle size by uniformly and stably supplying the raw material to the entire raw material charging area of the vibrating granulator in a continuous and substantially constant amount. The purpose is to be able to produce efficiently and in large quantities.

【0012】[0012]

【課題を解決するための手段】本発明は、湿潤原料を容
器に導入し、当該原料の排出方向に沿う方向における円
振動を付与し、該原料を転動塊成化しミニペレットを得
る振動造粒機の原料分配供給装置であって、湿潤原料を
搬送する原料搬入用ベルトコンベアと、原料搬入用ベル
トコンベアの出側に配置され、前記容器の原料投入領域
上にて揺動し得るホッパとを有して構成され、前記ホッ
パの内側面には、2本の原料搬出用ベルトコンベアを対
向配置し、両コンベアの下方に向けて移動する下行部の
間隔を下方に向けて小としてなるようにしたものであ
る。
According to the present invention, a wet raw material is introduced into a container, circular vibration is applied in a direction along the discharge direction of the raw material, and the raw material is tumbled and agglomerated to obtain mini-pellets. A raw material distribution and supply device of a granulator, a raw material carry-in belt conveyor that conveys a wet raw material, and a hopper that is arranged on the exit side of the raw material carry-in belt conveyor and that can swing on the raw material input area of the container. The inner surface of the hopper is provided with two belt conveyors for carrying out raw materials so as to face each other, and the distance between the descending parts moving downward of both conveyors is made smaller toward the lower side. It is the one.

【0013】[0013]

【作用】ホッパは、原料搬入用コンベアから搬入される
湿潤原料を分配供給するに際し、振動造粒機の容器の原
料投入領域上にて揺動し、原料を該原料投入領域の全域
に分配する。そして、ホッパから分配される原料は、該
ホッパ内面の2本の原料搬出用ベルトコンベアの下行部
間に挟まれて一定の流量で積極的に排出される。従っ
て、原料は、原料投入領域の全域に均等に、かつ連続し
た一定量で安定的に分配供給される。
The hopper swings on the raw material charging area of the container of the vibrating granulator when distributing and supplying the wet raw material carried in from the raw material carrying conveyor, and distributes the raw material throughout the raw material charging area. .. The raw material distributed from the hopper is sandwiched between the descending portions of the two raw material carrying-out belt conveyors on the inner surface of the hopper, and is positively discharged at a constant flow rate. Therefore, the raw material is stably and uniformly supplied to the entire raw material charging area in a uniform and continuous amount.

【0014】[0014]

【実施例】図1は本発明の一実施例に係る原料分配供給
装置を備えた振動造粒機を示す側面図、図2は図1の正
面図、図3は図1のIII −III 線に沿う矢視図、図4は
本発明が適用される焼結工程図、図5は攪拌混合機の一
例を示す模式図、図6は振動造粒機の一例を示す模式
図、図7は従来の原料供給装置を示す模式図である。
1 is a side view showing a vibrating granulator equipped with a raw material distributing and feeding device according to an embodiment of the present invention, FIG. 2 is a front view of FIG. 1, and FIG. 3 is a III-III line of FIG. FIG. 4 is a schematic view showing an example of a stirring mixer, FIG. 6 is a schematic view showing an example of a vibrating granulator, and FIG. 7 is a schematic view showing an example of a vibrating granulator. It is a schematic diagram which shows the conventional raw material supply apparatus.

【0015】本発明方法を用いたDL式焼結機のための
焼結プロセスでは、図4に示す如く、微粉鉱石槽1に装
入された微粉原料を下部コンスタントフィーダ2により
定量に切出し、これをベルトコンベア3で搬送し、この
原料を攪拌混合機4に供給し、適正造粒水分に調合、か
つ均一水分となるように攪拌混合する。更に、この原料
を後述する原料分配供給装置50にて振動造粒機5に供
給し、粒径 2〜10mmの収率が80重量%以上であるミニペ
レットを事前造粒する。他方、配合槽6の下部コンスタ
ントフィーダ7により定量に切出された通常の焼結原料
(返鉱、石灰石、コークス、粉鉱等)を、ベルトコンベ
ア8上で多層積み配合した後、ドラム形ミキサ9にて原
料全体の水分が 5〜 7%になるように水分を添加し、ド
ラムの回転により混合、転動造粒し、給鉱ホッパー10
へ搬送し、ドラムフィーダ11にて定量切出す。そし
て、前記振動造粒されたミニペレットと2次配合原料を
ベルトシュート12上で混合し、DL式焼結機13のパ
レット14へ装入した後、点火炉15にて原料中のコー
クスに着火し焼結する。
In the sintering process for the DL type sintering machine using the method of the present invention, as shown in FIG. 4, the fine powder raw material charged in the fine powder ore tank 1 is cut out in a fixed amount by the lower constant feeder 2 and Is conveyed by a belt conveyor 3 and this raw material is supplied to a stirring and mixing machine 4 to be mixed with proper granulation water and stirred and mixed so as to obtain a uniform water content. Further, this raw material is supplied to a vibrating granulator 5 by a raw material distribution and supply device 50 described later to pre-granulate mini pellets having a particle size of 2 to 10 mm and a yield of 80% by weight or more. On the other hand, ordinary sintering raw materials (returned ore, limestone, coke, powder ore, etc.) quantitatively cut by the lower constant feeder 7 of the compounding tank 6 are layered and mixed on the belt conveyor 8 and then mixed in a drum mixer. At 9, the water is added so that the water content of the whole raw material becomes 5 to 7%, and the mixture is tumbled and granulated by rotating the drum, and the ore feeding hopper 10
To a drum feeder 11 and cut out quantitatively. Then, the vibration-granulated mini-pellets and the secondary blended raw material are mixed on the belt chute 12 and charged into the pallet 14 of the DL type sintering machine 13, and then the coke in the raw material is ignited in the ignition furnace 15. And sinter.

【0016】ここで、上記攪拌混合機4は図5に示す如
くである。即ち、攪拌混合機4は、台座16を介し架台
17に固定された双U形容器18内に、 2本の互いに反
対方向(上半部が外向きの回転)に回転する螺旋羽根軸
19、20を並設し、該螺旋羽根軸19、20に攪拌用
の羽根21を螺旋状に固着している。各螺旋羽根軸1
9、20はそれらの両側軸端部を軸受22に支承され、
給鉱側の軸端部には軸継手23を介し、駆動用モータ2
4が接続されている。また、双U形容器18の螺旋羽根
軸19、20始端側には原料投入口25を設け、螺旋羽
根軸19、20終端側には原料排出口26を設け、また
原料投入口25の下流側には加湿装置27を設けてい
る。
Here, the stirring and mixing machine 4 is as shown in FIG. That is, the agitator-mixer 4 has two twin U-shaped containers 18 fixed to a pedestal 17 via a pedestal 16 and two spiral blade shafts 19, which rotate in mutually opposite directions (the upper half is rotated outward). 20 are arranged in parallel, and stirring blades 21 are spirally fixed to the spiral blade shafts 19 and 20. Each spiral blade shaft 1
9 and 20 are supported by bearings 22 at their both shaft ends,
The drive motor 2 is connected to the shaft end on the mining side via a shaft coupling 23.
4 is connected. Further, a raw material inlet 25 is provided on the start side of the spiral blade shafts 19 and 20 of the twin U-shaped container 18, a raw material outlet 26 is provided on the end side of the spiral blade shafts 19 and 20, and the downstream side of the raw material inlet 25. A humidifier 27 is provided in the.

【0017】また、上記振動造粒機5は図1〜図3に示
す如くである。即ち、振動造粒機5は、架台30上に、
軸受31、32を介して、 2本の偏心軸33、34を軸
支し、それらの偏心軸33、34により複数の広幅角ト
ラフ状の平板状底面容器35を多段多列状態で支持す
る。尚、36はブラケット、37は連結ピンである。
The vibrating granulator 5 is as shown in FIGS. That is, the vibration granulator 5 is mounted on the pedestal 30.
Two eccentric shafts 33 and 34 are axially supported via bearings 31 and 32, and the eccentric shafts 33 and 34 support a plurality of wide-angle trough-shaped flat plate bottom containers 35 in a multi-stage multi-row state. Incidentally, 36 is a bracket and 37 is a connecting pin.

【0018】即ち、振動造粒機5は、一端に原料投入部
35A、他端に原料排出部35Bを形成し、水平面内に
配置された 2本の同位相で、かつ同振幅で矢印で示す方
向に回転駆動される 2本の偏芯軸33、34上に積載さ
れたトラフ状容器35を、上下方向に複数段、横方向に
複数列密接して並設した構造になっている。
That is, the vibrating granulator 5 has a raw material feeding section 35A at one end and a raw material discharging section 35B at the other end, and two arrows arranged in the horizontal plane have the same phase and the same amplitude as indicated by arrows. The structure is such that trough-shaped containers 35 loaded on two eccentric shafts 33 and 34 that are rotationally driven in the direction are closely arranged side by side in a plurality of stages in the vertical direction and in a plurality of rows in the lateral direction.

【0019】そして、偏芯軸33は軸継手38を介して
駆動用モータ39にて駆動され、偏芯軸34はタイミン
グベルト41を介して偏心軸33と同期駆動せしめられ
る。これにより、振動造粒機5は、容器35内の原料に
偏心軸33、34による振動加速度3G〜 10Gの当該原料
の排出方向に沿う方向における円振動(振幅10〜30mm、
振動数 600〜1000回/分)を付与する。
The eccentric shaft 33 is driven by a drive motor 39 via a shaft joint 38, and the eccentric shaft 34 is driven synchronously with the eccentric shaft 33 via a timing belt 41. As a result, the vibrating granulator 5 causes the raw material in the container 35 to have a circular vibration (amplitude 10 to 30 mm;
Vibration frequency of 600 to 1000 times / min.

【0020】このとき、平板状底面容器35は、ブラケ
ット36に略水平支持され、前述の偏心軸33、34の
図1における時計方向回りの方向の円振動を付与される
状態下で、原料投入部35Aから原料を供給され、この
原料を原料排出部35Bの側へ給送せしめる。ここで、
容器35内の原料は、その層厚を15mm以下とするように
設定されている。これにより、容器35の原料投入部3
5Aから装入された、所要の湿り程度に加湿混合された
湿潤原料は、振幅10〜30mmの円振動を 4秒以上付与さ
れ、この円振動の働きによって上方向に放り上げられ、
そして落下し、更に自転運動を繰り返し与えられなが
ら、原料排出部35Bの側に位相されていき、この間に
転動塊成化され、ミニペレットとなる。
At this time, the flat bottom container 35 is supported substantially horizontally by the bracket 36, and the raw material is charged under the condition that the aforementioned eccentric shafts 33, 34 are circularly oscillated in the clockwise direction in FIG. The raw material is supplied from the portion 35A, and the raw material is fed to the raw material discharge portion 35B. here,
The raw material in the container 35 is set to have a layer thickness of 15 mm or less. Thereby, the raw material charging section 3 of the container 35
The wet raw material charged from 5A and humidified and mixed to the required degree of wetness is given a circular vibration with an amplitude of 10 to 30 mm for 4 seconds or more, and is thrown upward by the action of this circular vibration.
Then, it falls, and while being repeatedly given a rotation motion, it is phased to the side of the raw material discharge part 35B, and during this time, it is rolling agglomerated and becomes a mini pellet.

【0021】尚、平板状底面容器35は、原料投入部3
5Aから原料排出部35Bの側に向けて例えば10度の下
り勾配を付与され、かつ反時計方向の円振動を付与され
るものであっても良い。これによれば、容器35内にお
いて、細粒は原料投入部35A側に移動し、攪拌されて
核粒子となり、他方、成長した粒子は重力により原料排
出部35B側に移動し、粒度を揃えられる状態で排出さ
れることとなる。
The flat bottom container 35 is provided in the raw material charging section 3
For example, a downward gradient of 10 degrees may be applied from 5A toward the raw material discharge part 35B, and counterclockwise circular vibration may be applied. According to this, in the container 35, the fine particles move to the raw material feeding part 35A side and are agitated to become core particles, while the grown particles move to the raw material discharging part 35B side by gravity, and the particle size is made uniform. It will be discharged in the state.

【0022】然るに、本実施例においては、攪拌混合機
4により攪拌混合された湿潤原料を、振動造粒機5に供
給するため、図1、図2に示す如くの原料分配供給装置
50を備えている。即ち、原料分配供給装置50は、予
め所要の湿り具合になるように加湿混合された原料を振
動造粒機5の各原料投入部35Aに分配供給する。
However, in this embodiment, in order to supply the wet raw material which is agitated and mixed by the agitating and mixing machine 4 to the vibrating granulator 5, a raw material distribution and supply device 50 as shown in FIGS. 1 and 2 is provided. ing. That is, the raw material distribution / supply device 50 distributes and supplies the raw materials that are preliminarily humidified and mixed so as to have a desired wetness condition, to the respective raw material charging sections 35A of the vibrating granulator 5.

【0023】原料分配供給装置50は、攪拌混合機4と
振動造粒機5との間に配置され、原料搬入用コンベア5
1と、ホッパ52とを有して構成されている。
The raw material distribution / supply device 50 is arranged between the agitating mixer 4 and the vibrating granulator 5, and the raw material carrying conveyor 5 is provided.
1 and a hopper 52.

【0024】原料搬入用コンベア51は攪拌混合機4の
原料排出口26から供給される湿潤原料を、ホッパ52
に向けて搬送する。
The raw material carrying conveyer 51 feeds the wet raw material supplied from the raw material discharge port 26 of the agitating mixer 4 to the hopper 52.
Transport it to.

【0025】ホッパ52は原料搬入用コンベア51の出
側において、架台53上の軸受54、54にピン55を
介して吊下げ支持され、振動造粒機5の容器35の原料
投入部35Aの全域上方にて揺動し得る。ホッパ52の
揺動装置56は、架台53に固定されるモータ57と、
モータ57にて駆動されるクランク装置58とから構成
される。
The hopper 52 is hung and supported by bearings 54, 54 on a pedestal 53 via pins 55 on the exit side of the raw material carry-in conveyor 51, and the entire area of the raw material charging section 35A of the container 35 of the vibration granulator 5 is covered. It can rock up. The swing device 56 of the hopper 52 includes a motor 57 fixed to the pedestal 53,
It is composed of a crank device 58 driven by a motor 57.

【0026】ホッパ52の内側面には、2本の原料搬出
用ベルトコンベア61、61が対向配置されており、両
原料搬出用ベルトコンベア61、61の下方に向けて移
動する下行部61A、61Aの間隔は、下方に向けて次
第に小(幅狭)となるように設定されている。62はコ
ンベア駆動モータである。63はシュートである。
On the inner surface of the hopper 52, two raw material unloading belt conveyors 61, 61 are arranged so as to face each other, and the descending parts 61A, 61A which move toward the lower side of both raw material unloading belt conveyors 61, 61. The interval is set to be gradually smaller (narrower) downward. 62 is a conveyor drive motor. 63 is a shoot.

【0027】分配供給装置50にあっては、攪拌混合機
4にて適正な水分を点火され、均一に混合された湿潤原
料が、原料排出口26から、原料搬入用コンベア51に
供給される。この原料は、容器35の原料投入部35A
の全域上方にて揺動するホッパ52に搬入され、該ホッ
パ52の相対する原料搬出用ベルトコンベア61、61
間に挟まれながら、原料投入部35Aの全域に分配され
る。
In the distribution and supply device 50, the proper raw material is ignited by the agitation mixer 4 and the uniformly mixed wet raw material is supplied from the raw material discharge port 26 to the raw material carrying conveyor 51. This raw material is stored in the raw material charging section 35A of the container 35.
Is conveyed into the hopper 52 that swings above the entire area of the hopper 52, and the raw material unloading belt conveyors 61, 61 facing the hopper 52 are conveyed.
While being sandwiched between them, it is distributed throughout the raw material charging section 35A.

【0028】以下、本実施例の作用について説明する。
ホッパ52は、原料搬入用コンベア51から搬入される
湿潤原料を分配供給するに際し、振動造粒機5の容器3
5の原料投入領域上にて揺動し、原料を該原料投入領域
の全域に分配する。そして、ホッパ52から分配される
原料は、該ホッパ52内面の2本の原料搬出用ベルトコ
ンベア61、61の下行部61A、61A間に挟まれて
一定の流量で積極的に排出される。従って、原料は、原
料投入領域の全域に均等に、かつ連続した一定量で安定
的に分配供給される。
The operation of this embodiment will be described below.
The hopper 52 distributes and supplies the wet raw material carried in from the raw material carrying-in conveyor 51, and the container 3 of the vibrating granulator 5
The raw material is distributed over the entire raw material charging area by rocking on the raw material charging area 5. The raw material distributed from the hopper 52 is sandwiched between the two raw material unloading belt conveyors 61, 61 on the inner surface of the hopper 52 and is positively discharged at a constant flow rate. Therefore, the raw material is stably distributed evenly and continuously in a constant amount throughout the raw material charging area.

【0029】本発明による原料分配供給装置50は上述
したように、原料を振動造粒機5の原料投入領域の広い
範囲(複数の原料投入部35A)に安定して均一に分配
することができ、振動造粒機5の性能向上及び生産性ア
ップを図ることができ、これの実用的効果は大なるもの
である。
As described above, the raw material distribution / supplying device 50 according to the present invention can stably and uniformly distribute the raw material to a wide range (a plurality of raw material feeding portions 35A) of the raw material feeding region of the vibrating granulator 5. The performance and productivity of the vibrating granulator 5 can be improved, and the practical effect thereof is great.

【0030】[0030]

【発明の効果】以上のように本発明によれば、振動造粒
機の原料投入領域の全域に、原料を均等に、かつ連続し
た略一定量で安定的に分配供給することにより、粒径の
揃った均質な粒状の製品を効率良く、然も多量に生産可
能とすることができる。
As described above, according to the present invention, it is possible to stably and uniformly distribute and feed the raw material to the entire area of the raw material charging area of the vibrating granulator so that the particle size can be improved. It is possible to efficiently and uniformly produce a uniform granular product with uniform production.

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

【図1】図1は本発明の一実施例に係る原料分配供給装
置を備えた振動造粒機を示す側面図である。
FIG. 1 is a side view showing a vibrating granulator equipped with a raw material distribution and supply device according to an embodiment of the present invention.

【図2】図2は図1の正面図である。FIG. 2 is a front view of FIG.

【図3】図3は図1のIII −III 線に沿う矢視図であ
る。
FIG. 3 is a view taken along the line III-III in FIG.

【図4】図4は本発明が適用される焼結工程図である。FIG. 4 is a sintering process diagram to which the present invention is applied.

【図5】図5は攪拌混合機の一例を示す模式図である。FIG. 5 is a schematic diagram showing an example of a stirring mixer.

【図6】図6は振動造粒機の一例を示す模式図である。FIG. 6 is a schematic diagram showing an example of a vibrating granulator.

【図7】図7は従来の原料供給装置を示す模式図であ
る。
FIG. 7 is a schematic view showing a conventional raw material supply device.

【符号の説明】[Explanation of symbols]

5 振動造粒機 35 容器 35A 原料投入部 50 原料分配供給装置 51 原料搬入用コンベア 52 ホッパ 61 原料搬出用ベルトコンベア 61A 下行部 5 Vibratory Granulator 35 Container 35A Raw Material Feeding Section 50 Raw Material Distributing and Supplying Device 51 Raw Material Carrying Conveyor 52 Hopper 61 Raw Material Carrying Out Belt Conveyor 61A Descending Part

───────────────────────────────────────────────────── フロントページの続き (72)発明者 末森 ▲あきら▼ 岡山県倉敷市水島川崎通1丁目(番地な し) 川崎製鉄株式会社水島製鉄所内 (72)発明者 藤井 紀文 岡山県倉敷市水島川崎通1丁目(番地な し) 川崎製鉄株式会社水島製鉄所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Suemori ▲ Akira ▼ 1-chome, Mizushima Kawasaki-dori, Kurashiki-shi, Okayama Prefecture (no address) Inside the Mizushima Steel Works, Kawasaki Steel Co., Ltd. Tsudori 1-chome (No house number) Kawasaki Steel Co., Ltd. Mizushima Works

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 湿潤原料を容器に導入し、当該原料の排
出方向に沿う方向における円振動を付与し、該原料を転
動塊成化しミニペレットを得る振動造粒機の原料分配供
給装置であって、湿潤原料を搬送する原料搬入用ベルト
コンベアと、原料搬入用ベルトコンベアの出側に配置さ
れ、前記容器の原料投入領域上にて揺動し得るホッパと
を有して構成され、前記ホッパの内側面には、2本の原
料搬出用ベルトコンベアを対向配置し、両コンベアの下
方に向けて移動する下行部の間隔を下方に向けて小とし
てなることを特徴とする振動造粒機の原料分配供給装
置。
1. A raw material distribution and supply device of a vibrating granulator which introduces a wet raw material into a container, imparts circular vibration in a direction along the discharge direction of the raw material, and roll-agglomerates the raw material to obtain mini pellets. There is a raw material carry-in belt conveyor that conveys a wet raw material, and is configured to have a hopper that is arranged on the exit side of the raw material carry-in belt conveyor and that can swing in the raw material charging area of the container, On the inner surface of the hopper, two belt conveyors for carrying out raw materials are arranged so as to oppose each other, and the distance between the descending parts moving downward of both conveyors is made smaller toward the lower side. Raw material distribution and supply device.
JP35653791A 1991-12-25 1991-12-25 Device for distributing and supplying raw material in vibrating granulator Withdrawn JPH05168899A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35653791A JPH05168899A (en) 1991-12-25 1991-12-25 Device for distributing and supplying raw material in vibrating granulator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35653791A JPH05168899A (en) 1991-12-25 1991-12-25 Device for distributing and supplying raw material in vibrating granulator

Publications (1)

Publication Number Publication Date
JPH05168899A true JPH05168899A (en) 1993-07-02

Family

ID=18449521

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35653791A Withdrawn JPH05168899A (en) 1991-12-25 1991-12-25 Device for distributing and supplying raw material in vibrating granulator

Country Status (1)

Country Link
JP (1) JPH05168899A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0727250A2 (en) * 1995-02-16 1996-08-21 Japan Energy Corporation Method of packing particles into vessels and apparatus therefor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0727250A2 (en) * 1995-02-16 1996-08-21 Japan Energy Corporation Method of packing particles into vessels and apparatus therefor
EP0727250A3 (en) * 1995-02-16 1998-05-20 Japan Energy Corporation Method of packing particles into vessels and apparatus therefor

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