JPH02229540A - Control device for disk pelletizer - Google Patents
Control device for disk pelletizerInfo
- Publication number
- JPH02229540A JPH02229540A JP5057389A JP5057389A JPH02229540A JP H02229540 A JPH02229540 A JP H02229540A JP 5057389 A JP5057389 A JP 5057389A JP 5057389 A JP5057389 A JP 5057389A JP H02229540 A JPH02229540 A JP H02229540A
- Authority
- JP
- Japan
- Prior art keywords
- disk pelletizer
- pelletizer
- disk
- angle
- ultrasonic level
- 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
Links
- 239000002994 raw material Substances 0.000 claims abstract description 18
- 238000005259 measurement Methods 0.000 claims abstract description 4
- 230000014759 maintenance of location Effects 0.000 claims description 5
- 239000008188 pellet Substances 0.000 abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 4
- 239000004449 solid propellant Substances 0.000 abstract description 4
- 238000005245 sintering Methods 0.000 abstract description 3
- 239000002245 particle Substances 0.000 description 6
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 3
- 235000012255 calcium oxide Nutrition 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012256 powdered iron Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
- Glanulating (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
原料条件の変化に対応して、ディスクペレタイザー傾斜
角度および回転数を変えるディスクペレタイザー制御装
置に関する.
[従来の技術]
粉鉄鉱石等の粒状化にディスクベレタイザ=が広く使用
されている.ディスクペレタイザーでは、原料条件(銘
柄、水分、バインダーに添加率等)や原料の供給量が変
化したとき、生ベレットの粒度(または粒度範囲)を一
定に保つため、傾斜角度と回転数を調整する.そして、
作業者が製造される生ペレットの粒径を見ながら、この
調整を行っている.
[発明が解決しようとする課題]
製造される生ベレットの粒度を見ながら作業者が行う従
来の調整方法は、作業者の経験と勘をたよりに行うため
、どうしてもオーバーアクションになりがちで、!ll
II!操作を数回繰り返すことになり、長時間を要する
という問題点がある.[課題を解決するための手段]
この発明は以上の問題点を解決しようとするもので、デ
ィスクペレタイザーの原料滞留面の上方に問隔をもって
設けた少なくとも2個の超音波レベル計と、該超音波レ
ベル計の測定信号、ディスクペレタイザーの傾動装置か
らのディスクペレタイザー傾斜角度信号およびディスク
ベレタイザの回転駆動装置からの回転数信号に基づいて
、設定保有菫となるディスクペレタイザー傾斜角度と、
該ディスクペレタイザー傾斜角度のときの最適回転数を
求め、ディスクペレタイザーの傾動装置と回転駆動装置
に送信する演i器とからなるディスクペレタイザー制御
装置である.[作用]
演算器が超音波レベル計の測定値から原料の安息角を求
め、目標保有量になるディスクペレタイザーの傾斜角度
とその傾斜角度に対する最適回転数を求めて、ディスク
ペレタイザーの傾斜角度と回転数をディスクペレタイザ
ーの傾動装置および回転駆動装置に指令する.従って、
原料条件や原料の供給量に変化があると自動的に、短時
間で調!1操作が行われる.
〔実施例]
本発明の実施例を塊成鉱製造におけるディスクペレタイ
ザーを例として以下に説明する.第3図は生ベレットの
製造から焼結機への装入までの工程を示す図である.1
は−44μ粒度40〜50%以上のべレットフィードの
貯槽、2は−8■騰粒度の粉粒鉄鉱石の貯槽、3は塊成
鉱の破砕、整粒過程で発生する返鉱の貯槽、4はバイン
ダーとしての生石灰の貯槽である.各槽から切り出され
た原料は、ドラムミキサー5で水を添加しながら混合さ
れ、ディスクベレタイザ−6に供給される.ディスクベ
レタイザ−6では、水を添加しながら5〜10龍粒度の
生ベレットが製造される.生ベレットは二次ドラムミキ
サー7に供給される.二次ドラムミキサー7で、粉状固
体燃料の貯槽8がら切り出された粉状固体燃料が生ペレ
ットの表面に被覆される.粉状固体燃料が被覆された生
ペレットは、往復動ベルトコンベア9、装入ベルトコン
ベア10を介して焼結1fillに供給される.そして
、塊成鉱の品質〈タンブラー強度、成品粒度等》が低下
した場合、品質の回復を計るためバインダー(生石灰)
の添加率や添加水の量が変更される.これらの変更が行
われると原料の安息角が変わるため、ディスクベレタイ
ザ−6の傾斜角度および回転数の調整が行われる.
第1図は本発明のディスクペレタイザー制御装置のブロ
ック図、第2図は超音波レベル計を取付けたディスクペ
レタイザーを示す図である 21は原料滞留面の上方に
所定の間隔をもって設けた超音波レベル計で、原料の安
息角をもとめる基になる原料滞留面からレベル計までの
高さhを測定するためのものである.第2図では2個設
けてある.なお、3個以上設ければ原料の安息角がより
精度よく求められる.22は演算器で、(1) 超音
波レベル計21の測定値h,,h2および超音波レベル
計21、21の間隔ρから原料の安息角αを計算し,デ
ィスクペレタイザーの傾斜角θ(θ=α+β:ここにβ
は保有角で設定値)を求める.
■ ディスクペレタイザーの傾斜角θが求まれば5ディ
スクペレタイザーの最適回転数nは次式より求まる,
n =N c Xν;ここにN0はディスクペレタイザ
ーの臨界回転数で、ペレタイザーの角度と直径の関数で
Nc+ =42.3XnXSinθ/Dと表され一定数
である.また,νは比回転数で、v = n / N
oと表され、0.4〜0.75が適正値とされている.
すなわち、
0.4XN.<n<0.75N,
となるようにnを調整してやればよいことになる.求め
たディスクペレタイザーの傾斜角θおよびディスクペレ
タイザーの最適回転数nをディスクペレタイザ−6に送
信する.61はディスクペレタイザーの傾斜角を変える
傾動装置,62はディスクペレタイザーの回転数を変え
る回転駆動装置である.
そして、傾動装置61は演算器22からディスクベレタ
イザ−6の保有角βを一定にする(保有量が一定)傾斜
角θを受信して、当該角度に変更する.回転駆動装置6
2は演算822からディスクベレタイザ−6の最適回転
数(傾斜角θのときの》を受信して、当該回転数に変更
する.従って、生ベレットの粒度(または、粒度範囲)
と強度が維持される.
[発明の効果]
本発明は、原料条件が変わった場合、ディスクペレタイ
ザーの原料滞留面の上方に設けた複数の超音波レベル計
と演算器により、ディスクペレタイザーの傾斜角および
回転数を自動的に、最適値に変更するものであるから、
短時間に、且つ正確に変更され、塊成鉱の品質を悪化さ
せることがなくなるという効果がある.
ある.
6・・・ディスクペレタイザーDetailed Description of the Invention [Field of Industrial Application] This invention relates to a disk pelletizer control device that changes the disk pelletizer inclination angle and rotation speed in response to changes in raw material conditions. [Conventional technology] Disc beretizers are widely used for granulating powdered iron ore. In a disk pelletizer, when the raw material conditions (brand, moisture, binder addition rate, etc.) or raw material supply amount change, the inclination angle and rotation speed are adjusted to keep the particle size (or particle size range) of the green pellets constant. .. and,
The operator makes this adjustment while observing the particle size of the raw pellets being manufactured. [Problem to be solved by the invention] The conventional adjustment method, in which the operator performs the adjustment while observing the grain size of the raw pellets being manufactured, relies on the operator's experience and intuition, which tends to result in overaction. ll
II! The problem is that the operation has to be repeated several times and it takes a long time. [Means for Solving the Problems] The present invention aims to solve the above-mentioned problems, and includes at least two ultrasonic level meters disposed at a distance above the raw material retention surface of a disk pelletizer, and the ultrasonic level meters. Based on the measurement signal of the sonic level meter, the disk pelletizer inclination angle signal from the disk pelletizer tilting device, and the rotation speed signal from the disk pelletizer rotational drive device, the disk pelletizer inclination angle is set to a predetermined value;
This is a disk pelletizer control device consisting of an operator which determines the optimum rotational speed at the disk pelletizer inclination angle and transmits the data to the disk pelletizer tilting device and rotary drive device. [Operation] The computing unit calculates the angle of repose of the raw material from the measurement value of the ultrasonic level meter, calculates the angle of inclination of the disc pelletizer to achieve the target holding amount, and the optimum rotation speed for that angle of inclination, and adjusts the angle of inclination and rotation of the disc pelletizer. The number is commanded to the tilting device and rotary drive device of the disk pelletizer. Therefore,
Automatically adjusts in a short time when there are changes in raw material conditions or raw material supply amount! 1 operation is performed. [Example] An example of the present invention will be described below using a disk pelletizer for producing agglomerated ore as an example. Figure 3 shows the process from producing green pellets to charging them into the sintering machine. 1
2 is a storage tank for pellet feed with a grain size of -44μ of 40 to 50% or more, 2 is a storage tank for powdered iron ore with a grain size of -8μ, 3 is a storage tank for return ore generated during the crushing of agglomerate ore, and the sizing process. 4 is a storage tank for quicklime as a binder. The raw materials cut out from each tank are mixed in a drum mixer 5 while adding water, and then supplied to a disc beletizer 6. In the disk beretizer 6, green pellets with a grain size of 5 to 10 grains are produced while adding water. The raw pellets are fed to a secondary drum mixer 7. In the secondary drum mixer 7, the surface of the green pellets is coated with the powdered solid fuel cut out from the powdered solid fuel storage tank 8. The raw pellets coated with powdered solid fuel are supplied to sintering 1fill via a reciprocating belt conveyor 9 and a charging belt conveyor 10. If the quality of the agglomerate (tumbler strength, finished product particle size, etc.) deteriorates, a binder (quicklime) is added to restore the quality.
The addition rate and amount of added water are changed. When these changes are made, the angle of repose of the raw material changes, so the inclination angle and rotation speed of the disc beletizer 6 are adjusted. Fig. 1 is a block diagram of the disc pelletizer control device of the present invention, and Fig. 2 is a diagram showing a disc pelletizer equipped with an ultrasonic level meter. 21 is an ultrasonic level provided at a predetermined interval above the raw material retention surface. It is used to measure the height h from the raw material retention surface to the level meter, which is the basis for determining the angle of repose of the raw material. In Figure 2, two are provided. Note that if three or more are provided, the angle of repose of the raw material can be determined more accurately. 22 is a computing unit that (1) calculates the angle of repose α of the raw material from the measured values h, , h2 of the ultrasonic level meter 21 and the interval ρ between the ultrasonic level meters 21 and 21, and calculates the angle of repose α of the disc pelletizer θ (θ = α + β: β here
is the holding angle). ■ Once the inclination angle θ of the disc pelletizer is determined, the optimal rotation speed n of the 5-disc pelletizer can be determined from the following formula,
n = N c Also, ν is the specific rotation speed, v = n / N
o, and 0.4 to 0.75 is considered an appropriate value.
That is, 0.4XN. All you have to do is adjust n so that <n<0.75N. The obtained inclination angle θ of the disk pelletizer and the optimum rotation speed n of the disk pelletizer are sent to the disk pelletizer-6. 61 is a tilting device that changes the inclination angle of the disk pelletizer, and 62 is a rotation drive device that changes the rotation speed of the disk pelletizer. Then, the tilting device 61 receives the tilt angle θ that makes the holding angle β of the disk beletizer 6 constant (the holding amount is constant) from the calculator 22, and changes it to the angle. Rotary drive device 6
2 receives the optimum rotation speed (when the inclination angle θ) of the disc beletizer 6 from the operation 822 and changes it to the rotation speed. Therefore, the particle size (or particle size range) of the raw pellet
and strength is maintained. [Effects of the Invention] When the raw material conditions change, the present invention automatically adjusts the inclination angle and rotation speed of the disc pelletizer using a plurality of ultrasonic level meters and a calculator provided above the raw material retention surface of the disc pelletizer. , since it changes to the optimal value,
The effect is that the changes can be made quickly and accurately, and the quality of the agglomerate ore will not deteriorate. be. 6...Disc pelletizer
Claims (1)
って設けた少なくとも2個の超音波レベル計と、該超音
波レベル計の測定信号、ディスクペレタイザーの傾動装
置からのディスクペレタイザー傾斜角度信号およびペレ
タイザーの回転駆動装置からの回転数信号に基ずいて、
設定保有量となるディスクペレタイザー傾斜角度と、該
ディスクペレタイザー傾斜角度のときの最適回転数を求
め、ディスクペレタイザーの傾動装置と回転駆動装置に
送信する演算器とからなるディスクペレタイザー制御装
置。At least two ultrasonic level meters provided at a distance above the raw material retention surface of the disk pelletizer, measurement signals from the ultrasonic level meters, a disk pelletizer tilt angle signal from a disk pelletizer tilting device, and a pelletizer rotation drive device. Based on the rotation speed signal from
A disk pelletizer control device comprising a calculation unit that determines a disk pelletizer inclination angle that is a set holding amount and an optimum rotation speed at the disk pelletizer inclination angle and sends the information to a disk pelletizer tilting device and rotation drive device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5057389A JPH02229540A (en) | 1989-03-02 | 1989-03-02 | Control device for disk pelletizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5057389A JPH02229540A (en) | 1989-03-02 | 1989-03-02 | Control device for disk pelletizer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02229540A true JPH02229540A (en) | 1990-09-12 |
Family
ID=12862738
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5057389A Pending JPH02229540A (en) | 1989-03-02 | 1989-03-02 | Control device for disk pelletizer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02229540A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100723213B1 (en) * | 2005-11-15 | 2007-05-29 | 주식회사 포스코 | Double Disc Type Granulator |
JP2015067879A (en) * | 2013-09-30 | 2015-04-13 | 株式会社Ihi | Manufacturing method of electrode for discharge surface treatment, and discharge surface treatment method |
JP2015188788A (en) * | 2014-03-27 | 2015-11-02 | 株式会社神戸製鋼所 | Method for estimating particle size and standard deviation of granules, and method for controlling granulation process |
CN106521147A (en) * | 2017-01-09 | 2017-03-22 | 中冶北方(大连)工程技术有限公司 | Pelletizing disc control system and method |
-
1989
- 1989-03-02 JP JP5057389A patent/JPH02229540A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100723213B1 (en) * | 2005-11-15 | 2007-05-29 | 주식회사 포스코 | Double Disc Type Granulator |
JP2015067879A (en) * | 2013-09-30 | 2015-04-13 | 株式会社Ihi | Manufacturing method of electrode for discharge surface treatment, and discharge surface treatment method |
JP2015188788A (en) * | 2014-03-27 | 2015-11-02 | 株式会社神戸製鋼所 | Method for estimating particle size and standard deviation of granules, and method for controlling granulation process |
CN106521147A (en) * | 2017-01-09 | 2017-03-22 | 中冶北方(大连)工程技术有限公司 | Pelletizing disc control system and method |
CN106521147B (en) * | 2017-01-09 | 2018-05-25 | 中冶北方(大连)工程技术有限公司 | A kind of pelletizing disk control system and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPH02229540A (en) | Control device for disk pelletizer | |
JPS61278363A (en) | Two-stage crushing method and apparatus for crushing fragilematerial | |
US5102586A (en) | Agglomerating process of sinter mix and apparatus therefor | |
JP2000279788A (en) | Rotary pan type granulator, and production of granular material using the same | |
JPH0742521B2 (en) | Sintered raw material granulator | |
US4648900A (en) | Suction sintering method and apparatus therefor | |
US3060496A (en) | Apparatus for making nodules or pellets | |
JPH11262650A (en) | Automatic granulating apparatus for powder | |
JP3345723B2 (en) | Fluidized bed or tumbling fluidized bed granulator | |
SU1146084A1 (en) | System for automatic controlling of grinding complex | |
JPH0436422A (en) | Method for pelletizing sintering raw material | |
JPS62502030A (en) | drum for agglomeration | |
GB1429418A (en) | Method and apparatus for metering particulate material | |
RU2026378C1 (en) | Method for control of pelletizing process in pan granulator | |
JPH0551654A (en) | Pretreatment and granulating method for raw material to be sintered | |
SU842109A1 (en) | Method of pelletizing agglomeration charge | |
JPH02173220A (en) | Method for controlling permeability on pallet in sintering machine | |
JPS6326164B2 (en) | ||
JPS597500B2 (en) | Stirred fluidized bed equipment | |
JPH0472796B2 (en) | ||
SU1079292A1 (en) | Method of regulation of charging cone-type crusher | |
JP2004301368A (en) | Device for charging raw material to be sintered | |
JPS6250402A (en) | Method for charging raw material to blast furnace | |
JPH02102724A (en) | Production of pellet with vibrating mill | |
JPS5938289B2 (en) | Method for producing sintered ore |