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JPS5820858B2 - How to control the amount of powder cut out - Google Patents
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JPS5820858B2 - How to control the amount of powder cut out - Google Patents

How to control the amount of powder cut out

Info

Publication number
JPS5820858B2
JPS5820858B2 JP52037223A JP3722377A JPS5820858B2 JP S5820858 B2 JPS5820858 B2 JP S5820858B2 JP 52037223 A JP52037223 A JP 52037223A JP 3722377 A JP3722377 A JP 3722377A JP S5820858 B2 JPS5820858 B2 JP S5820858B2
Authority
JP
Japan
Prior art keywords
powder
amount
water
moisture
containing powder
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
JP52037223A
Other languages
Japanese (ja)
Other versions
JPS53122491A (en
Inventor
吉岡博行
小山朝良
徳田将敏
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP52037223A priority Critical patent/JPS5820858B2/en
Publication of JPS53122491A publication Critical patent/JPS53122491A/en
Publication of JPS5820858B2 publication Critical patent/JPS5820858B2/en
Expired legal-status Critical Current

Links

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  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
  • Control Of Conveyors (AREA)

Description

【発明の詳細な説明】 本発明は高炉の媒溶剤として用いる石灰粉末等の水分を
含む粉体の切出し量制御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the amount of powder containing water, such as lime powder, used as a solvent in a blast furnace.

焼結原料中の石灰石量は焼結鉱の塩基度を左右する重要
な因子であるから、その添加量は正確に制御されなけれ
ばならない。
Since the amount of limestone in the sintering raw material is an important factor that influences the basicity of the sintered ore, the amount added must be accurately controlled.

そこで、原料ホッパから石灰粉末を切出すlこ際してt
t’i該石灰粉石灰粉末値を測定して見掛けの切出し量
を補正する必要がある。
Therefore, lime powder is cut out from the raw material hopper.
It is necessary to measure the lime powder value and correct the apparent cutting amount.

従来は、石灰石中の水分変動が余り大きくないため、乾
燥法による間欠測定によって水分値の補正をするだけで
十分であったが、近頃では粉塵公害を防止する目的で石
灰石に対する散水が頻繁に行われるため、石灰石中の水
分値の変動が大きくなり、そこで水分値の連続測定を行
う必要を生ずるようになった。
In the past, since moisture fluctuations in limestone were not so large, it was sufficient to correct the moisture value by intermittent measurements using the drying method, but recently limestone has been frequently sprinkled with water to prevent dust pollution. As a result, the moisture value in limestone fluctuates greatly, making it necessary to continuously measure the moisture value.

そのため、近時、中性子水分計を用いる水分値の連続測
定が行われているが、この測定方法には安全管理が煩雑
であること、保守が困難であること、測定精度が悪いこ
と等の欠点があるほか、測定器の保護管が原料粉末中に
挿入されているため、原料の保護管への付着、滞溜によ
り誤差を生じ易い等の欠点もあり、これらの欠点の改善
が求められていた。
Therefore, in recent years, continuous measurement of moisture values using neutron moisture meters has been carried out, but this measurement method has drawbacks such as complicated safety management, difficult maintenance, and poor measurement accuracy. In addition, since the protective tube of the measuring device is inserted into the raw material powder, there are also other drawbacks such as the possibility of errors due to the material adhering to the protective tube or stagnation, and improvements to these drawbacks are required. Ta.

本発明は上記事情に鑑み工夫されたものであって、ホッ
パから切出され、ベルトコンベアで連続的に移送される
焼結原料石灰等の水分を含む粉体の該水分値をマイクロ
波の透過率に基いて連続的に測定し、該測定結果に基い
て前記粉体の切出し量の制御を行うことを特徴とする粉
体の切出し量制御方法である。
The present invention has been devised in view of the above circumstances, and the moisture value of powder containing moisture such as sintering raw lime, which is cut out from a hopper and continuously transferred by a belt conveyor, is measured by microwave transmission. This is a method for controlling the amount of powder to be cut out, characterized in that the amount of powder to be cut out is controlled based on the measurement result.

以下、本発明の一実施例に用いる装置を示す図面lこ基
いて本発明の詳細な説明する。
Hereinafter, the present invention will be described in detail with reference to the drawings showing an apparatus used in an embodiment of the present invention.

第1図において、1は水分を含む粉体20のホッパ、2
は談ホッパの下方に設置されたベルトコンベア、3はホ
ッパ1の切出しゲート、4は切出しゲ゛−ト3の直後に
おけるベルトコンベア2上方に配置されたマイクロ波の
送信アンテナ、5はベルトコンベア2の下方、送信アン
テナ4の直下に配置されたマイクロ波の受信アンテナで
ある。
In FIG. 1, 1 is a hopper for powder 20 containing moisture;
3 is the cutting gate of the hopper 1; 4 is the microwave transmission antenna placed above the belt conveyor 2 immediately after the cutting gate 3; 5 is the belt conveyor 2 This is a microwave receiving antenna placed directly below the transmitting antenna 4.

FM変調され、マイクロ発振器6から発振されたマイク
ロ波(基準波)はアイソレータ8が設けられた導波管9
を経て送信アンテナ4に送られる。
The FM-modulated microwave (reference wave) oscillated from the micro oscillator 6 passes through a waveguide 9 provided with an isolator 8.
The signal is then sent to the transmitting antenna 4.

そして、該送信アンテナ4から発せられたマイクロ波は
、ホッパ1から切出され、ベルトコンベア2によって連
続的に移送されている粉体20及びベルトコンベア2を
透過するときに一部吸収され、透過したマイクロ波のみ
が受信アンテナ5に受信される。
The microwaves emitted from the transmitting antenna 4 are cut out from the hopper 1 and are partially absorbed when passing through the powder 20 and the belt conveyor 2, which are continuously transported by the belt conveyor 2. Only the received microwaves are received by the receiving antenna 5.

該受信アンテナ5に受信された透過マイクロ波(透過波
)はアイソレータ10が設けられた導波管11によって
後段の測定回路に送られる。
The transmitted microwave (transmitted wave) received by the receiving antenna 5 is sent to a subsequent measuring circuit through a waveguide 11 provided with an isolator 10.

ところで、本実施例では図示の如く、マイクロ波発信器
6から発せられた基準波はカップラ7を通って前述の如
く送信側の導波管9に送られ、他方、受信側の導波管1
1により導かれた透過波はカップラ12を通って前述の
如く後段の測定回路に送られるようになっているが、送
信側のカップラ7と受信側のカップラ12とはディレィ
ライン13によって接続されているため、前記基準波と
透過波とは混合してビート波となる。
By the way, in this embodiment, as shown in the figure, the reference wave emitted from the microwave oscillator 6 passes through the coupler 7 and is sent to the waveguide 9 on the transmitting side as described above, and on the other hand, the reference wave is sent to the waveguide 1 on the receiving side.
The transmitted wave guided by 1 is sent through the coupler 12 to the subsequent measuring circuit as described above, but the coupler 7 on the transmitting side and the coupler 12 on the receiving side are connected by a delay line 13. Therefore, the reference wave and the transmitted wave are mixed to form a beat wave.

このようにして得られるビート波はその振幅Ebが透過
率IT+に比例するものであるため、これをマイクロ波
ディテクタ14で検波した後、ACアンプ15、検波平
滑回路16を通過させることによってその振幅Ebに比
例する信号に処理される。
The amplitude Eb of the beat wave obtained in this way is proportional to the transmittance IT+, so after detecting it with the microwave detector 14, the beat wave is passed through the AC amplifier 15 and the detection smoothing circuit 16, so that its amplitude can be adjusted. It is processed into a signal proportional to Eb.

そして、該信号を10gアンプ17及びDCアンプ18
で処理することによって10gIT+に比例する信号が
出力される。
Then, the signal is transferred to the 10g amplifier 17 and the DC amplifier 18.
By processing this, a signal proportional to 10gIT+ is output.

切出しゲート3の直後における粉体20の層厚dはほぼ
一定に保たれており、かつ、ベルトコンベア2によるマ
イクロ波の吸収率は一定であるから、上述のようにして
連続的に測定されるマイクロ波の透過率測定結果とこの
測定点を通過する粉体20の水分値との間には一定の比
例関係が成立する。
The layer thickness d of the powder 20 immediately after the cutting gate 3 is kept almost constant, and the microwave absorption rate by the belt conveyor 2 is constant, so it is continuously measured as described above. A certain proportional relationship is established between the microwave transmittance measurement result and the moisture value of the powder 20 passing through this measurement point.

したがって、上述のようにして求められた1 0 g
IT+に比例する出力信号により、粉体20の水分値が
求まる。
Therefore, 1 0 g obtained as above
The moisture value of the powder 20 is determined by the output signal proportional to IT+.

第2図はこの水分値と透過率との関係を示すものであり
、この図から両者間には直線的比例関係が成立している
ことがよく分かる。
FIG. 2 shows the relationship between the moisture value and the transmittance, and it is clear from this figure that a linear proportional relationship exists between the two.

本発明では、このようにして連続的に求められた粉体2
0の水分値の測定結果に基いて粉体20の切出し量を制
御するものであるが、その制御は例えば次のようにして
なされる。
In the present invention, the powder 2 obtained continuously in this way
The cutting amount of the powder 20 is controlled based on the measurement result of the moisture value of 0, and the control is performed, for example, as follows.

すなわち、粉体20の測定結果として前述の如<DCア
ンプ18より出力された信号は水分補正回路21に送ら
れ、他方、ベルトコンベア2の前端から搬送コンベア2
2に移載された粉体20の重量は該搬送コンベア22に
検出部24を設置した秤量機23によって連続的に秤量
さね、その測定結果である秤量信号も秤量機23から水
分補正回路21に送られる。
That is, the signal outputted from the DC amplifier 18 as the measurement result of the powder 20 as described above is sent to the moisture correction circuit 21, and on the other hand, the signal output from the front end of the belt conveyor 2 to the conveyor 2 is sent to the moisture correction circuit 21.
The weight of the powder 20 transferred to No. 2 is continuously measured by a weighing machine 23 equipped with a detection unit 24 on the conveyor 22, and a weighing signal as a result of the measurement is also sent from the weighing machine 23 to the moisture correction circuit 21. sent to.

0水分補正回路21は前記両信号に基いて粉体20の重
量に水分値による補正を加えてその実質粉体重量を求め
、その結果信号を比較器25に出力する。
The 0-moisture correction circuit 21 corrects the weight of the powder 20 based on the moisture value based on both of the signals to determine the actual powder weight, and outputs the resulting signal to the comparator 25.

比較器25は設定器26より送られた実質粉体重量の設
定値と、前記の如くして求められた実5質粉体重量の実
測値とを比較し、次に、ベルトコンベア2の駆動モータ
19に接続されたベルトスピード制御回路27は、前記
比較器25の出力に基いて、実質粉体重量の実測値と設
定値との間の偏差をなくすようにベルトスピードの制御
を行う。
The comparator 25 compares the set value of the actual powder weight sent from the setting device 26 with the actual measured value of the actual powder weight obtained as described above, and then A belt speed control circuit 27 connected to the motor 19 controls the belt speed based on the output of the comparator 25 so as to eliminate the deviation between the actual measured value and the set value of the actual powder weight.

0 なお、本発明においては、上記実施例に示したよう
にディレィライン13を用いると、使用帯域内で変調周
期あたり数周期のビート周期が得られる。
0 In the present invention, when the delay line 13 is used as shown in the above embodiment, several beat periods can be obtained per modulation period within the used band.

もつとも、本発明においては、上記実施例の場5合の如
く、基準波と透過波とを混合することを必須とするもの
ではない。
However, in the present invention, it is not essential to mix the reference wave and the transmitted wave as in case 5 of the above embodiment.

しかし、基準波と透過波とを混合しない場合には、マイ
クロ波検波器14が二乗特性を備えているため、透過率
の二乗IT2に比例する出力としてしか得られないので
、前記9実施例に比しdB換算で2倍のダイナミックレ
ンジが必要となる。
However, in the case where the reference wave and the transmitted wave are not mixed, the microwave detector 14 has a square-law characteristic and can only obtain an output proportional to the square IT2 of the transmittance. In terms of dB, twice the dynamic range is required.

本発明方法により水分値を測るためには広いダイナミッ
クレンジが要求されるから、透過率の一部に比例する出
力が得られる前記実施例の混合方式はこの点有利である
Since a wide dynamic range is required to measure moisture values by the method of the present invention, the mixing method of the embodiment described above is advantageous in this respect because it provides an output proportional to a portion of the transmittance.

5 本発明は上記の如く構成されるものであって、前記
実施例に示した方式による実験の結果によれば水分値と
透過率との間には水分0.2%程度の直線性と再現性が
得られ、しかも水分値の測定誤差は標準偏差で示せば約
0.25%程度であり、含水フ粉体の層厚が数十ミリメ
ートルから百数十ミリメートルの範囲では十分に満足で
きる結果が得られた。
5 The present invention is constructed as described above, and according to the results of experiments using the method shown in the above embodiment, there is a linearity and reproducibility between the moisture value and the transmittance of approximately 0.2% moisture. In addition, the measurement error of the moisture value is approximately 0.25% in standard deviation, which is a sufficiently satisfactory result when the layer thickness of the hydrated powder is in the range of several tens of millimeters to over 100 millimeters. was gotten.

また、本発明はマイクロ波を用いて水分値を測定する方
式であるから、安全管理上の問題が皆無であること、放
射線を浴びる危険がないこと、測定器が含水粉体に接続
しないため該粉体の付着、滞溜を生じないこと、したが
って誤差を生じにくいこと、さらに水分値の測定点が従
来の如きホッパ内ではなく、計量機により近いベルトコ
ンベア上に位置しているため制御性に秀れていること等
等、本発明は従来の中性子水分計による方法に比し格段
にすぐれた効果を備えている。
In addition, since the present invention uses microwaves to measure moisture levels, there are no safety management problems, there is no risk of exposure to radiation, and the measuring device is not connected to water-containing powder, so there is no risk of exposure to radiation. There is no adhesion or stagnation of powder, so errors are less likely to occur, and the moisture value measurement point is located on the belt conveyor, closer to the weighing machine, rather than inside the hopper as in the past, which improves controllability. The present invention has much better effects than the conventional method using a neutron moisture meter.

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

第1図は本発明の一実施例を示す側断面図、第2図は本
発明による場合の水分とマイクロ波透過率との関係を示
す図表である。 1・・・ホツノ人2・・・ベルトコンベア、計・・切出
しゲート、4・・・マイクロ波の送信アンテナ、5・・
・マイクロ波の受信アンテナ。
FIG. 1 is a side sectional view showing an embodiment of the present invention, and FIG. 2 is a chart showing the relationship between moisture and microwave transmittance in the case of the present invention. 1...Hotsunojin 2...Belt conveyor, total...cutting gate, 4...Microwave transmitting antenna, 5...
・Microwave receiving antenna.

Claims (1)

【特許請求の範囲】[Claims] 1 ホッパから含水粉体を切出し、該含水粉体をベルト
コンベア上へ一定層厚に積載して連続的に移送する場合
において、前記移送中のベルトコンベア及びその上に積
載された含水粉体の層を透過するマイクロ波の透過率に
基いて該含水粉体の水分値を測定し、該測定結果の水分
値を用いることにより前記含水粉体の見掛けの切出し量
を補正して実質切出し量を求め、該実質切出し量の設定
値に対する偏差に基いて前記ベルトコンベアの移動スピ
ードを制御することにより前記含水粉体の切出し量の制
御を行うことを特徴とする粉体の切出し量制御方法。
1. When cutting out water-containing powder from a hopper, stacking the water-containing powder on a belt conveyor in a constant layer thickness, and continuously transporting it, the belt conveyor during transfer and the water-containing powder loaded thereon are The moisture value of the water-containing powder is measured based on the transmittance of microwaves transmitted through the layer, and the apparent cut-out amount of the water-containing powder is corrected by using the moisture value of the measurement result to determine the actual cut-out amount. A method for controlling the amount of cut-out powder, characterized in that the amount of water-containing powder to be cut out is controlled by controlling the moving speed of the belt conveyor based on the deviation from the set value of the actual cut-out amount.
JP52037223A 1977-03-31 1977-03-31 How to control the amount of powder cut out Expired JPS5820858B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52037223A JPS5820858B2 (en) 1977-03-31 1977-03-31 How to control the amount of powder cut out

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52037223A JPS5820858B2 (en) 1977-03-31 1977-03-31 How to control the amount of powder cut out

Publications (2)

Publication Number Publication Date
JPS53122491A JPS53122491A (en) 1978-10-25
JPS5820858B2 true JPS5820858B2 (en) 1983-04-26

Family

ID=12491584

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52037223A Expired JPS5820858B2 (en) 1977-03-31 1977-03-31 How to control the amount of powder cut out

Country Status (1)

Country Link
JP (1) JPS5820858B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58104839A (en) * 1981-12-16 1983-06-22 Sumitomo Cement Co Ltd Quantitative feeding mechanism of powder continuous quantitative feeding device
JPS5987346A (en) * 1982-11-11 1984-05-19 Inoue Japax Res Inc Detecting apparatus of moisture
JPS6426641U (en) * 1987-08-10 1989-02-15

Also Published As

Publication number Publication date
JPS53122491A (en) 1978-10-25

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