JPS5844203B2 - Slag flow rate measurement method - Google Patents
Slag flow rate measurement methodInfo
- Publication number
- JPS5844203B2 JPS5844203B2 JP53108977A JP10897778A JPS5844203B2 JP S5844203 B2 JPS5844203 B2 JP S5844203B2 JP 53108977 A JP53108977 A JP 53108977A JP 10897778 A JP10897778 A JP 10897778A JP S5844203 B2 JPS5844203 B2 JP S5844203B2
- Authority
- JP
- Japan
- Prior art keywords
- slag
- flow rate
- blast furnace
- flow
- cross
- 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
Links
Landscapes
- Measuring Volume Flow (AREA)
- Blast Furnaces (AREA)
Description
【発明の詳細な説明】 この発明は高炉滓等の溶滓流量測定方法に関する。[Detailed description of the invention] The present invention relates to a method for measuring the flow rate of molten slag such as blast furnace slag.
高炉滓等の溶滓の有効利用方法の一つとして溶滓を樋に
よって水砕設備に導いて破砕する方法が有るが、水砕設
備に必要かつ充分な冷却水を供給するためには溶滓流量
を確実に把握しておく必要がある。One method of effectively using molten slag, such as blast furnace slag, is to lead the slag to granulation equipment through a gutter and crush it. It is necessary to accurately grasp the flow rate.
ここに溶滓は高温かつ高粘度であり、樋への付着が生じ
るなど、流量測定が容易でなく、従来は充分実用的な溶
滓流量測定方法がなかった。The slag has a high temperature and high viscosity, and it is difficult to measure the flow rate because it adheres to the gutter, and so far there has been no sufficiently practical method for measuring the flow rate of the slag.
この発明は水砕設備の冷却水制御にも適用し得る溶滓流
量測定方法を提供することを目的とする。An object of the present invention is to provide a method for measuring the flow rate of slag that can also be applied to cooling water control for fracking equipment.
この発明に係る溶滓流量測定方法は、溶滓を流して輸送
する溶滓流路の中途に溶滓流断面が真円になり得る充分
な落差を有する不連続段差部を設け、この不連続段差部
の充分下部において直径用イメージセンサで真円の溶滓
流の断面直径を測定し、この断面直径測定値から換算し
て溶滓流量を求めるものである。The method for measuring the flow rate of slag according to the present invention is to provide a discontinuous step portion having a sufficient head to make the cross section of the slag flow a perfect circle in the middle of a slag flow path through which the slag is transported. A diameter image sensor is used to measure the cross-sectional diameter of a perfectly circular slag flow sufficiently below the stepped portion, and the flow rate of the slag is determined by converting the measured value of the cross-sectional diameter.
次にこの発明に係る溶滓流量測定方法の一実施例を図面
に基づいて説明する。Next, an embodiment of the slag flow rate measuring method according to the present invention will be described based on the drawings.
第1図において、高炉滓1を水砕設備(図示省略)へ輸
送する高炉樋2の中途には充分な落差を有する不連続段
差部3が設けられ、この不連続段差部3の周辺には直径
用イメージセンサ4、温度計5、指標物発射装置6、指
標物検出器1,8が設置されている。In FIG. 1, a discontinuous step portion 3 with a sufficient head is provided in the middle of a blast furnace gutter 2 that transports blast furnace slag 1 to a fracking facility (not shown), and the area around this discontinuous step portion 3 is A diameter image sensor 4, a thermometer 5, an index object emitting device 6, and index object detectors 1 and 8 are installed.
不連続段差部3は、この段差部3を高炉滓1が落下する
際に高炉原流断面が真円になる程度の充分な落差Hoを
有し、一方、直径用イメージセンサ4は、不連続段差部
3の充分下部に臨んでいて断面真円の高炉滓流の断面直
径りを測定する。The discontinuous step portion 3 has a sufficient head Ho such that the cross section of the blast furnace raw flow becomes a perfect circle when the blast furnace slag 1 falls through the step portion 3. On the other hand, the diameter image sensor 4 The cross-sectional diameter of the blast furnace slag that faces sufficiently below the stepped portion 3 and has a perfectly circular cross-section is measured.
指標物発射装置6は、不連続段差部3の比較的上部また
は不連続段差部3よりも上流側において高炉浮流表面に
、陶磁器などの高融点物質よりなる指標物9を空気圧な
どによって打ち込んで付着させるっこのような指標物9
は高炉滓流とともに不連続段差部3を落下するので高炉
滓1の流速測定の指標になり得るとともに、高温の高炉
滓1よりも当然低輝度であるので高炉浮流表面において
も識別が容易である。The indicator launching device 6 drives an indicator 9 made of a high melting point material such as ceramics into the blast furnace floating surface at a relatively upper part of the discontinuous step portion 3 or upstream of the discontinuous step portion 3 by using air pressure or the like to attach it. Indicator object like this 9
Since it falls down the discontinuous step part 3 along with the blast furnace slag flow, it can be used as an indicator for measuring the flow velocity of the blast furnace slag 1, and since it is naturally lower in brightness than the high-temperature blast furnace slag 1, it is easy to identify it even on the surface of the blast furnace floating stream. .
従って指標物9を追跡すれば高炉滓1の流速測定が可能
である。Therefore, by tracking the indicator 9, it is possible to measure the flow velocity of the blast furnace slag 1.
指標物検出器γ、8は、高炉滓流の断面直径測定が行な
われている部分またはその近傍に臨み、かつ高炉滓流に
乗って落下する指標物9を検出し得るようになっている
。The indicator detector γ, 8 faces the part where the cross-sectional diameter of the blast furnace slag is being measured or its vicinity, and is adapted to detect the indicator 9 falling on the blast furnace slag.
また検出器7,8は高炉滓流に沿って鉛直方向に配列さ
れ、落下していく指標物9を順次検出し得る。Further, the detectors 7 and 8 are arranged vertically along the blast furnace slag flow, and can sequentially detect the falling index object 9.
各検出器γ、8の検出信号S1.S2は演算器10に入
力され、指標物9を各検出器7,8が検出した時点の時
間差Tが演算器10において算出される。Detection signal S1 of each detector γ,8. S2 is input to the calculator 10, and the time difference T between the times when the index object 9 is detected by each of the detectors 7 and 8 is calculated by the calculator 10.
さらに各検出器γ、8が指標物9を検出した位置の距離
りを時間差Tで除することによって指標物9の落下速度
■すなわち高炉滓1流速■が算出される。Further, by dividing the distance of the position where each detector γ, 8 detects the index object 9 by the time difference T, the falling velocity (■) of the index object 9, that is, the flow rate (2) of the blast furnace slag 1 is calculated.
演算器10においてはこの流速■と、前記断面直径りか
らπD2/4として算出される断面積Aとを乗じて高炉
滓体積流量QVが求められる。In the calculator 10, the blast furnace slag volumetric flow rate QV is determined by multiplying this flow velocity (1) by the cross-sectional area A calculated as πD2/4 from the cross-sectional diameter.
温度計5は高炉滓1表面温度を検出してその測定値S3
を演算器10に入力し、演算器10ではこの測定値Sか
ら高炉滓1の比重量γを求め、さらに、この比重量γと
体積流量Qvから高炉滓重量流量Qwを求める。The thermometer 5 detects the surface temperature of the blast furnace slag 1 and outputs the measured value S3.
is input to the computing unit 10, and the computing unit 10 determines the specific weight γ of the blast furnace slag 1 from this measured value S, and further determines the blast furnace slag weight flow rate Qw from this specific weight γ and the volumetric flow rate Qv.
このような設備を用い流量測定を行う場合には、断面直
径りと流量QVの関係を基礎データとして求めておき、
高炉滓1輸送に際して、断面直径りを測定して、この測
定値を前記基礎データに基づいて流量QVに換算し、あ
るいは表面温度のデータを加味して流量Qwを求める。When measuring flow rate using such equipment, first obtain the relationship between cross-sectional diameter and flow rate QV as basic data.
When transporting the blast furnace slag 1, the cross-sectional diameter is measured, and this measured value is converted to a flow rate QV based on the basic data, or the flow rate Qw is determined by taking surface temperature data into consideration.
すなわち高炉滓1が高炉樋2から解放された状態で流量
測定を行うので、高炉樋2の影響を受けることなく精密
に流量測定を行うことができ、また直径りのみの測定に
よって流量を求め得るので簡略な測定設備によって確実
に流量測定し得る。That is, since the flow rate is measured while the blast furnace slag 1 is released from the blast furnace gutter 2, the flow rate can be accurately measured without being affected by the blast furnace gutter 2, and the flow rate can be determined by measuring only the diameter. Therefore, the flow rate can be reliably measured using simple measuring equipment.
さらに直径りをイメージセンサによって非接触で測定し
ているので、連続的、かつ精密な測定を容易に行うこと
ができる。Furthermore, since the diameter is measured without contact using an image sensor, continuous and precise measurements can be easily performed.
ここに流RQvおよびQwは断面直径りと次のような関
係にあり、
Qv CX: D2e−2/D
QWOCγD2e2/D
従って断面直径りのみの測定によって流量Qvを測定で
き、かつ、さらに比重量γを測定すれば流量QWをも求
め得ることが分る。Here, the flow rate RQv and Qw have the following relationship with the cross-sectional diameter, Qv CX: D2e-2/D QWOCγD2e2/D Therefore, the flow rate Qv can be measured by measuring only the cross-sectional diameter, and the specific weight γ It can be seen that by measuring , the flow rate QW can also be determined.
なお断面直径りを測定する位置は不連続段差部3上端か
ら充分な落差Hを有する必要があるが、現在のところH
=4[mlとして良好な測定結果を得ている。Note that the position where the cross-sectional diameter is measured needs to have a sufficient head height H from the upper end of the discontinuous step portion 3;
Good measurement results were obtained as = 4ml.
この条件によって測定したV−D曲線、Qv−D曲線の
一例をそれぞれ第2図、第3図に示す。Examples of V-D curves and Qv-D curves measured under these conditions are shown in FIGS. 2 and 3, respectively.
また指標物9は高炉滓1中に埋没することなく、かつ高
炉滓1とともに流動する必要があるが、種種の形状の指
標物9で実験した結果、第4図のような画鋲状の指標物
9が最も好適であることが判明している。In addition, the indicator 9 needs to flow together with the blast furnace slag 1 without being buried in the blast furnace slag 1, but as a result of experiments with indicators 9 of various shapes, we found that the indicator 9 has a thumbtack shape as shown in Fig. 4. 9 has been found to be the most suitable.
前述のとおりこの発明に係る溶滓流量測定方法は、溶滓
を流して輸送する溶滓流路の中途に溶滓流断面が真円に
なり得る充分な落差を有する不連続段差部を設け、この
不連続段差部の充分下部において直径用イメージセンサ
で真円の溶滓流断面直径を測定し、この断面直径測定値
から換算して溶滓流量を求めるので、溶滓流路への溶滓
付着などの影響を受けることなく、容易かつ確実に溶滓
流量を測定し得るという優れた効果を有する。As mentioned above, the method for measuring the flow rate of slag according to the present invention includes providing a discontinuous step portion having a sufficient head to make the cross section of the slag flow a perfect circle in the middle of the slag flow path through which the slag flows and is transported; The slag flow cross-sectional diameter of a perfect circle is measured with a diameter image sensor sufficiently below this discontinuous step part, and the slag flow rate is determined by converting from this cross-sectional diameter measurement value, so that the slag flows into the slag flow path. It has the excellent effect of being able to easily and reliably measure the slag flow rate without being affected by adhesion or the like.
第1図はこの発明に係る溶滓流量測定方法の一実施例に
用いる測定設備を示す概念図、第2図は同実施例による
V−D曲線の一例定例を示すグラフ、第3図は同実施例
によるQv−D曲線の一例定例を示すグラフ、第4図は
同実施に用いる最適な指標物を示す斜視図である。
1・・・・・・高炉滓、2・・・・・・高炉樋、3・・
・・・・不連続段差部、4・・・・・・直径用イメージ
センサ、5・・・・・・温度計、6・・・・・・指標物
発射装置、γ、8・・・・・・指標物検出器、9・・・
・・・指標物、10・・・・・・演算器。FIG. 1 is a conceptual diagram showing measurement equipment used in an embodiment of the slag flow rate measurement method according to the present invention, FIG. 2 is a graph showing an example of a V-D curve according to the embodiment, and FIG. 3 is the same. A graph showing an example of the Qv-D curve according to the example, and FIG. 4 is a perspective view showing an optimal indicator used in the same implementation. 1... Blast furnace slag, 2... Blast furnace gutter, 3...
... Discontinuous step portion, 4 ... Diameter image sensor, 5 ... Thermometer, 6 ... Indicator launcher, γ, 8 ... ...Indicator object detector, 9...
...Indicator object, 10...Arithmetic unit.
Claims (1)
円となったときの直径値と該溶滓流の流速の関係から溶
滓の流量を表わす基礎データを求めておき、流下する溶
滓の断面が真円となるに必要な落差のある段差部をもっ
た溶滓流路を設け、該溶滓流路の段差部に流滓の直径を
検出する直径検出器と流速を検出する流速検出器を臨ま
せ、該直径検出器と流速検出器によって得られた各値と
前記基礎データとによって溶滓の流量を求める溶滓流量
の測定方法。1 Obtain basic data representing the flow rate of the slag from the relationship between the diameter value when the slag flows almost vertically through the space and the cross section of the slag flow becomes a perfect circle and the flow velocity of the slag flow, A slag flow path is provided with a stepped portion having a height necessary to make the cross section of the flowing slag a perfect circle, and a diameter detector for detecting the diameter of the slag and a flow rate are provided at the stepped portion of the slag flow path. A method for measuring the flow rate of slag, in which the flow rate of the slag is determined by using each value obtained by the diameter detector and the flow rate detector and the basic data.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53108977A JPS5844203B2 (en) | 1978-09-05 | 1978-09-05 | Slag flow rate measurement method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53108977A JPS5844203B2 (en) | 1978-09-05 | 1978-09-05 | Slag flow rate measurement method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5535280A JPS5535280A (en) | 1980-03-12 |
| JPS5844203B2 true JPS5844203B2 (en) | 1983-10-01 |
Family
ID=14498440
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53108977A Expired JPS5844203B2 (en) | 1978-09-05 | 1978-09-05 | Slag flow rate measurement method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5844203B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5132024A (en) * | 1988-10-26 | 1992-07-21 | Mintek | Hydro-cyclone underflow monitor based on underflow slurry stream shape |
| DE102017101562B4 (en) | 2017-01-26 | 2022-03-03 | Forbo Siegling Gmbh | Process for manufacturing and/or recycling a conveyor belt and conveyor belt |
-
1978
- 1978-09-05 JP JP53108977A patent/JPS5844203B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5535280A (en) | 1980-03-12 |
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