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JP2861664B2 - Flow measurement method for high concentration powder conveyed in pipe - Google Patents
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JP2861664B2 - Flow measurement method for high concentration powder conveyed in pipe - Google Patents

Flow measurement method for high concentration powder conveyed in pipe

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Publication number
JP2861664B2
JP2861664B2 JP23379492A JP23379492A JP2861664B2 JP 2861664 B2 JP2861664 B2 JP 2861664B2 JP 23379492 A JP23379492 A JP 23379492A JP 23379492 A JP23379492 A JP 23379492A JP 2861664 B2 JP2861664 B2 JP 2861664B2
Authority
JP
Japan
Prior art keywords
powder
light
tube
pipe
light transmission
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 - Fee Related
Application number
JP23379492A
Other languages
Japanese (ja)
Other versions
JPH0682287A (en
Inventor
進市 磯崎
聰 松井
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 Engineering Corp
Original Assignee
Nippon Kokan Ltd
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Filing date
Publication date
Application filed by Nippon Kokan Ltd filed Critical Nippon Kokan Ltd
Priority to JP23379492A priority Critical patent/JP2861664B2/en
Publication of JPH0682287A publication Critical patent/JPH0682287A/en
Application granted granted Critical
Publication of JP2861664B2 publication Critical patent/JP2861664B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は管内を搬送媒体により搬
送される高濃度粉体の流量測定方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for measuring a flow rate of a high-concentration powder conveyed by a conveying medium in a pipe.

【0002】[0002]

【従来の技術】従来粉体の流量測定方法として、光透過
方式の粉体濃度計を利用したものが知られている。図7
その一例を示す。図7に示すように、粉体移送管1に
相対する二つの観察窓2を設置し、一方の観察窓2から
光源体3から発する平行光束4を入射し、粉体移送管1
内に入射する。入射した光は粉体7によって減衰し、残
りの透過光を他方の観察窓2から取出し、光検出
に導入して、透過光量を検出する。ここで、入射光強度
Io が粉体7の粒子群を通過し、透過光強度Iに減衰す
る場合、透過率I/Io は数1のランベルトベア則によ
って表される。尚、6はシール用のOリングである。
2. Description of the Related Art Conventionally, as a method for measuring the flow rate of powder, a method using a light transmission type powder densitometer is known. FIG.
To show an example. As shown in FIG. 7, the powder transfer pipe two opposite viewing window 2 to 1 it was placed, and the incident parallel light beam 4 emitted from one of the observation window 2 from light source 3, the powder transfer pipe 1
Incident inside. The incident light attenuated by the powder 7, taken out the rest of the transmitted light from the other observation window 2, the light amount detection end 5
To detect the amount of transmitted light. Here, when the incident light intensity Io passes through the particle group of the powder 7 and attenuates to the transmitted light intensity I, the transmittance I / Io is expressed by the Lambert-Beer rule of Formula 1 . Reference numeral 6 denotes an O-ring for sealing.

【0003】[0003]

【数1】 (Equation 1)

【0004】透過率(I/Io )を測定することによ
り、粉体の粒子濃度(φm )が求まり、更に粉体粒子の
移動速度が搬送媒体(ガス)流速に等しいと仮定し
て、粉体濃度値と搬送媒体平均流速値の積から粉体流
量値を算出する。
By measuring the transmittance (I / Io), the particle concentration (φ m ) of the powder is determined, and further assuming that the moving speed of the powder particles is equal to the flow speed of the carrier medium (gas), It calculates the powder flow rate value from the product of the powder density value and the transport medium average flow velocity value.

【0005】[0005]

【発明が解決しようとする課題】然しながら、上述した
光透過方式による粉体濃度計による測定においては、測
定可能粉体最大濃度が制約されるため、高濃度粉体測定
に適用する場合には、粉体移送管から搬送媒体(ガス)
を等速吸引したり、あるいは分岐管を設けたりして、一
部分の粒子をサンプリングして測定する必要がある。こ
の様な改良した方式によっても、実用化されているダス
ト濃度計の最大粉体濃度は200/m3程度であり、
それ以上の濃度粒子群に対しては光が減衰してしまう
、光透過式粉体濃度計を適用して高濃度粉体流量を測
定することは困難であった。
However, in the measurement using the powder densitometer based on the light transmission method described above, the maximum measurable powder concentration is restricted. Transfer medium (gas) from powder transfer tube
Or it sucked constant speed, or by or provided a branch pipe, it is necessary to measure by sampling a portion of the particles. Even with such an improved system, the maximum powder concentration of a practically used dust concentration meter is about 200 g / m 3 ,
Light is decays for more concentration particles
Because, by applying the light transmission type powder concentration meter measuring the high density powder flow rate is difficult.

【0006】本発明は上記のような問題点を解決するた
めに成されたものであり、高濃度領域の粉体濃度測定を
可能にし、粉体流量をオンラインで測定出来る方法を
供することを目的とする。
[0006] The present invention has been made to solve the above problems, a high powder density measurement of the density region to allow, Hisage how that can measure the powder flow rate in line <br />.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
本発明による管内を搬送される高濃度粉体の流量測
方法は、一定の先端間隔で対向する二つの光透過用測定
管を、粉体が搬送媒体により搬送される管内に突出して
設置し、先端間隔を一定に保ちながら二つの光透過用測
定管を前記管内で移動させると共に、この光透過用測定
管を介して前記管内に光を透過させて管内の各位置にお
ける光の透過率を測定し、測定した透過率から粉体平均
度を算出し、この粉体平均濃度と前記搬送媒体の流速
値とから粉体流量を算出することを特徴とするものであ
[Means for Solving the Problems In order to achieve the above Symbol purpose
Flow rate measurement of a high density powder conveyed through the tube according to the invention
The method consists of two light transmission measurements facing each other at a fixed tip distance.
Project the pipe into the pipe where the powder is transported by the transport medium
Installed, and maintain two tips for light transmission while keeping the tip spacing constant.
The constant tube is moved within the tube, and the light transmission measurement is performed.
Light is transmitted through the tube into the tube, and the light is transmitted to each position in the tube.
Takes the transmittance of light is measured, that calculates the powder average <br/> concentration from the measured transmittance, and calculates the powder flow amount from the powder average density and the flow rate value of the transport medium Features
You .

【0008】この場合、測定部での粉体移送管は、垂直
な管とし、隣接する配管と同芯同軸の連続した断面で、
且つ、その直径の6倍以上の長さを有するものとし、そ
して、この粉体移送管の粉体入側端から長さ方向の70
〜80%の位置に開口部を設けて光透過用測定管を設置
することが、測定部での粉体の流れの均一性を保つ上で
好ましい。
[0008] In this case, the powder transfer pipe in the measuring section is vertical.
With a continuous section concentric with the adjacent pipe,
And shall have a length of at least six times its diameter.
Then, 70 mm in the length direction from the powder entry side end of the powder transfer tube.
An opening is provided at a position of ~ 80% and a measuring tube for light transmission is installed.
To maintain uniformity of powder flow in the measuring section.
preferable.

【0009】[0009]

【作用】[Action] 本発明では、粉体移送管内で一定の先端間隔でIn the present invention, at a constant tip interval in the powder transfer tube,
対向するように突出して配設された光透過用測定管を介Through a light transmission measurement tube protruding so as to face
して、粉体に光を透過させるので、測定部光路長(光透Then, light is transmitted through the powder.
過用測定管の先端間隔に等しい)が粉体移送管径より小Is equal to the diameter of the powder transfer tube)
さくなり、光透過量の減衰量を抑制することが出来、高And the attenuation of light transmission can be suppressed,
濃度の粉体の測定が可能となる。叉、本発明では、光強It becomes possible to measure the concentration of the powder. Also, in the present invention,
度の大きい平行光束を容易に実現可能とするために、レIn order to make it possible to easily realize a large parallel light beam,
ーザ光のような連続光源体を光源体として用いるものとUsing a continuous light source such as laser light as the light source
する。I do.

【0010】即ち、本発明者等は、粉体が高濃度の場
合、透過光強度が上述した数1に従って小さくなるた
め、測定精度が悪くなるが、これを防止するために光の
透過長さ(光路長)を小さくすることに着目して検討を
行い、図3に示すような粉体平均濃度と透過率(I/I
o )との関係を得て、上記発明に到達したものである。
That is, the present inventors have found that powders having a high concentration
In this case, the intensity of the transmitted light is reduced in accordance with the above equation (1).
Measurement accuracy deteriorates, but to prevent this, light
Consideration focused on reducing transmission length (optical path length)
Then, the powder average concentration and transmittance (I / I
o) and the above invention has been achieved.

【0011】図3は、硅砂5号(調和平均径(dp3
2)が0.34mm、粒子の真比重(ρ)が2.58)
の粉体を空気を搬送媒体とした試験により求めた光透過
率(I/Io )と粉体平均濃度との関係を示す図であ
る。
FIG . 3 shows silica sand No. 5 (harmonic mean diameter (dp3
2) is 0.34 mm, and the true specific gravity (ρ) of the particle is 2.58)
Transmission obtained by a test using powdered air as a carrier medium
FIG. 4 is a diagram showing the relationship between the ratio (I / Io) and the average powder concentration.
You.

【0012】ここでは粉体移送管の内径をDとし、粉体
移送管内に挿入した光透過用測定管の先端間隔、即ち光
の透過長さ(光路長)をLとして、D>Lの範囲で、L
を種々に変化させて粉体平均濃度と透過率(I/Io )
との関係を得たものである。光透過用測定管の先端間隔
Lが小さい程、透過光強度Iが増大している。ここでは
3kg/m 3 程度までの測定が可能であることを示して
いる。比較として、図7に示すような粉体濃度計を用い
た場合、点線で示すように0.2kg/m 3 程度までし
か測定できなかった。
Here, the inside diameter of the powder transfer tube is D,
The distance between the tips of the light transmission measurement tubes inserted into the transfer tube,
Let L be the transmission length (optical path length) of L in the range of D> L.
And the transmittance (I / Io)
It is the one that got the relationship. Tip spacing of light transmission measurement tube
The transmitted light intensity I increases as L decreases. here
Show that measurement up to about 3 kg / m 3 is possible
I have. For comparison, a powder densitometer as shown in FIG. 7 was used.
Was case, up to about 0.2 kg / m 3 as indicated by the dotted line
Could not be measured.

【0013】今回の実験で使用したレーザの光源体で
は、透過率を0.15以上にすることが、粉体密度の測
定精度を向上させるために必要であった。しかし、光量
検出端の精度を向上させることによって、透過率を更に
小さく出来る。
With the laser light source used in this experiment,
It is necessary to set the transmittance to 0.15 or more to measure the powder density.
It was necessary to improve the constant accuracy. But the amount of light
By improving the accuracy of the detection end, the transmittance can be further increased.
Can be smaller.

【0014】実際の粉体流量測定においては、粉体の粒
子径が異なり、粉体の種類が異なる所謂混粒状態にある
ので、本発明では、図3を基にして、図5に示すような
透過率と測定条件との関係式を用いて、光量検出端の出
力信号に基づき、粉体平均濃度を求める。
In actual powder flow measurement, the particle size of the powder
In a so-called mixed particle state with different diameters and different types of powder
Therefore, in the present invention, as shown in FIG.
Using the relational expression between transmittance and measurement conditions, the output of the light
The average powder concentration is determined based on the force signal.

【0015】図5は後述する図1、図2の粉体流量測定
装置を用いた場合の透過率(I/Io )と測定条件との
関係を示す図で、粉体として硅砂2種と鉄鉱石とを用い
た試験により得られたものである。図5から明らかなよ
うに、粉体粒径が異なっても、粉体粒子の真比重(ρ)
を考慮することによって、透過率(I/Io )が一つの
較正直線上に一致して測定することが出来た。このこと
から本発明では粉体粒径、粉体種類が混粒していても測
定が可能であることを得た。
FIG . 5 shows the powder flow rate measurement of FIGS. 1 and 2 described later.
Between the transmittance (I / Io) when using the apparatus and the measurement conditions
This diagram shows the relationship, using two types of silica sand and iron ore as powder.
It was obtained by a test. It is clear from FIG.
Thus, even if the powder particle size is different, the true specific gravity of the powder particles (ρ)
Is considered, the transmittance (I / Io) becomes one
The measurement could be made in agreement with the calibration straight line. this thing
Therefore, in the present invention, even if powder particle size and powder type are mixed,
I found that it was possible.

【0016】即ち、測定装置としての光透過用測定管の
先端間隔Lを特定し、被測定物の粉体の真比重(ρ)及
び調和平均径(dp32)が取扱いプロセスの固有値と
して自明であることから、透過率(I/Io )を測定す
ることにより、図5の関係式から粉体平均濃度値(kg
/m 3 )を一義的に求めることが出来る。
That is, a light transmission measuring tube as a measuring device is used.
The tip distance L is specified, and the true specific gravity (ρ) and
And harmonic mean diameter (dp32)
Measurement, the transmittance (I / Io) is measured.
From the relational expression of FIG. 5, the powder average concentration value (kg
/ M 3 ) can be determined uniquely.

【0017】一方、搬送媒体の流速を測定する流速検出
端の出力信号に基づき搬送媒体の平均流速値を算出す
る。即ち、既存のピトー管による圧力の検出信号、又は
熱線式流速検出端による温度の検出信号と搬送媒体の平
均流速との一般的関係式を用いることにより、搬送媒体
の平均流速値の算出が出来る。更に、上記粉体平均濃度
と搬送媒体の平均流速値とを乗算することによって、粉
体流量を算出することが出来る。
On the other hand, flow velocity detection for measuring the flow velocity of the transport medium
Calculates the average flow velocity value of the transport medium based on the output signal at the end.
You. That is, the detection signal of the pressure by the existing pitot tube, or
The temperature detection signal from the hot-wire type
By using a general relational expression with the uniform flow velocity,
Can be calculated. Furthermore, the above powder average concentration
Is multiplied by the average flow velocity value of the transport medium.
The body flow can be calculated.

【0018】更に、本発明においては、相対する二つの
光透過用測定管の先端間隔Lを一定に保った状態で、二
つの光透過用測定管を粉体移送管内で径方向を横断する
ように移動させ、粉体移送管の径方向の粉体平均濃度の
分布を測定する。
Further, in the present invention, two opposing two
With the distance L between the tips of the measuring tubes for light transmission kept constant,
Traverse two light transmission measuring tubes in the powder transfer tube
So that the average powder concentration in the radial direction of the powder
Measure the distribution.

【0019】図4は粉体移送管内の直径方向の粉体分布
を推定するための説明図である。光透過用測定管の先端
間隔Lを一定間隔に保って管の内直径の範囲で、少なく
とも管中心から一方の管壁に向かって、先端間隔長さを
一単位としてステップ的に管の半径に沿い連続して移動
することにより、管内の移動位置に対応する透過光量の
減衰分布から管内の直径方向の粉体平均濃度の分布を測
定し、同時に次の数2の加重平均式を用いて粉体移送管
内の粉体平均濃度を求める。
FIG . 4 shows the powder distribution in the diameter direction in the powder transfer tube.
FIG. 4 is an explanatory diagram for estimating. Tip of measuring tube for light transmission
Keep the interval L at a constant interval and reduce the
Both, from the pipe center toward one pipe wall,
Moves continuously along the radius of the pipe in steps as a unit
By doing so, the transmitted light amount corresponding to the moving position in the tube
From the attenuation distribution, measure the distribution of the average powder concentration in the diameter direction in the pipe.
At the same time, using the following weighted average formula of Equation 2
Find the average concentration of powder inside.

【0020】[0020]

【数2】 (Equation 2)

【0021】[0021]

【実施例】【Example】 以下に本発明の実施例を図によって説明すHereinafter, an embodiment of the present invention will be described with reference to the drawings.
る。図1、図2は本発明の一実施例を示す図であり、図You. 1 and 2 are views showing an embodiment of the present invention.
1は、光透過率検出部、流量検出端、及び演算装置から1 is from the light transmittance detector, the flow detector, and the arithmetic unit
なる粉体流量測定装置を粉体移送管に設置した状態を示Shows a state in which the powder flow measurement device
す図であり、図2は、図1に示す光透過率検出部の要部FIG. 2 is a main part of the light transmittance detector shown in FIG.
を示す図である。これらの図において、10は光透過率FIG. In these figures, 10 is the light transmittance
検出部、11a、11bは光透過用測定管、12は先端Detector, 11a and 11b are measuring tubes for light transmission, 12 is tip
間隔調節装置、13は流速検出端、7は粉体である。An interval adjusting device, 13 is a flow velocity detecting end, and 7 is a powder.

【0022】本発明で用いた粉体流量測定装置は、粉体
7が搬送媒体により搬送される配管系9内に設けられ、
隣接する上下の配管と同心等断面積の垂直な粉体移送管
1の軸芯Cに直交する線E上に位置して対向させた開口
部8a、8bに挿入され、一定の先端間隔Lで対向する
ように突出して配設された光透過用測定管11a、11
bと、光透過用測定管11a、11bに付設した先端間
隔調節装置12と、一方の光透過用測定管11aの後端
部に配置した平行光束入射用の光源体3と、他方の光透
過用測定管11bの後端部に配置した光量検出端5とか
らなる光透過率検出部10と、搬送媒体の流速を測定す
る流速検出端13と、光量検出端5及び流量検出端13
の出力信号から粉体平均濃度と搬送媒体平均流速値とを
各々算出し、これらを乗算して粉体流量値を演算する演
算装置14とを組合わせてなるものである。
The powder flow measuring device used in the present invention is a powder flow measuring device.
7 is provided in a piping system 9 transported by the transport medium,
Vertical powder transfer pipe with the same cross-sectional area as the adjacent upper and lower pipes
Opposed openings located on a line E orthogonal to the axis C of one
Inserted into the portions 8a and 8b and opposed at a constant tip interval L
Measuring tubes 11a, 11 arranged so as to protrude
b and the tip attached to the light transmission measurement tubes 11a and 11b.
Separation adjusting device 12 and rear end of one light transmission measuring tube 11a
Light source body 3 for parallel light beam incidence arranged in
Light amount detection end 5 disposed at the rear end of overuse measurement tube 11b
And the flow rate of the transport medium are measured.
Flow rate detecting end 13, light quantity detecting end 5 and flow rate detecting end 13
From the output signal of
Calculate and multiply these to calculate the powder flow rate.
And the arithmetic unit 14.

【0023】演算装置14は、光量検出端5及び流速検
出端13から各々測定値を信号に変換した送信信号を受
信し、演算部15で演算し、表示部16に粉体7の流量
を表示させる。17は記憶部である。粉体7の流量は、
指令部18から図示しない搬送媒体の流速調整機構、粉
体供給機構等へ指示することによって、調節することが
出来る。上記では粉体移送管1をその直径の6倍の長さ
のものとし、粉体入側端から75%の位置に開口部8
a、8bを設けて、光透過用測定管11a、11bを設
置した。
The arithmetic unit 14 includes a light amount detecting end 5 and a flow rate detecting end.
Receives a transmission signal obtained by converting the measured value into a signal from the output terminal 13.
The calculation unit 15 calculates the flow rate of the powder 7 on the display unit 16.
Is displayed. 17 is a storage unit. The flow rate of the powder 7 is
The flow rate adjusting mechanism for the transport medium (not shown)
It can be adjusted by instructing the body supply mechanism etc.
I can do it. In the above description, the length of the powder transfer tube 1 is six times its diameter.
And an opening 8 at a position 75% from the powder entry end.
a and 8b, and light transmission measuring tubes 11a and 11b.
Was placed.

【0024】ここでは光源体3と光量検出端5とには、
光束を拡大、縮小するために光収束用レンズ20を設け
ている。光束を正確に検出するために、光透過用測定管
11aと光透過用測定管11bとは同一径のものを用
い、同一軸芯になるように設置することが必要である。
叉、光束を正確に検出するために、観察窓2(透明ガラ
ス)、Oリング6等の気密機構が用いられている。更に
光源体3と、光量検出端5等は外乱を防止するために、
カバー19を設けている。
Here, the light source body 3 and the light amount detection end 5 are
A light converging lens 20 is provided to enlarge and reduce the light flux
ing. Measuring tube for light transmission to detect light flux accurately
11a and the light transmission measurement tube 11b have the same diameter.
It is necessary to install them so that they are coaxial.
In addition, in order to accurately detect the light beam, the observation window 2 (transparent glass)
S), an airtight mechanism such as an O-ring 6 is used. Further
In order to prevent disturbance, the light source body 3 and the light amount detection end 5
A cover 19 is provided.

【0025】次に、上述した粉体流量測定装置を用いて
本発明を行う場合について説明する。粉体7を搬送する
配管系9内に設けた粉体移送管1内に粉体7を搬送媒体
によって通過させる。ここでは粉体移送管1が配管系9
内の配管と同心等断面積なので、測定部での流れの均一
性が保たれているために、その中を通過する粉体7の濃
度は配管系9内の粉体7の濃度と同じである。
Next, using the powder flow rate measuring device described above,
The case where the present invention is performed will be described. Convey powder 7
The powder 7 is transported into a powder transfer pipe 1 provided in a piping system 9.
Let through. Here, the powder transfer pipe 1 is connected to a pipe system 9.
Uniform cross-sectional area with pipes inside, uniform flow in the measuring section
The powder 7 passing therethrough
The degree is the same as the concentration of the powder 7 in the piping system 9.

【0026】光透過用測定管11a、11bは、粉体移
送管1の軸芯Cに直交する線E上に位置して対向させた
開口部8a、8bに挿入して配設しているので、光透過
用測定管11a、11bは同一径であり、その軸芯が一
致する。これによって、光透過用測定管11aの端部に
接続した光束入射用の光源体3から入射された光束は平
行光束4となって粉体移送管1内を直角に横切り、対向
する光透過用測定管11bを通過して光量検出端5で検
出される。
The light transmission measurement tubes 11a and 11b are
It is located on the line E perpendicular to the axis C of the pipe 1
Since it is inserted and arranged in the openings 8a and 8b, light transmission
Measuring tubes 11a and 11b have the same diameter,
Match. Thereby, the end of the light transmission measurement tube 11a
The light beam incident from the connected light beam source 3 is flat.
The light beam 4 traverses the powder transfer tube 1 at a right angle as a
Passing through the light transmission measuring tube 11b,
Will be issued.

【0027】光透過用測定管11aから光透過用測定管
11bへ光を透過し、その透過光量の減衰を元の光の投
光強度と比較して求め、粉体移送管1内の粉体平均濃度
を算出する。この場合、測定部の光路長Lを粉体移送管
1の直径より小さくしているので、前述した図5の粉体
平均濃度と透過率との関係から先端間隔Lを適宜選定し
て、光透過量の減衰量を抑制することが出来る。その結
果、粉体7の高濃度粒子群の平均濃度を正確に測定する
ことが出来る。
From the light transmission measurement tube 11a to the light transmission measurement tube
11b, and attenuates the amount of transmitted light to reflect the original light.
Average concentration of powder in powder transfer tube 1 obtained by comparing with light intensity
Is calculated. In this case, the optical path length L of the measuring unit is
1 is smaller than the diameter of the powder of FIG.
From the relationship between the average density and the transmittance, select the tip interval L as appropriate.
Thus, the attenuation of the light transmission amount can be suppressed. The result
As a result, the average concentration of the high concentration particles of the powder 7 is accurately measured.
I can do it.

【0028】本発明では実際の粉体流量測定において、
粉体7が粒子径が異なり、粒子の種類が異なる所謂混粒
状態にあるので、図3を基にして、前述した図5に示す
透過 率と測定条件との関係式を演算装置14の記憶部1
7にあらかじめ記憶させ、測定された光量検出端5の出
力信号に基づき、演算部15で粉体平均濃度を算出す
る。
In the present invention, in actual powder flow rate measurement,
So-called mixed particles in which the powder 7 has different particle diameters and different types of particles
In the state shown in FIG. 5, based on FIG.
The relational expression between the transmittance and the measurement condition is stored in the storage unit 1 of the arithmetic unit 14.
7 is stored in advance, and the output of the measured light amount detection end 5 is output.
The calculation unit 15 calculates the average powder concentration based on the force signal.
You.

【0029】一方、流速検出端13の出力信号から演算
部15により搬送媒体平均流速値を算出する。ここでは
ピトー管による圧力の検出信号と搬送媒体平均流速の一
般的関係式を用いることにより、上記搬送媒体平均流速
値を算出する。更に、上記粉体平均濃度と搬送媒体平均
流速値とを演算部15により乗算することによって、粉
体流量値を算出する。
On the other hand, calculation is performed from the output signal of the flow velocity detecting end 13.
The transport medium average flow velocity value is calculated by the unit 15. here
Pressure detection signal by pitot tube
By using the general relational expression, the average flow velocity
Calculate the value. Furthermore, the average powder concentration and the average
By multiplying the flow velocity value by the calculation unit 15, the powder
Calculate the body flow value.

【0030】そして、本発明では、粉体移送管1の内部
に位置し、相対する光透過用測定管11a、11bを、
その先端間隔Lを所定間隔に保って、粉体移送管1の内
直径の範囲で、一方の管壁から他方の管壁に連続し所定
の速度で粉体移送管1の直径に沿い移動させることによ
り、粉体移送管1内の移動位置に対応する透過光量の減
衰分布から粉体移送管1内の直径方向の粉体濃度分布と
平均濃度値とを算出する。これらの値は表示部16によ
って表示される。
In the present invention, the inside of the powder transfer tube 1 is
And the opposing measurement tubes for light transmission 11a, 11b are
Keeping the tip interval L at a predetermined interval, the inside of the powder transfer pipe 1
Continuous from one tube wall to the other within the diameter range
At a speed along the diameter of the powder transfer tube 1.
And the amount of transmitted light corresponding to the moving position in the powder transfer tube 1 is reduced.
From the decay distribution, the powder concentration distribution in the diameter direction in the powder transfer tube 1 and
An average density value is calculated. These values are displayed on the display unit 16.
Is displayed.

【0031】本発明では粉体移送管1の直径と光透過用
測定管11a、11bの直径との最適関係範囲として
は、次の数3によって決めることが出来る。これは次の
理由によるものである。 光透過用測定管11a、11bの直径が太いと粉体移
送管1内の流の外乱になり、測定に疑義がでる。 光透過用測定管11a、11bの直径と粉体粒径の関
係は、光透過用測定管11a、11bの直径が太いと検
出値が安定する。
In the present invention, the diameter of the powder transfer tube 1 and the light transmission
As the optimum relationship range with the diameter of the measuring tubes 11a and 11b
Can be determined by the following equation (3). This is
It is for a reason. If the diameter of the light transmission measurement tubes 11a and 11b is large,
Disturbance of the flow in the pipe 1 causes doubts in the measurement. The relationship between the diameter of the light transmission measurement tubes 11a and 11b and the powder particle size.
The staff detects that the diameter of the light transmission measurement tubes 11a and 11b is large.
Outgoing price stabilizes.

【0032】[0032]

【数3】 (Equation 3)

【0033】本発明では光透過用測定管11a、11b
の先端間隔Lの最適範囲は、次の理由によって決めるこ
とが出来る。下限値については先端間隔Lが狭すぎる
と、測定区間の流速分布が阻害されるので、その影響を
受けない最小の間隔とする。一般には、光透過用測定管
11a、11bの直径dtの3倍程度である。上限値に
ついては先端間隔Lが広いと光透過量減衰が大きくなる
ので、光透過量減衰の許容出来る間隔とする。
In the present invention, the light transmission measuring tubes 11a and 11b are used.
The optimum range of the tip interval L of the
Can be. Tip spacing L is too narrow for lower limit
And the flow velocity distribution in the measurement section is disturbed.
The minimum interval that can not be received. Generally, light transmission measurement tube
It is about three times the diameter dt of 11a and 11b. To the upper limit
When the distance L between the tips is large, the attenuation of light transmission increases.
Therefore, the interval is set so that the light transmission amount attenuation can be tolerated.

【0034】本発明によれば、条件として管長2.0
m、管径0.2mの粉体移送管1を配管系9に配置し、
粉体移送管1の入側から75%の位置に設けた開口部8
a、8bに光透過用測定管11a、11bを挿入して突
出させ、その先端間隔Lを0.1mになるように配設し
て、粉体7として硅砂5号(dp32=0.34mm,
ρ=2.58)を空気を搬送媒体として流速20m/秒
で搬送した場合、図6に示すような結果を得ることが出
来た。図6は粉体流量(トン/時間)と測定経過時間と
の関係を示す図である。
According to the present invention, the condition that the pipe length is 2.0
m, a powder transfer pipe 1 having a pipe diameter of 0.2 m is arranged in a piping system 9,
Opening 8 provided at a position 75% from the entrance side of powder transfer tube 1
Insert the light transmission measurement tubes 11a and 11b into the
And set it so that the tip distance L is 0.1 m.
And, as the powder 7, silica sand No. 5 (dp32 = 0.34mm,
ρ = 2.58) using air as a carrier medium and a flow velocity of 20 m / sec.
In the case of transport by
Came. Fig. 6 shows the powder flow rate (ton / hour) and the elapsed measurement time.
FIG.

【0035】ここでは粉体濃度のサンプリング間隔を
0.6秒とし、粉体平均濃度と空気の流速値との乗算か
ら、粉体流量値を算出しプロットしたものである。上記
結果から明らかなように、高濃度領域の粉体濃度測定に
よって、粉体流量をオンラインで測定することが出来
る。
Here, the sampling interval of the powder concentration is
0.6 second, multiplying the average powder concentration by the air velocity value
Are calculated and plotted. the above
As is clear from the results, the powder concentration measurement in the high concentration region
Therefore, the powder flow rate can be measured online.
You.

【0036】[0036]

【発明の効果】【The invention's effect】 本発明によれば、以下の効果が得られAccording to the present invention, the following effects can be obtained.
る。You. 粉体濃度3kg/mPowder concentration 3kg / m 3 Three 迄の高濃度の測定が可能であMeasurement of high concentrations up to
る。You. 高濃度粉体の多量搬送量の測定が可能である。It is possible to measure a large amount of transported high-concentration powder. 粉体移送管の径方向の粉体濃度の分布が測定出来る。The distribution of the powder concentration in the radial direction of the powder transfer tube can be measured.

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

【図1】本発明に用いた粉体流量測定装置を設置した状
態を示す図である。
FIG. 1 is a view showing a state where a powder flow rate measuring device used in the present invention is installed.

【図2】本発明に用いた光透過率検出部の要部を示す図
である。
FIG. 2 is a diagram showing a main part of a light transmittance detection unit used in the present invention.

【図3】本発明により先端間隔を変化させた場合の粉体
平均濃度と透過率との関係を示す図である。
3 is a diagram showing the relationship between the powder average density and transmittance in the case of changing the tip gap by the present invention.

【図4】本発明の管内の直径方向の粉体濃度分布を測定
するための説明図である。
FIG. 4 is an explanatory diagram for measuring a powder concentration distribution in a diameter direction in a tube according to the present invention .

【図5】本発明の一実施例から定めた透過率と測定条件
の関係を示す図である。
FIG. 5 shows transmittance and measurement conditions determined from one embodiment of the present invention.
Is a diagram showing the relationship between.

【図6】本発明の一実施例による粉体流量と測定経過時
間との関係を示す図である。
6 is a diagram showing the relationship between the measured elapsed time powder flow amount according to an embodiment of the present invention.

【図7】従来の光透過方式粉体濃度計の一例を示す図で
ある。
FIG. 7 is a diagram showing an example of a conventional light transmission type powder densitometer.

【符号の説明】 粉体移送管 観察窓 光源体 平行光束 光量検出端 Oリング 粉体 8a、8b 開口部 配管系 10 透過率検出部 11a、11b 光透過用測定管 12 先端間隔調節装置 13 流速検出端 14 算装置15 演算部 16 表示部 17 記憶部 18 指令部 [Description of Signs ] 1 powder transfer tube 2 observation window 3 light source 4 parallel light beam 5 light quantity detection end 6 O-ring 7 powder 8a, 8b opening 9 piping system 10 light transmittance detector 11a, 11b light transmission measurement tube 12 distal spacing adjustment device 13 flow rate detecting end 14 arithmetic device 15 calculating unit 16 display unit 17 storage unit 18 instruction unit

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 一定の先端間隔で対向する二つの光透過
用測定管を、粉体が搬送媒体により搬送される管内に突
出して設置し、先端間隔を一定に保ちながら二つの光透
過用測定管を前記管内で移動させると共に、この光透過
用測定管を介して前記管内に光を透過させて管内の各位
置における光の透過率を測定し、測定した透過率から
体平均濃度を算出し、この粉体平均濃度と前記搬送媒体
の流速値とから粉体流量を算出することを特徴とする
内を搬送される高濃度粉体の流量測定方法。
1. Two light transmissions facing each other at a fixed tip interval.
Projecting pipe into the pipe where the powder is transported by the transport medium.
Out and set it up, and keep the tip
The overused measuring tube is moved within said tube and the light transmission
The light is transmitted through the measuring tube through
The light transmittance was measured in the location, the powder average density calculated from the measured transmittance, and calculates the powder flow rate from the powder average density and the flow rate value of the transport medium tube
Method for measuring the flow rate of high-concentration powder conveyed inside .
JP23379492A 1992-09-01 1992-09-01 Flow measurement method for high concentration powder conveyed in pipe Expired - Fee Related JP2861664B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23379492A JP2861664B2 (en) 1992-09-01 1992-09-01 Flow measurement method for high concentration powder conveyed in pipe

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23379492A JP2861664B2 (en) 1992-09-01 1992-09-01 Flow measurement method for high concentration powder conveyed in pipe

Publications (2)

Publication Number Publication Date
JPH0682287A JPH0682287A (en) 1994-03-22
JP2861664B2 true JP2861664B2 (en) 1999-02-24

Family

ID=16960678

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23379492A Expired - Fee Related JP2861664B2 (en) 1992-09-01 1992-09-01 Flow measurement method for high concentration powder conveyed in pipe

Country Status (1)

Country Link
JP (1) JP2861664B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100819863B1 (en) * 2001-09-03 2008-04-07 엘지.필립스 엘시디 주식회사 Flow measuring device

Also Published As

Publication number Publication date
JPH0682287A (en) 1994-03-22

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