JP2002257709A - Measuring instrument for measuring concentration and particle size of floating substance - Google Patents

Measuring instrument for measuring concentration and particle size of floating substance

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Publication number
JP2002257709A
JP2002257709A JP2001061389A JP2001061389A JP2002257709A JP 2002257709 A JP2002257709 A JP 2002257709A JP 2001061389 A JP2001061389 A JP 2001061389A JP 2001061389 A JP2001061389 A JP 2001061389A JP 2002257709 A JP2002257709 A JP 2002257709A
Authority
JP
Japan
Prior art keywords
measuring
particle size
concentration
suspended
tank
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
Application number
JP2001061389A
Other languages
Japanese (ja)
Inventor
Saichiro Morita
佐一郎 森田
Tetsuya Sumi
哲也 角
Hideaki Komiya
秀昭 小宮
Takashi Ochi
隆志 越智
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.)
Yokogawa Electric Corp
Original Assignee
Yokogawa Electric 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 Yokogawa Electric Corp filed Critical Yokogawa Electric Corp
Priority to JP2001061389A priority Critical patent/JP2002257709A/en
Publication of JP2002257709A publication Critical patent/JP2002257709A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To measure a concentration of a floating substance, and measure also an amount of the floating substance of a prescribed particle size contained in a measured fuid. SOLUTION: This measuring instrument for measuring a concentraion and a particle size of the floating substance is provided with measuring vessels cascade-connected multi-stagedly to store the measured fluid, flow-meters for measuring flow rates of the respective measured fluids stored in the respective measuring vessels, floating substance concentration measuring instrument main bodies provided in the respective measuring vessels to measure a floating substance-contaminated concentration of the measured fluid, and separators provided respectively between the measuring vessels to separate a prescribed particle size of the floating substances.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、浮遊物質の濃度が
測定出来ると共に、測定流体に含まれる所定粒度の浮遊
物質の量が測定出来る浮遊物質濃度粒度測定装置に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and a method for measuring the concentration of suspended solids and the amount of suspended solids having a predetermined particle size contained in a measurement fluid.

【0002】[0002]

【従来の技術】図4は、従来より一般に使用されている
従来例の構成説明図で、ダムにおいて、浮遊砂が浮遊物
質に相当する場合の浮遊物質混入濃度測定に使用された
例である。図5は図4の測定原理図である。
2. Description of the Related Art FIG. 4 is an explanatory view of the structure of a conventional example generally used in the prior art, and is an example in which a suspended sand corresponds to a suspended solid in a dam, and is used for measuring the concentration of suspended solids mixed therein. FIG. 5 is a diagram illustrating the measurement principle of FIG.

【0003】図4において、1は差圧測定装置本体で、
この場合は、スタンドAに取付けられ、入力される高圧
と低圧との差圧を電気信号に変換して出力する。第1の
導圧管2は、差圧測定装置本体1の高圧側に一端が接続
され、他端が浮遊物質が混入されている測定流体に開放
されている。
In FIG. 4, reference numeral 1 denotes a differential pressure measuring device main body,
In this case, it is attached to the stand A and converts the input differential pressure between the high pressure and the low pressure into an electric signal and outputs it. The first pressure guiding tube 2 has one end connected to the high pressure side of the differential pressure measuring device main body 1 and the other end opened to a measurement fluid mixed with a floating substance.

【0004】第2の導圧管3は、差圧測定装置本体1の
低圧側に一端が接続され、他端が浮遊物質が混入されて
いる測定流体に開放されている。演算器4は、前記差圧
から、この浮遊物質が混入されている測定流体の平均密
度を演算しこの平均密度と予め求められている浮遊物質
が混入されていない測定流体の基準密度とからこの測定
流体の浮遊物質濃度を演算する。この場合は、演算器4
は、変換器に内蔵されている。
[0004] One end of the second pressure guiding tube 3 is connected to the low pressure side of the differential pressure measuring device main body 1, and the other end is open to a measurement fluid containing a suspended substance. The arithmetic unit 4 calculates the average density of the measurement fluid in which the suspended substance is mixed from the differential pressure, and calculates the average density from the average density and the predetermined reference density of the measurement fluid in which the suspended substance is not mixed. Calculate the suspended solids concentration of the measurement fluid. In this case, arithmetic unit 4
Is built into the converter.

【0005】以上の構成において、図5により、装置の
測定原理を説明する。Bは、浮遊物質混入濃度が測定さ
れるダムや河川に相当する水槽で、この場合は、水が満
たされている。
In the above configuration, the measurement principle of the apparatus will be described with reference to FIG. B is a water tank corresponding to a dam or a river in which the concentration of suspended solids is measured, and in this case, is filled with water.

【0006】そして、第1の導圧管2と第2の導圧管3
とは、、水槽Bの所定位置に挿入されている。そして、
第1の導圧管2の先端部は、第2の導圧管3の先端部よ
りも距離Hだけ深く水槽B内に挿入され、第2の導圧管
3及び第1の導圧管2の内部は水封止または水パージさ
れている。
Then, the first pressure guiding tube 2 and the second pressure guiding tube 3
Is inserted at a predetermined position of the water tank B. And
The distal end of the first impulse line 2 is inserted deeper into the water tank B by a distance H than the distal end of the second impulse line 3, and the inside of the second impulse line 3 and the first impulse line 2 are filled with water. Sealed or water purged.

【0007】この場合、差圧測定装置本体1に入力され
る高圧P1及び低圧P2は、それぞれ次式(1),
(2)で示される。 P1=ρH1−ρ0(H1+h1)+ρ0(h1+H1+H−h4)+P0 (1) P2=ρH2−ρ0(H2+h2)+ρ0(h2+H1+H−h3)+P0 (2)
In this case, the high pressure P1 and the low pressure P2 input to the differential pressure measuring device main body 1 are expressed by the following equations (1) and (2), respectively.
This is indicated by (2). P1 = ρH1−ρ0 (H1 + h1) + ρ0 (h1 + H1 + H−h4) + P0 (1) P2 = ρH2−ρ0 (H2 + h2) + ρ0 (h2 + H1 + H−h3) + P0 (2)

【0008】ただし、式(1),(2)において、 ρ:水槽B内の第1の導圧管2の先端部と第2の導圧管
3の先端部との間の水の平均密度 ρ0:第1の導圧管2及び第2の導圧管3に封止された
封止水の密度 H:第1の導圧管2の先端部から第2の導圧管3の先端
部までの距離
In the formulas (1) and (2), ρ: average density of water between the tip of the first impulse line 2 and the end of the second impulse line 3 in the water tank B ρ0: Density of sealing water sealed by the first pressure guiding tube 2 and the second pressure guiding tube 3 H: distance from the tip of the first pressure guiding tube 2 to the tip of the second pressure guiding tube 3

【0009】H1:差圧測定装置本体1のダイアフラム
の中心から水槽Bの最上部までの距離 H2:第2の導圧管3の先端部から水槽Bの最上部まで
の距離 h1:第1の導圧管2の先端部から差圧測定装置本体1
のダイアフラムの中心までの距離
H1: Distance from the center of the diaphragm of the differential pressure measuring device main body 1 to the top of the water tank B H2: Distance from the tip of the second pressure guiding tube 3 to the top of the water tank B h1: First connection Main body 1 of differential pressure measuring device from tip of pressure tube 2
Distance to the center of the diaphragm

【0010】h2:第2の導圧管3の先端部から差圧測
定装置本体1のダイアフラムの中心までの距離 h3:第2の導圧管3の最上部から第2の導圧管3の先
端部までの距離 h4:第1の導圧管2の最上部から第2の導圧管3の先
端部までの距離 P0:大気圧 である。
H2: distance from the end of the second impulse line 3 to the center of the diaphragm of the differential pressure measuring device main body 1 h3: from the top of the second impulse line 3 to the end of the second impulse line 3 H4: distance from the top of the first pressure guiding tube 2 to the tip of the second pressure guiding tube 3 P0: atmospheric pressure.

【0011】そして、H1−H2=Hであり、h3=h
4とした場合、差圧測定装置本体1は上記の式(1)及
び式(2)より、次式(3)で示される差圧(P1−P
2)を、ダイアフラムで検出し、その検出信号を電気信
号に変換する。
Then, H1-H2 = H, and h3 = h
4, the differential pressure measuring device main body 1 uses the differential pressure (P1-P) expressed by the following equation (3) from the above equations (1) and (2).
2) is detected by the diaphragm, and the detection signal is converted into an electric signal.

【0012】P1−P2=H(ρ−ρ0) (3) そして、式(3)においてH及びρ0は既知の値である
ので、演算器4は差圧測定装置本体1の出力(差圧信
号)を入力して、式(3)における水の平均密度ρを算
出する。
P1−P2 = H (ρ−ρ0) (3) Since H and ρ0 in Expression (3) are known values, the arithmetic unit 4 outputs the differential pressure signal (the differential pressure signal ) To calculate the average density ρ of water in equation (3).

【0013】そして、演算器4には、H、ρ0及び浮遊
物質が混入していない状態の水の基準密度が既知の値と
して予め格納されており、演算器4は、算出した水の平
均密度ρと格納された基準密度との差を算出し、浮遊物
質混入濃度の指数として出力する。
The arithmetic unit 4 previously stores H, ρ0, and the reference density of water in which no suspended matter is mixed, as a known value. The difference between ρ and the stored reference density is calculated and output as an index of the concentration of suspended solids.

【0014】[0014]

【発明が解決しようとする課題】しかしながら、このよ
うな装置においては、測定流体に含まれる所定粒度の浮
遊物質の量が測定出来無い。
However, in such an apparatus, the amount of suspended matter having a predetermined particle size contained in the measurement fluid cannot be measured.

【0015】本発明の目的は、上記の課題を解決するも
ので、浮遊物質の濃度が測定出来ると共に、測定流体に
含まれる所定粒度の浮遊物質の量が測定出来る浮遊物質
濃度粒度測定装置を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems, and to provide a suspended substance concentration particle size measuring apparatus capable of measuring the concentration of suspended substance and measuring the amount of suspended substance having a predetermined particle size contained in a measurement fluid. Is to do.

【0016】[0016]

【課題を解決するための手段】このような目的を達成す
るために、本発明では、請求項1の浮遊物質濃度粒度測
定装置においては、多段にカスケ−ド接続されて設けら
れ測定流体が蓄えられる測定槽と、この測定槽に蓄えら
れる測定流体流量を測定する流量計と、前記測定槽に設
けられ前記測定流体の浮遊物質混入濃度を測定する浮遊
物質濃度測定装置本体と、前記測定槽間に設けられ所定
粒度の浮遊物質を分離する分離器とを具備したことを特
徴とする。
In order to achieve the above object, according to the present invention, in the apparatus for measuring the particle concentration of suspended solids according to the present invention, the measuring fluid is provided in cascade connection in multiple stages. Measurement tank, a flow meter for measuring the flow rate of the measurement fluid stored in the measurement tank, a floating substance concentration measuring device main body provided in the measurement tank for measuring the concentration of suspended solids in the measurement fluid, and the measurement tank And a separator for separating suspended substances having a predetermined particle size.

【0017】本発明の請求項2の浮遊物質濃度粒度測定
装置において、測定流体が蓄えられる測定槽と、この測
定槽に蓄えられる測定流体流量を測定する流量計と、前
記測定槽に設けられ前記測定流体の浮遊物質混入濃度を
測定する浮遊物質濃度測定装置本体と、前記測定槽の下
流に設けられ所定粒度の浮遊物質を分離する分離器とを
具備し、前記分離器より流出した前記測定流体を前記測
定槽に所定回数戻すようにしたことを特徴とする。
According to a second aspect of the present invention, there is provided an apparatus for measuring particle concentration of suspended solids, wherein a measuring tank for storing a measuring fluid, a flow meter for measuring a flow rate of the measuring fluid stored in the measuring tank, The apparatus further comprises: a suspended substance concentration measuring device main body for measuring a suspended substance mixed concentration of a measurement fluid; and a separator provided downstream of the measurement tank for separating suspended substances having a predetermined particle size, and the measurement fluid flowing out of the separator. Is returned to the measuring tank a predetermined number of times.

【0018】本発明の請求項3においては、請求項1又
は請求項2記載の浮遊物質濃度粒度測定装置において、
前記流量計と前記浮遊物質濃度測定装置本体との測定信
号から前記分離器で分離された浮遊物質重量を演算する
演算器を具備したことを特徴とする。
According to a third aspect of the present invention, there is provided an apparatus for measuring particle concentration of suspended solids according to the first or second aspect,
An arithmetic unit for calculating the weight of the suspended substance separated by the separator from the measurement signals of the flow meter and the suspended substance concentration measuring device main body is provided.

【0019】本発明の請求項4においては、請求項1乃
至請求項3の何れかに記載の浮遊物質濃度粒度測定装置
において、前記分離器として、装置の上流側から下流側
に分離される前記所定粒度の大きさが順次小さくなるよ
うに設定されたことを特徴とする。
According to a fourth aspect of the present invention, in the apparatus for measuring particle concentration of suspended solids according to any one of the first to third aspects, the separator is separated from an upstream side to a downstream side of the apparatus. It is characterized in that the size of the predetermined granularity is set so as to be gradually reduced.

【0020】本発明の請求項5においては、請求項1乃
至請求項4の何れかに記載の浮遊物質濃度粒度測定装置
において、前記分離器により分離された前記浮遊物質重
量から前記測定流体の浮遊物質の粒度分布を表示する表
示器を具備したことを特徴とする。
According to a fifth aspect of the present invention, in the apparatus for measuring suspended particle concentration and particle size according to any one of the first to fourth aspects, the suspension of the measurement fluid is determined from the weight of the suspended substance separated by the separator. An indicator for displaying the particle size distribution of the substance is provided.

【0021】本発明の請求項6においては、請求項1乃
至請求項5の何れかに記載の浮遊物質濃度粒度測定装置
において、前記分離機として、フィルタが使用されたこ
とを特徴とする。
According to a sixth aspect of the present invention, in the apparatus for measuring the concentration and concentration of suspended solids according to any one of the first to fifth aspects, a filter is used as the separator.

【0022】本発明の請求項7においては、請求項6記
載の浮遊物質濃度粒度測定装置において、前記フィルタ
として、オートクリーンフィルタが使用されたことを特
徴とする。
According to a seventh aspect of the present invention, in the apparatus for measuring the particle concentration of suspended solids according to the sixth aspect, an auto-clean filter is used as the filter.

【0023】本発明の請求項8においては、請求項1乃
至請求項7の何れかに記載の浮遊物質濃度粒度測定装置
において、前記流量計として、電磁流量計が使用された
ことを特徴とする。
According to an eighth aspect of the present invention, in the apparatus for measuring the concentration and concentration of suspended solids according to any one of the first to seventh aspects, an electromagnetic flowmeter is used as the flowmeter. .

【0024】[0024]

【発明の実施の形態】以下図面を用いて本発明を詳しく
説明する。図1は本発明の一実施例の要部構成説明図
で、浮遊砂濃度/粒度分布の測定に使用された例に付い
て示す。図2は図1の動作説明図である。図において、
図4と同一記号の構成は同一機能を表す。以下、図4と
相違部分のみ説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail with reference to the drawings. FIG. 1 is an explanatory view of a main part configuration of an embodiment of the present invention, showing an example used for measuring suspended sand concentration / particle size distribution. FIG. 2 is an explanatory diagram of the operation of FIG. In the figure,
4 have the same functions. Hereinafter, only differences from FIG. 4 will be described.

【0025】図において、ポンプPU1は、測定流体源
Cから測定流体FLを引き込む。第1,第2,第3の測
定槽TA1,TA2,TA3は、多段にカスケード接続
されて設けられ、測定流体源Aから引き込まれた測定流
体FLが蓄えられる。
In the figure, a pump PU1 is connected to a measuring fluid source.
The measuring fluid FL is drawn from C. The first, second, and third measurement tanks TA1, TA2, and TA3 are provided in a cascade connection in multiple stages, and store the measurement fluid FL drawn from the measurement fluid source A.

【0026】流量計F1,F2,F3は、測定槽TA
1,TA2,TA3に引き込まれた測定流体FLの流量
をそれぞれ測定する。この場合は、流量計として、電磁
流量計が使用されている。
The flow meters F1, F2 and F3 are connected to a measuring tank TA.
The flow rates of the measurement fluid FL drawn into 1, TA2, and TA3 are respectively measured. In this case, an electromagnetic flowmeter is used as the flowmeter.

【0027】浮遊物質濃度測定装置本体M1,M2,M
3は、測定槽TA1,TA2,TA3に設けられ、測定
流体FLの浮遊物質混入濃度をそれぞれ測定する。分離
器S1,S2は、測定槽TA1,TA2,TA3間に設
けられ、それぞれ所定粒度の浮遊物質を分離する。
Suspended substance concentration measuring apparatus main body M1, M2, M
Reference numeral 3 is provided in each of the measurement tanks TA1, TA2, and TA3, and measures the concentration of suspended solids in the measurement fluid FL. The separators S1 and S2 are provided between the measuring tanks TA1, TA2 and TA3, and each separate a suspended substance having a predetermined particle size.

【0028】この場合は、分離器S1,S2として、装
置の上流側から下流側に分離される所定粒度の大きさが
順次小さくなるように設定されている。この場合は、例
えば、分離器S1は100μm以上、分離器S2は10
0μm〜10μmの粒度に分離する。
In this case, the separators S1 and S2 are set so that the size of a predetermined particle size separated from the upstream side to the downstream side of the apparatus becomes smaller in order. In this case, for example, the separator S1 is 100 μm or more, and the separator S2 is 10 μm or more.
Separate to a particle size of 0 μm to 10 μm.

【0029】また、この場合は、分離機S1,S2とし
て、フィルタが使用され、且つ、オートクリーンフィル
タが使用されている。演算器C1,C2,C3は、流量
計F1,F2,F3と浮遊物質濃度測定装置本体M1,
M2,M3との測定信号とから、それぞれの分離器S
1,S2で分離された浮遊物質重量を演算する。
In this case, filters are used as the separators S1 and S2, and an auto-clean filter is used. The arithmetic units C1, C2, and C3 are composed of the flow meters F1, F2, and F3 and the suspended matter concentration measuring device main body M1,
From the measurement signals of M2 and M3, the respective separators S
Calculate the weight of suspended solids separated in 1 and S2.

【0030】表示器Dは、それぞれの分離器S1,S2
により分離された浮遊物質重量から、測定流体の浮遊物
質の粒度分布を表示する。分離器S0は、ポンプPU1
と流量計F1との間に設けられ、前もって、粗大浮遊物
質を除去する為の分離器である。
The display D is provided with respective separators S1 and S2.
The particle size distribution of the suspended substance of the measurement fluid is displayed from the suspended substance weight separated by the above. The separator S0 is connected to the pump PU1.
And a flow meter F1 for removing coarse suspended substances in advance.

【0031】ポンプPU2は、分離器S0と流量計F1
との間に設けられ、測定槽TA1に測定流体FLを送
る。ポンプPU3は、分離器S1と流量計F2との間に
設けられ、測定槽TA1に取り付けられた液位コントロ
ーラLC1の指示に基づき、測定槽TA2に測定流体F
Lを送る。
The pump PU2 includes a separator S0 and a flow meter F1.
And sends the measurement fluid FL to the measurement tank TA1. The pump PU3 is provided between the separator S1 and the flow meter F2, and is supplied to the measurement tank TA2 based on an instruction of the liquid level controller LC1 attached to the measurement tank TA1.
Send L.

【0032】ポンプPU4は、分離器S2と流量計F3
との間に設けられ、測定槽TA2に取り付けられた液位
コントローラLC2の指示に基づき、測定槽TA3に測
定流体FLを送る。
The pump PU4 includes a separator S2 and a flow meter F3.
And sends the measurement fluid FL to the measurement tank TA3 based on an instruction from the liquid level controller LC2 attached to the measurement tank TA2.

【0033】ポンプPU5は、浮遊物質濃度測定装置本
体M3に設けられ、測定槽TA3に取り付けられた液位
コントローラLC3の指示に基づき、測定槽TA3の測
定流体FLを排出する。
The pump PU5 is provided in the suspended substance concentration measuring device main body M3, and discharges the measurement fluid FL in the measurement tank TA3 based on an instruction from the liquid level controller LC3 attached to the measurement tank TA3.

【0034】以上の構成において、測定流体源Cから、
ポンプPU1により測定流体FLを引き込み、第1の測
定槽TA1に測定流体FLが蓄えられる。第1の測定槽
TA1中の浮遊物質濃度測定装置本体M1により、測定
流体FLの浮遊物質混入濃度が測定される。
In the above configuration, from the measurement fluid source C,
The measurement fluid FL is drawn in by the pump PU1, and the measurement fluid FL is stored in the first measurement tank TA1. The suspended substance concentration of the measurement fluid FL is measured by the suspended substance concentration measuring device main body M1 in the first measurement tank TA1.

【0035】次に、第1の測定槽TA1の底から,沈降
した浮遊砂を含む測定流体FLを引き出し、分離器S1
を通して、粒径d1以下のものだけが含まれる測定流体
FLを、第2の測定槽TA2へ移す。
Next, the measuring fluid FL containing the suspended suspended sand is drawn out from the bottom of the first measuring tank TA1 and separated from the separator S1.
, The measurement fluid FL containing only those having a particle diameter of d1 or less is transferred to the second measurement tank TA2.

【0036】第2の測定槽TA2中の浮遊物質濃度測定
装置本体M2により、測定流体FLの浮遊物質混入濃度
が測定される。次に、第2の測定槽TA2の底から,沈
降した浮遊砂を含む測定流体FLを引き出し、分離器S
2を通して、粒径d2以下のものだけが含まれる測定流
体FLを、第3の測定槽TA3へ移す。
The suspended substance concentration of the measurement fluid FL is measured by the suspended substance concentration measuring device main body M2 in the second measuring tank TA2. Next, from the bottom of the second measurement tank TA2, the measurement fluid FL containing the suspended suspended sand is drawn out, and the separator S
Through 2, the measuring fluid FL containing only those having a particle size of d2 or less is transferred to the third measuring tank TA3.

【0037】第3の測定槽TA3中の浮遊物質濃度測定
装置本体M3により、測定流体FLの浮遊物質混入濃度
が測定される。以上の如く、測定槽TAと浮遊物質濃度
測定装置本体Mと分離器Sと流量計Fとのユニットを、
必要に応じて増やすことにより、図2に示す如く、表示
器Dにより、浮遊砂の粒度分布が測定出来る。
The suspended substance concentration of the measurement fluid FL is measured by the suspended substance concentration measuring device body M3 in the third measuring tank TA3. As described above, the unit of the measuring tank TA, the suspended matter concentration measuring device main body M, the separator S, and the flow meter F,
By increasing the number as needed, the particle size distribution of suspended sand can be measured by the display D as shown in FIG.

【0038】即ち、測定流体源Aから、分離器S1を通
して、ポンプPU1により測定流体FLを引き込む。流
量計F1により、浮遊砂を含む測定流体FLの流量Q1
が測定される。測定槽TA1内の浮遊物質濃度測定装置
本体M1により、浮遊砂の濃度の測定値α1が分かる
と、 測定槽TA1に流入する浮遊砂の重量W1=Q1・α1 測定槽TA1で測定する浮遊砂の粒径d<d1
That is, the measurement fluid FL is drawn in from the measurement fluid source A through the separator S1 by the pump PU1. The flow rate Q1 of the measurement fluid FL including suspended sand is measured by the flow meter F1.
Is measured. When the measured value α1 of the concentration of the suspended sand is known by the suspended matter concentration measuring device main body M1 in the measurement tank TA1, the weight W1 of the suspended sand flowing into the measurement tank TA1 = Q1 · α1 of the suspended sand measured in the measurement tank TA1. Particle size d <d1

【0039】測定槽TA2に流入する浮遊砂の重量W2
=Q2・α2 測定槽TA2で測定する浮遊砂の粒径d<d2<d1 粒径d1からd2までの浮遊砂の量(Q1・α1−Q2
・α2)
Weight W2 of suspended sand flowing into measuring tank TA2
= Q2 · α2 Particle size d <d2 <d1 of suspended sand measured in the measuring tank TA2 Amount of suspended sand from the particle size d1 to d2 (Q1 · α1-Q2
・ Α2)

【0040】測定槽TA3に流入する浮遊砂の重量W3
=Q3・α3 測定槽TA2で測定する浮遊砂の粒径d<d3<d2 粒径d2からd3までの浮遊砂の量(Q2・α2−Q3
・α3)
Weight W3 of suspended sand flowing into measuring tank TA3
= Q3 · α3 The particle size d <d3 <d2 of the suspended sand measured in the measuring tank TA2.
・ Α3)

【0041】この結果、 (1)浮遊物質の濃度が測定出来ると共に、測定流体に
含まれる所定粒度d1,d2の浮遊物質の量が測定出来
る浮遊物質濃度粒度測定装置が得られる。
As a result, (1) a suspended substance concentration particle size measuring apparatus capable of measuring the concentration of suspended substances and measuring the amount of suspended substances having predetermined particle sizes d1 and d2 contained in the measurement fluid is obtained.

【0042】(2)演算器C1,C2,C3が使用され
たので、所定粒度の浮遊物質の量がリアルタイムに測定
出来る浮遊物質濃度粒度測定装置が得られる。
(2) Since the computing units C1, C2, and C3 are used, a suspended substance concentration particle size measuring apparatus capable of measuring the amount of suspended substance having a predetermined particle size in real time is obtained.

【0043】(3)所定粒度d1,d2,d3の大きさ
毎に粒度の大きさ順に浮遊物質が容易に分離できる浮遊
物質濃度粒度測定装置が得られる。
(3) An apparatus for measuring the concentration of suspended solids can be obtained in which suspended solids can be easily separated in the order of particle size for each of the predetermined particle sizes d1, d2, and d3.

【0044】(4)測定流体の浮遊物質の粒度分布が容
易にリアルタイムに表示できる浮遊物質濃度粒度測定装
置が得られる。
(4) An apparatus for measuring the particle size of a suspended substance which can easily display the particle size distribution of the suspended substance in the measurement fluid in real time can be obtained.

【0045】(5)遠心分離機等でなく、フィルタS
1,S2が使用されたので、フィルタは安価であり、浮
遊物質の分離が安価に出来る浮遊物質濃度粒度測定装置
が得られる。
(5) A filter S, not a centrifuge, etc.
Since S1 and S2 are used, the filter is inexpensive, and a suspended substance concentration particle size measuring apparatus capable of inexpensively separating suspended substances can be obtained.

【0046】(6)オートクリーンフィルタS1,S2
が使用されたので、フィルタが自動的にクリーニングさ
れ、連続的操作が容易な浮遊物質濃度粒度測定装置が得
られる。
(6) Auto clean filters S1, S2
Was used, the filter was automatically cleaned, and a particle size measuring device for suspended substance concentration which was easy to operate continuously was obtained.

【0047】(7)電磁流量計F1,F2,F3が使用
されたので、電磁流量計は測定管内には障害物が無く、
浮遊物質の詰まり、付着、衝突による流量測定誤差の生
ずる恐れが少ない浮遊物質濃度粒度測定装置が得られ
る。
(7) Since the electromagnetic flowmeters F1, F2, and F3 are used, the electromagnetic flowmeter has no obstruction in the measuring tube,
It is possible to obtain a particle size measuring apparatus for measuring the concentration of suspended solids which is less likely to cause a flow rate measurement error due to clogging, adhesion and collision of suspended solids.

【0048】(8)本装置を連続して使用する場合に
は、リアルタイムで、流れている河川等の測定流体中に
どのような粒度分布の浮遊物質が流れているか概略知る
ことが出来る。つまり、流れの中の浮遊物質の濃度と粒
度分布の連続計測が可能となる浮遊物質濃度粒度測定装
置が得られる。
(8) When this apparatus is used continuously, it is possible to know in real time what kind of particle size distribution of suspended solids flows in a measuring fluid such as a flowing river. That is, a suspended substance concentration particle size measuring apparatus capable of continuously measuring the concentration and the particle size distribution of the suspended substance in the flow can be obtained.

【0049】図3は本発明の他の実施例の要部構成説明
図である。本実施例においては、流量計F1、測定槽T
A1、浮遊物質濃度測定装置本体M1とを各1個を繰り
返し使用して、実質的に、流量計F1、測定槽TA1、
浮遊物質濃度測定装置本体M1を複数個利用するように
したものである。
FIG. 3 is an explanatory view of a main part configuration of another embodiment of the present invention. In this embodiment, the flow meter F1 and the measuring tank T
A1, the suspended substance concentration measuring device main body M1 is repeatedly used for each one, and the flow meter F1, the measuring tank TA1,
In this embodiment, a plurality of suspended substance concentration measuring apparatus main bodies M1 are used.

【0050】測定流体FLは、最初実線で示されたR1
の経路を辿り、次に、点線で示されたR2の経路を辿
り、最後に、フィルタS2に切換えられて、一点鎖線で
示されたR1の経路を辿る。
The measurement fluid FL is R1 indicated by a solid line at first.
, Then follow the path of R2 indicated by the dotted line, and finally, switch to the filter S2 and follow the path of R1 indicated by the dashed line.

【0051】流量計、測定槽、浮遊物質濃度測定装置本
体が削減出来、特に、高価な計測器が削減出来、安価
で、且つ、スペースファクタが良好な浮遊物質濃度粒度
測定装置が得られる。
It is possible to reduce the number of flowmeters, measuring tanks and suspended substance concentration measuring devices, and in particular, to reduce expensive measuring instruments, and to obtain a suspended substance concentration and particle size measuring apparatus which is inexpensive and has a good space factor.

【0052】なお、前述の実施例においては、流量計F
1,F2,F3、……、測定槽TA1,TA2,TA
3、……、浮遊物質濃度測定装置本体M1,M2,M3
……、と分離器S1,S2……、とを連続的に配置して
装置を構成する例に付いて説明した。
In the above embodiment, the flow meter F
1, F2, F3, ..., measuring tanks TA1, TA2, TA
3,..., Suspended matter concentration measuring device main body M1, M2, M3
.., And separators S1, S2,.

【0053】しかし、例えば、流量計F1、測定槽TA
1、浮遊物質濃度測定装置本体M1と分離器S1とを各
1個使用して、測定の第1の段階が終了した後、流量計
F2,F3、測定槽TA2,TA3、浮遊物質濃度測定
装置本体M2,M3と分離器S2の代わりに、流量計F
1、測定槽TA1、浮遊物質濃度測定装置本体M1と分
離器S1とを再度使用するようにしても良い。なお、分
離器S1の分離粒度は段階毎に変えることは勿論であ
る。
However, for example, the flow meter F1, the measuring tank TA
1. After the first stage of measurement is completed using one each of the suspended substance concentration measuring device main body M1 and the separator S1, the flow meters F2 and F3, the measuring tanks TA2 and TA3, the suspended substance concentration measuring device Instead of the main bodies M2 and M3 and the separator S2, a flow meter F
1. The measuring tank TA1, the suspended matter concentration measuring device main body M1, and the separator S1 may be used again. In addition, it goes without saying that the separation particle size of the separator S1 is changed every stage.

【0054】このようにすれば、更に、安価で、且つ、
スペースファクタが良好な浮遊物質濃度粒度測定装置が
得られる。
In this way, the cost is lower and
An apparatus for measuring the concentration of suspended solids having a good space factor can be obtained.

【0055】なお、以上の説明は、本発明の説明および
例示を目的として、特定の好適な実施例を示したに過ぎ
ない。したがって本発明は、上記実施例に限定されるこ
となく、その本質から逸脱しない範囲で更に多くの変
更、変形をも含むものである。
It should be noted that the foregoing description has been directed to specific preferred embodiments for the purpose of illustration and illustration of the invention. Therefore, the present invention is not limited to the above-described embodiment, but includes many more changes and modifications without departing from the spirit thereof.

【0056】[0056]

【発明の効果】以上説明したように、本発明の請求項1
によれば、次のような効果がある。浮遊物質の濃度が測
定出来ると共に、測定流体に含まれる所定粒度の浮遊物
質の量が測定出来、且つ、より連続測定し易い浮遊物質
濃度粒度測定装置が得られる。
As described above, according to the first aspect of the present invention,
According to the above, the following effects are obtained. The concentration of suspended solids can be measured, the amount of suspended solids of a predetermined particle size contained in the fluid to be measured can be measured, and an apparatus for measuring the concentration of suspended solids that can be measured more easily can be obtained.

【0057】本発明の請求項2によれば、次のような効
果がある。浮遊物質の濃度が測定出来ると共に、測定流
体に含まれる所定粒度の浮遊物質の量が測定出来、且
つ、安価で、スペースファクタが良好な浮遊物質濃度粒
度測定装置が得られる。
According to the second aspect of the present invention, the following effects can be obtained. The concentration of suspended solids can be measured, the amount of suspended solids of a predetermined particle size contained in the measurement fluid can be measured, and an inexpensive suspended solid concentration particle size measuring device with a good space factor can be obtained.

【0058】本発明の請求項3によれば、次のような効
果がある。演算器が使用されたので、所定粒度の浮遊物
質の量がリアルタイムに測定出来る浮遊物質濃度粒度測
定装置が得られる。
According to the third aspect of the present invention, the following effects can be obtained. Since the arithmetic unit is used, a floating substance concentration particle size measuring device capable of measuring the amount of the floating substance having a predetermined particle size in real time is obtained.

【0059】本発明の請求項4によれば、次のような効
果がある。所定粒度の大きさ毎に粒度の大きさ順に浮遊
物質が容易に分離できる浮遊物質濃度粒度測定装置が得
られる。
According to the fourth aspect of the present invention, the following effects can be obtained. An apparatus for measuring the concentration of suspended solids, which can easily separate the suspended solids in the order of the magnitude of the particle size for each predetermined particle size, is obtained.

【0060】本発明の請求項5によれば、次のような効
果がある。 (1)測定流体の浮遊物質の粒度分布が容易にリアルタ
イムに表示できる浮遊物質濃度粒度測定装置が得られ
る。
According to the fifth aspect of the present invention, the following effects can be obtained. (1) A floating substance concentration particle size measuring apparatus capable of easily displaying the particle size distribution of the floating substance of the measurement fluid in real time can be obtained.

【0061】(2)本装置を連続して使用する場合に
は、リアルタイムで、流れている河川等の測定流体中に
どのような粒度分布の浮遊物質が流れているか概略知る
ことが出来る。つまり、流れの中の浮遊物質の濃度と粒
度分布の連続計測が可能となる浮遊物質濃度粒度測定装
置が得られる。
(2) When the present apparatus is used continuously, it is possible to roughly know in real time what particle size distribution of suspended solids flows in a measuring fluid such as a flowing river. That is, a suspended substance concentration particle size measuring apparatus capable of continuously measuring the concentration and the particle size distribution of the suspended substance in the flow can be obtained.

【0062】本発明の請求項6によれば、次のような効
果がある。遠心分離機等でなく、フィルタが使用された
ので、フィルタは安価であり、浮遊物質の分離が安価に
出来る浮遊物質濃度粒度測定装置が得られる。
According to the sixth aspect of the present invention, the following effects can be obtained. Since a filter is used instead of a centrifugal separator or the like, the filter is inexpensive, and a suspended substance concentration particle size measuring apparatus capable of inexpensively separating suspended substances can be obtained.

【0063】本発明の請求項7によれば、次のような効
果がある。オートクリーンフィルタが使用されたので、
フィルタが自動的にクリーニングされ、連続的操作が容
易な浮遊物質濃度粒度測定装置が得られる。
According to the seventh aspect of the present invention, the following effects can be obtained. Since the auto clean filter was used,
The filter is automatically cleaned and a particle size measuring apparatus for the suspended substance concentration which can be easily operated continuously is obtained.

【0064】本発明の請求項8によれば、次のような効
果がある。電磁流量計が使用されたので、電磁流量計は
測定管内には障害物が無く、浮遊物質の詰まり、付着、
衝突による流量測定誤差の生ずる恐れが少ない浮遊物質
濃度粒度測定装置が得られる。
According to the eighth aspect of the present invention, the following effects can be obtained. Since an electromagnetic flowmeter was used, the electromagnetic flowmeter had no obstructions in the measurement tube and clogged, adhered,
An apparatus for measuring the particle size and concentration of suspended solids which is less likely to cause a flow rate measurement error due to collision is obtained.

【0065】従って、本発明によれば、浮遊物質の濃度
が測定出来ると共に、測定流体に含まれる所定粒度の浮
遊物質の量が測定出来る浮遊物質濃度粒度測定装置を実
現することが出来る。
Therefore, according to the present invention, it is possible to realize a suspended substance concentration particle size measuring apparatus capable of measuring the concentration of suspended substance and measuring the amount of suspended substance having a predetermined particle size contained in a measurement fluid.

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

【図1】本発明の一実施例の要部構成説明図である。FIG. 1 is an explanatory diagram of a main part configuration of an embodiment of the present invention.

【図2】図1の動作説明図である。FIG. 2 is an operation explanatory diagram of FIG. 1;

【図3】本発明の他の実施例の要部構成説明図FIG. 3 is an explanatory view of a main part configuration of another embodiment of the present invention.

【図4】従来より一般に使用されている従来例の構成説
明図である。
FIG. 4 is an explanatory diagram of a configuration of a conventional example generally used in the related art.

【図5】図4の測定原理図である。FIG. 5 is a diagram illustrating the measurement principle of FIG. 4;

【符号の説明】[Explanation of symbols]

1 差圧測定装置本体 2 第1の導圧管 3 第2の導圧管 4 演算器 A スタンド B 水槽 C 測定流体源 C1 演算器 C2 演算器 C3 演算器 D 表示器 F1 流量計 F2 流量計 F3 流量計 FL 測定流体 LC1 液位コントローラ LC2 液位コントローラ LC3 液位コントローラ M1 浮遊物質濃度測定装置本体 M2 浮遊物質濃度測定装置本体 M3 浮遊物質濃度測定装置本体 PU1 ポンプ PU2 ポンプ PU3 ポンプ PU4 ポンプ PU5 ポンプ S0 分離器 S1 分離器 S2 分離器 TA1 第1の測定槽 TA2 第2の測定槽 TA3 第3の測定槽 DESCRIPTION OF SYMBOLS 1 Differential pressure measuring device main body 2 1st impulse line 3 2nd impulse line 4 Computing unit A Stand B Water tank C Measurement fluid source C1 Computing unit C2 Computing unit C3 Computing unit D Display F1 Flow meter F2 Flow meter F3 Flow meter FL Measurement fluid LC1 Liquid level controller LC2 Liquid level controller LC3 Liquid level controller M1 Floating substance concentration measuring apparatus main body M2 Floating substance concentration measuring apparatus main body M3 Floating substance concentration measuring apparatus main body PU1 Pump PU2 Pump PU3 Pump PU4 Pump PU5 Pump S0 Separator S1 Separator S2 Separator TA1 First measuring tank TA2 Second measuring tank TA3 Third measuring tank

───────────────────────────────────────────────────── フロントページの続き (72)発明者 越智 隆志 東京都武蔵野市中町2丁目9番32号 横河 電機株式会社内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Takashi Ochi 2-9-132 Nakamachi, Musashino City, Tokyo Inside Yokogawa Electric Corporation

Claims (8)

【特許請求の範囲】[The claims] 【請求項1】多段にカスケ−ド接続されて設けられ測定
流体が蓄えられる測定槽と、 この測定槽に蓄えられる測定流体流量を測定する流量計
と、 前記測定槽に設けられ前記測定流体の浮遊物質混入濃度
を測定する浮遊物質濃度測定装置本体と、 前記測定槽間に設けられ所定粒度の浮遊物質を分離する
分離器とを具備したことを特徴とする浮遊物質濃度粒度
測定装置。
1. A measuring tank provided in a multi-stage cascade connection and storing a measuring fluid, a flow meter for measuring a flow rate of the measuring fluid stored in the measuring tank, A suspended substance concentration particle size measuring apparatus, comprising: a suspended substance concentration measuring apparatus main body for measuring the concentration of suspended substance mixed therein; and a separator provided between the measurement tanks for separating suspended substance having a predetermined particle size.
【請求項2】測定流体が蓄えられる測定槽と、 この測定槽に蓄えられる測定流体流量を測定する流量計
と、 前記測定槽に設けられ前記測定流体の浮遊物質混入濃度
を測定する浮遊物質濃度測定装置本体と、 前記測定槽の下流に設けられ所定粒度の浮遊物質を分離
する分離器とを具備し、 前記分離器より流出した前記測定流体を前記測定槽に所
定回数戻すようにしたことを特徴とする浮遊物質濃度粒
度測定装置。
2. A measuring tank for storing a measuring fluid, a flow meter for measuring a flow rate of the measuring fluid stored in the measuring tank, and a floating substance concentration provided in the measuring tank for measuring a concentration of a floating substance mixed in the measuring fluid. A measuring device main body, and a separator provided downstream of the measuring tank for separating suspended substances having a predetermined particle size, wherein the measuring fluid flowing out of the separator is returned to the measuring tank a predetermined number of times. Characteristic particle size analyzer for suspended solids.
【請求項3】前記流量計と前記浮遊物質濃度測定装置本
体との測定信号から前記分離器で分離された浮遊物質重
量を演算する演算器を具備したことを特徴とする請求項
1又は請求項2記載の浮遊物質濃度粒度測定装置。
3. An arithmetic unit for calculating a weight of the suspended substance separated by the separator from a measurement signal of the flow meter and the main body of the suspended substance concentration measuring device.
An apparatus for measuring the concentration of suspended solids according to claim 1 or 2.
【請求項4】前記分離器が複数使用され、装置の上流側
から下流側に分離される前記所定粒度の大きさが順次小
さくなるように設定されたことを特徴とする請求項1乃
至請求項3の何れかに記載の浮遊物質濃度粒度測定装
置。
4. The apparatus according to claim 1, wherein a plurality of said separators are used, and said predetermined particle size separated from an upstream side of said apparatus to a downstream side thereof is set so as to decrease sequentially. 4. The suspended solid concentration particle size measuring apparatus according to any one of 3.
【請求項5】前記分離器により分離された前記浮遊物質
重量から前記測定流体の浮遊物質の粒度分布を表示する
表示器を具備したことを特徴とする請求項1乃至請求項
4の何れかに記載の浮遊物質濃度粒度測定装置。
5. The display according to claim 1, further comprising a display for displaying a particle size distribution of the suspended substance of the measurement fluid from the weight of the suspended substance separated by the separator. An apparatus for measuring suspended solids concentration and particle size as described above.
【請求項6】前記分離機として、フィルタが使用された
ことを特徴とする請求項1乃至請求項5の何れかに記載
の浮遊物質濃度粒度測定装置。
6. The particle size measuring apparatus according to claim 1, wherein a filter is used as the separator.
【請求項7】前記フィルタとして、オートクリーンフィ
ルタが使用されたことを特徴とする請求項6記載の浮遊
物質濃度粒度測定装置。
7. The apparatus according to claim 6, wherein an auto-clean filter is used as said filter.
【請求項8】前記流量計として、電磁流量計が使用され
たことを特徴とする請求項1乃至請求項7の何れかに記
載の浮遊物質濃度粒度測定装置。
8. The apparatus according to claim 1, wherein an electromagnetic flowmeter is used as said flowmeter.
JP2001061389A 2001-03-06 2001-03-06 Measuring instrument for measuring concentration and particle size of floating substance Pending JP2002257709A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001061389A JP2002257709A (en) 2001-03-06 2001-03-06 Measuring instrument for measuring concentration and particle size of floating substance

Publications (1)

Publication Number Publication Date
JP2002257709A true JP2002257709A (en) 2002-09-11

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Family Applications (1)

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005114664A (en) * 2003-10-10 2005-04-28 Rion Co Ltd Device for particle detection
CN108732072A (en) * 2017-04-19 2018-11-02 西门子公司 Method and apparatus for adjusting smoke detector

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005114664A (en) * 2003-10-10 2005-04-28 Rion Co Ltd Device for particle detection
CN108732072A (en) * 2017-04-19 2018-11-02 西门子公司 Method and apparatus for adjusting smoke detector

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