JP2002350315A - Suspended solids quantity measuring device - Google Patents

Suspended solids quantity measuring device

Info

Publication number
JP2002350315A
JP2002350315A JP2001154998A JP2001154998A JP2002350315A JP 2002350315 A JP2002350315 A JP 2002350315A JP 2001154998 A JP2001154998 A JP 2001154998A JP 2001154998 A JP2001154998 A JP 2001154998A JP 2002350315 A JP2002350315 A JP 2002350315A
Authority
JP
Japan
Prior art keywords
measuring
suspended
concentration
tank
substance
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
JP2001154998A
Other languages
Japanese (ja)
Inventor
Saichiro Morita
佐一郎 森田
Tetsuya Sumi
哲也 角
Hideaki Komiya
秀昭 小宮
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 JP2001154998A priority Critical patent/JP2002350315A/en
Publication of JP2002350315A publication Critical patent/JP2002350315A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide an efficient measuring device which can measure the quantity of suspended solids. SOLUTION: The suspended solids quantity measuring device is charecterized by that it is provided with a measuring tank wherein the suspended solid-mixed fluid is stored, a feeder pump feeding the suspended solids-mixed fluid into the measuring tank, a first flowmeter measuring the quantity of the suspended solid-mixed fluid flown in the measuring tank, a suspended solids density measuring device installed in the tank for measuring the mixing concentration of the suspended solids-mixed fluid, an injector pump pouring a diluted suspended solids-mixed fluid into the measuring tank, a second flowmeter measuring the injection rate of the diluted suspended solids-mixed fluid, and a control device controlling operations of both the feeder/injector pumps based on each measurement signal for the suspended solids concentration measuring device, the first flowmeter and the second flowmeter so as to allow the mixing concentration of the suspended solids-mixed fluid in the measuring tank to be a prescribed concentration.

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、浮遊物質量が測定
出来、且つ、効率の良い浮遊物質量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 for measuring the amount of suspended solids which can measure the amount of suspended solids and which is efficient.

【0002】[0002]

【従来の技術】図3は、従来より一般に使用されている
従来例の浮遊物質濃度測定装置の構成説明図で、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4は図3の測定原
理図である。
2. Description of the Related Art FIG. 3 is an explanatory view of the structure of a conventional floating substance concentration measuring apparatus generally used in the prior art, which is used in a dam to measure the concentration of suspended solids when suspended sand corresponds to suspended substances. This is an example. FIG. 4 is a diagram showing the measurement principle of FIG.

【0003】図3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. 3, 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。
[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.

【0005】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。
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 and the predetermined density of the measurement fluid in which the suspended substance is not mixed. From this, the suspended substance concentration of this measurement fluid is calculated. In this case, the arithmetic unit 4 is built in the converter.

【0006】以上の構成において、図4により、浮遊物
質濃度測定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。
[0006] In the above configuration, the measurement principle of the suspended solid concentration measuring 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.

【0007】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。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。
[0007] The first impulse line 2 and the second impulse line 3 are
It is inserted at a predetermined position in the water tank B. 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.

【0008】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)

【0009】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 equations (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

【0010】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

【0011】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 tip 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.

【0012】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.

【0013】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 Equation (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).

【0014】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 stores in advance H, ρ0, and the reference density of water in a state in which suspended matter is not mixed, as a known value, and the arithmetic unit 4 calculates the calculated average density of water. The difference between ρ and the stored reference density is calculated and output as an index of the concentration of suspended solids.

【0015】[0015]

【発明が解決しようとする課題】ここで、浮遊物質混入
流体中の沈殿、堆積した浮遊物質を浮遊物質混入流体に
混ぜて排出使用とする考えがある、これは、例えば、ダ
ムに堆積した浮遊砂を水に混ぜて排出しようとする場合
に有効である。
Here, there is a concept that the sediment in the fluid containing the suspended substance and the accumulated suspended substance are mixed with the fluid containing the suspended substance to be used for discharge. It is effective when sand is to be mixed with water to discharge.

【0016】この場合、浮遊砂を水に混ぜて排出しただ
けでは、どのくらいの量の浮遊砂が有効に排出された
か、また、高濃度のため浮遊物質は沈殿し易く、どのく
らいの濃度が有効であるか、また、有効な排出濃度を維
持し続ける事も出来ない。
In this case, the amount of suspended sand effectively discharged only by mixing the suspended sand with the water and discharging, and the suspended matter is liable to precipitate due to the high concentration, and the concentration of the suspended matter is effective. Yes, and they cannot maintain effective emission concentrations.

【0017】本発明の目的は、上記の課題を解決するも
ので、浮遊物質量が測定出来、且つ、効率の良い浮遊物
質量測定装置を提供することにある。
An object of the present invention is to solve the above-mentioned problems and to provide an apparatus for measuring the amount of suspended solids which can measure the amount of suspended solids and which is efficient.

【0018】[0018]

【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の浮遊物質量測定装置
においては、浮遊物質混入流体が蓄えられる測定槽と、
この測定槽に前記浮遊物質混入流体を送る送入ポンプ
と、前記測定槽に流入される前記浮遊物質混入流体の量
を測定する第1の流量計と、前記測定槽に設けられ前記
浮遊物質混入流体の浮遊物質混入濃度を測定する浮遊物
質濃度測定装置と、前記測定槽に希釈された浮遊物質混
入流体を注入する注入ポンプと、前記希釈された浮遊物
質混入流体の注入量を測定する第2の流量計と、前記測
定槽内の前記浮遊物質混入流体濃度が所定濃度となるよ
うに前記浮遊物質濃度測定装置,前記第1と第2の流量
計の測定信号に基づき前記送入,注入ポンプの動作を制
御する制御装置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, there is provided an apparatus for measuring the amount of suspended solids, comprising: a measuring tank for storing a fluid mixed with suspended solids;
A feed pump for sending the floating substance-mixed fluid to the measurement tank, a first flow meter for measuring the amount of the floating substance-mixed fluid flowing into the measurement tank, and the floating substance mixing fluid provided in the measurement tank. A floating substance concentration measuring device for measuring the suspended substance mixed concentration of the fluid, an injection pump for injecting the diluted floating substance mixed fluid into the measurement tank, and a second measuring the injection amount of the diluted suspended substance mixed fluid. And the feed / injection pump based on measurement signals from the suspended substance concentration measuring device and the first and second flow meters so that the concentration of the suspended substance mixed fluid in the measurement tank becomes a predetermined concentration. And a control device for controlling the operation of (1).

【0019】本発明の請求項2の浮遊物質量測定装置に
おいて、浮遊物質混入流体が予め蓄えられる調整槽と、
浮遊物質混入流体が蓄えられる測定槽と、この測定槽に
前記調整槽から前記浮遊物質混入流体を送る送入ポンプ
と、前記測定槽に流入される前記浮遊物質混入流体の量
を測定する流量計と、前記測定槽に設けられ前記浮遊物
質混入流体の浮遊物質混入濃度を測定する浮遊物質濃度
測定装置と、前記調整槽に希釈された浮遊物質混入流体
を注入する注入ポンプと、前記調整槽内の前記浮遊物質
混入流体濃度が所定濃度となるように前記浮遊物質濃度
測定装置,前記流量計の測定信号に基づき前記送入,注
入ポンプの動作を制御する制御装置とを具備したことを
特徴とする。
In the apparatus for measuring the amount of suspended solids according to the second aspect of the present invention, an adjusting tank in which a fluid mixed with suspended solids is stored in advance;
A measuring tank in which a suspended substance-mixed fluid is stored, a feed pump for sending the suspended substance-mixed fluid from the adjustment tank to the measurement tank, and a flow meter for measuring an amount of the suspended substance-mixed fluid flowing into the measurement tank A floating substance concentration measuring device provided in the measurement tank for measuring the concentration of the floating substance mixed in the floating substance mixed fluid; an injection pump for injecting the diluted floating substance mixed fluid into the adjustment tank; And a controller for controlling the operation of the feed / injection pump based on the measurement signal of the flow meter so that the concentration of the fluid mixed with the floating substance becomes a predetermined concentration. I do.

【0020】本発明の請求項3においては、請求項1又
は請求項2記載の浮遊物質量測定装置において、前記流
量計の測定信号と前記浮遊物質濃度測定装置の測定信号
とから浮遊物質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, in the apparatus for measuring the amount of suspended solids according to the first or second aspect, the amount of suspended solids is determined from a measurement signal of the flow meter and a measurement signal of the concentration of suspended solids. It is characterized by having a computing unit for computing.

【0021】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量測定装置におい
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 a fourth aspect of the present invention, in the apparatus for measuring the amount of suspended solids according to any one of the first to third aspects, an electromagnetic flowmeter is used as the flowmeter.

【0022】[0022]

【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、ダムにおいて、堆積された浮遊砂を水に混ぜて排出
する場合の、浮遊砂量測定装置として使用された例に付
いて示す。図において、図3と同一記号の構成は同一機
能を表す。以下、図3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 of an embodiment of the present invention, showing an example of a dam used as a suspended sand amount measuring device in a case where accumulated suspended sand is mixed with water and discharged in a dam. In the figure, the configuration of the same symbol as in FIG. 3 indicates the same function. Hereinafter, only differences from FIG. 3 will be described.

【0023】図において、11は、浮遊物質混入流体が
蓄えられる測定槽である。この場合は、浮遊物質は浮遊
砂である。また、この場合は、測定槽11は、浮遊物質
混入流体が所定水位に達した際にオーバーフローする構
造となっている。即ち、測定槽11内に堰111が設け
られている。
In the figure, reference numeral 11 denotes a measuring tank for storing a fluid mixed with suspended substances. In this case, the suspended matter is suspended sand. In this case, the measuring tank 11 has a structure that overflows when the suspended substance-mixed fluid reaches a predetermined water level. That is, the weir 111 is provided in the measurement tank 11.

【0024】12は、この測定槽11に浮遊物質混入流
体を送る送入ポンプである。この場合は、送入ポンプ1
2は、ダムの貯水池Cより、高濃度の浮遊砂の混じった
水を取り入れる。
Reference numeral 12 denotes a feed pump for sending a fluid containing suspended substances to the measuring tank 11. In this case, the feed pump 1
No. 2 takes in water with a high concentration of suspended sand from reservoir C of the dam.

【0025】13は、測定槽11に流入される浮遊物質
混入流体の量を、測定する第1の流量計である。この場
合は、電磁流量計が使用されている。
Reference numeral 13 denotes a first flow meter for measuring the amount of the suspended substance-containing fluid flowing into the measuring tank 11. In this case, an electromagnetic flow meter is used.

【0026】14は、測定槽11に設けられ、浮遊物質
混入流体の浮遊物質混入濃度を測定する浮遊物質濃度測
定装置である。15は、測定槽11に、希釈された浮遊
物質混入流体を注入する注入ポンプである。
Reference numeral 14 denotes a floating substance concentration measuring device provided in the measuring tank 11 for measuring the concentration of the floating substance mixed in the fluid mixed with the floating substance. Reference numeral 15 denotes an injection pump for injecting the diluted suspended substance mixed fluid into the measurement tank 11.

【0027】この場合は、ダムの近くの河川Dから、低
濃度の浮遊砂の混じった水を取り入れる。16は、希釈
された浮遊物質混入流体の注入量を、測定する第2の流
量計である。この場合は、電磁流量計が使用されてい
る。
In this case, water mixed with suspended sand of low concentration is taken in from the river D near the dam. Reference numeral 16 denotes a second flow meter for measuring the injection amount of the diluted suspended substance-containing fluid. In this case, an electromagnetic flow meter is used.

【0028】17は、測定槽11内の浮遊物質混入流体
濃度が所定濃度となるように、浮遊物質濃度測定装置1
4,第1と第2の流量計13と16の測定信号に基づ
き、ポンプ12,15の動作を制御する制御装置であ
る。
Reference numeral 17 denotes a floating substance concentration measuring device 1 so that the concentration of the fluid mixed with the floating substance in the measuring tank 11 becomes a predetermined concentration.
4, a control device for controlling the operation of the pumps 12, 15 based on the measurement signals of the first and second flow meters 13 and 16.

【0029】18は、浮遊物質濃度測定装置14の測定
値を表示すると共に、浮遊物質濃度測定装置14の測定
信号を制御部に伝送する表示・伝送部である。なお、流
量計計13,16の測定信号と浮遊物質濃度測定装置1
4の測定信号とから浮遊物質量を演算する演算器は、こ
の場合は、制御装置17に内蔵されている。
Reference numeral 18 denotes a display / transmission unit which displays a measurement value of the suspended substance concentration measuring device 14 and transmits a measurement signal of the suspended substance concentration measuring device 14 to the control unit. The measurement signals of the flow meters 13 and 16 and the suspended solid concentration measurement device 1
In this case, a calculator for calculating the amount of suspended solids from the measurement signal of No. 4 is built in the control device 17.

【0030】以上の構成において、浮遊砂を含む水は、
ダムの貯水池Aから送水ポンプ12により、測定槽11
内に導かれる。送水量は、第1の流量計13により測定
される。
In the above configuration, the water containing suspended sand is
From the reservoir A of the dam to the measuring tank 11 by the water pump 12
Guided inside. The flow rate is measured by the first flow meter 13.

【0031】一方、注入ポンプ15により、希釈された
浮遊物質混入流体が、測定槽11に注入される。測定槽
11内で、浮遊物質濃度測定装置14により、浮遊砂を
含む水の濃度が測定される
On the other hand, the diluted suspended substance-mixed fluid is injected into the measuring tank 11 by the injection pump 15. In the measuring tank 11, the concentration of water containing suspended sand is measured by the suspended solid concentration measuring device 14.

【0032】測定槽11内の浮遊砂濃度は、制御部17
により、一定の所定濃度に制御される。測定された浮遊
砂を含む水は、測定槽11内に設けられた堰11からオ
ーバフローして排出口へと導かれ排出される。このよう
にして、流量と濃度とにより、排出された浮遊砂の量が
計測出来る。即ち、どれだけの量の浮遊砂が排出された
か、数値として求めることが出来る。
The suspended sand concentration in the measuring tank 11 is controlled by the controller 17.
Is controlled to a constant predetermined density. The measured water containing suspended sand overflows from the weir 11 provided in the measuring tank 11, is guided to the outlet, and is discharged. In this way, the amount of suspended sand discharged can be measured based on the flow rate and the concentration. That is, the amount of suspended sand discharged can be obtained as a numerical value.

【0033】この結果、 (1)高濃度の浮遊砂を含む水の流量と濃度を測定する
ことにより、高濃度の浮遊砂量を求めることが出来、排
出された高濃度の浮遊砂の総量を知ることが出来る浮遊
物質量測定装置が得られる。
As a result, (1) By measuring the flow rate and concentration of water containing high-concentration suspended sand, the amount of high-concentration suspended sand can be obtained, and the total amount of discharged high-concentration suspended sand can be calculated. An apparatus for measuring the amount of suspended solids that can be known is obtained.

【0034】(2)高濃度の浮遊砂を含む水を排出する
際に、その濃度を測定し、一定基準値以下の濃度で排出
する事により、下流の河川水の浮遊砂濃度を一定値以下
に抑えることが出来、環境への悪影響を抑えることが出
来る浮遊物質量測定装置が得られる。
(2) When discharging water containing a high concentration of suspended sand, the concentration of the suspended sand is measured and discharged at a concentration lower than a certain reference value, so that the concentration of suspended sand in the downstream river water is kept below a certain value. Thus, an apparatus for measuring the amount of suspended solids that can suppress adverse effects on the environment can be obtained.

【0035】(3)下流に流出する浮遊砂の濃度をつか
む事により、下流の河川全体の浮遊砂濃度を推定し、河
川全体の浮遊砂濃度とその経過時間との積を1つの指標
として、環境への影響を最低限になるように、コントロ
ールすることが出来る浮遊物質量測定装置が得られる。
(3) By grasping the concentration of suspended sand flowing out downstream, the suspended sand concentration of the entire downstream river is estimated, and the product of the suspended sand concentration of the entire river and its elapsed time is used as one index. An apparatus for measuring the amount of suspended solids that can be controlled so as to minimize the effect on the environment is obtained.

【0036】(4)流量計の測定信号と浮遊物質濃度測
定装置の測定信号とから浮遊物質量を演算する演算器が
使用されたので、浮遊物質量がリアルタイムに測定出来
る浮遊物質量測定装置が得られる。
(4) Since an arithmetic unit for calculating the amount of suspended solids is used from the measurement signal of the flow meter and the measurement signal of the suspended solid concentration measuring device, an apparatus for measuring the amount of suspended solids in real time can be provided. can get.

【0037】(5)流量計として電磁流量計が使用され
たので、浮遊物質混入流体がスラリー状あるいは小固形
物質を含む場合にも、測定誤差を生じない浮遊物質量測
定装置が得られる。
(5) Since the electromagnetic flow meter is used as the flow meter, a floating substance amount measuring apparatus which does not cause a measurement error even when the suspended substance mixed fluid contains a slurry or a small solid substance can be obtained.

【0038】図2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、調整槽21に、浚渫ポ
ンプ22により、ダムの貯水池Aより、高濃度の浮遊砂
の混じった水を取り入れる。
FIG. 2 is an explanatory view of a main part configuration of another embodiment of the present invention. In the present embodiment, water mixed with high-concentration suspended sand is taken into the adjusting tank 21 from the reservoir A of the dam by the dredging pump 22.

【0039】送入ポンプ23は、調整槽21から測定槽
11に浮遊物質混入流体を送る。注入ポンプ24は、調
整槽21に希釈された浮遊物質混入流体を注入する。制
御装置25は、調整槽21内の浮遊物質混入流体濃度が
所定濃度となるように、浮遊物質濃度測定装置14,流
量計13の測定信号に基づき、送入,注入ポンプ23,
24の動作を制御する。
The feed pump 23 sends the fluid containing suspended substances from the adjusting tank 21 to the measuring tank 11. The injection pump 24 injects the diluted suspended substance-mixed fluid into the adjustment tank 21. The control device 25 controls the feeding, injecting pump 23,
24 is controlled.

【0040】この結果、高価な流量計16を減らす事が
出来、安価な浮遊物質量測定装置が得られる。
As a result, the number of expensive flow meters 16 can be reduced, and an inexpensive suspended solids amount measuring device can be obtained.

【0041】なお、前述の実施例においては、測定槽1
1は堰111を有すると説明したが、これに限る事は無
く、要するに、浮遊物質混入流体が蓄えられる測定槽で
あれば良い。
In the above embodiment, the measuring tank 1 was used.
Although 1 has been described as having the weir 111, the present invention is not limited to this, and it is only necessary that the measuring tank be a storage tank that stores the fluid mixed with suspended substances.

【0042】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 is to be noted that the above description has shown only specific preferred embodiments for the purpose of explanation and illustration of the present 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.

【0043】[0043]

【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。 (1)高濃度の浮遊物質混入流体の流量と濃度を測定す
ることにより、高濃度の浮遊物質混入流体の量を求める
ことが出来、排出された高濃度の浮遊物質の総量を知る
ことが出来る浮遊物質量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. (1) By measuring the flow rate and concentration of the high-concentration suspended substance-containing fluid, the amount of the high-concentration suspended substance-containing fluid can be obtained, and the total amount of the discharged high-concentration suspended substance can be known. An apparatus for measuring the amount of suspended solids is obtained.

【0044】(2)高濃度の浮遊物質混入流体を排出す
る際に、その濃度を測定し、一定基準値以下の濃度で排
出する事により、下流の河川水の浮遊物質混入流体の濃
度を一定値以下に抑えることが出来、環境への悪影響を
抑えることが出来る浮遊物質量測定装置が得られる。
(2) When discharging a fluid having a high concentration of suspended solids, the concentration is measured and the concentration of the suspended solids is reduced by discharging the fluid at a concentration lower than a predetermined reference value. Thus, an apparatus for measuring the amount of suspended solids that can be suppressed to a value equal to or less than the value and the adverse effect on the environment can be obtained.

【0045】(3)下流に流出する浮遊物質の濃度をつ
かむ事により、下流の河川全体の浮遊物質濃度を推定
し、河川全体の浮遊物質濃度とその経過時間との積を1
つの指標として、環境への影響を最低限になるように、
コントロールすることが出来る浮遊物質量測定装置が得
られる。
(3) By determining the concentration of suspended solids flowing downstream, the concentration of suspended solids in the entire downstream river is estimated, and the product of the concentration of suspended solids in the entire river and the elapsed time is 1
One indicator is to minimize environmental impact,
An apparatus for measuring the amount of suspended solids that can be controlled is obtained.

【0046】本発明の請求項2によれば、次のような効
果がある。高価な流量計を減らす事が出来、安価な浮遊
物質量測定装置が得られる。
According to the second aspect of the present invention, the following effects can be obtained. An expensive flow meter can be reduced, and an inexpensive suspended solids amount measuring device can be obtained.

【0047】本発明の請求項3によれば、次のような効
果がある。流量計の測定信号と浮遊物質濃度測定装置の
測定信号とから浮遊物質量を演算する演算器が使用され
たので、浮遊物質量がリアルタイムに測定出来る浮遊物
質量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 an arithmetic unit for calculating the amount of suspended solids from the measurement signal of the flow meter and the measurement signal of the suspended solid concentration measuring device is used, a suspended solid amount measuring device capable of measuring the amount of suspended solids in real time is obtained.

【0048】本発明の請求項4によれば、次のような効
果がある。流量計として電磁流量計が使用されたので、
浮遊物質混入流体がスラリー状あるいは小固形物質を含
む場合にも測定誤差を生じない浮遊物質量測定装置が得
られる。
According to the fourth aspect of the present invention, the following effects can be obtained. Since an electromagnetic flowmeter was used as the flowmeter,
An apparatus for measuring the amount of suspended solids which does not cause a measurement error even when the fluid containing suspended solids contains a slurry or a small solid substance is obtained.

【0049】従って、本発明によれば、浮遊物質量が測
定出来、且つ、効率の良い浮遊物質量測定装置を実現す
ることが出来る。
Therefore, according to the present invention, the amount of suspended solids can be measured and an apparatus for measuring the amount of suspended solids with high efficiency can be realized.

【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】本発明の他の実施例の要部構成説明図FIG. 2 is an explanatory view of a main part configuration of another embodiment of the present invention.

【図3】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. 3 is an explanatory diagram of a configuration of a conventional example generally used in the related art.

【図4】図3の測定原理図である。FIG. 4 is a measurement principle diagram of FIG.

【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 11 測定槽 111 堰 12 送入ポンプ 13 第1の流量計 14 浮遊物質濃度測定装置 15 注入ポンプ 16 第2の流量計 17 制御装置 18 表示・伝送部 21 調整槽 22 浚渫ポンプ 23 送入ポンプ 24 注入ポンプ 25 制御装置 A スタンド B 水槽 C ダムの貯水池 D 河川 DESCRIPTION OF SYMBOLS 1 Differential pressure measuring device main body 2 1st impulse line 3 2nd impulse line 4 Computing unit 11 Measurement tank 111 Weir 12 Inlet pump 13 First flow meter 14 Floating substance concentration measuring device 15 Injection pump 16 Second flow rate Total 17 Control unit 18 Display / Transmission unit 21 Adjustment tank 22 Dredge pump 23 Inlet pump 24 Injection pump 25 Control unit A Stand B Water tank C Dam reservoir D River

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 2F035 AA03 2G052 AA06 AB00 AC03 AC06 AC12 AD09 AD29 AD49 BA05 BA14 CA02 CA04 CA08 CA12 CA29 CA36 CA38 DA00 DA22 GA21 HA01 HA15 HB10 HC04 HC24 HC28 HC38 HC44 JA09 JA23 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 2F035 AA03 2G052 AA06 AB00 AC03 AC06 AC12 AD09 AD29 AD49 BA05 BA14 CA02 CA04 CA08 CA12 CA29 CA36 CA38 DA00 DA22 GA21 HA01 HA15 HB10 HC04 HC24 HC28 HC38 HC44 JA09 JA23

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】浮遊物質混入流体が蓄えられる測定槽と、 この測定槽に前記浮遊物質混入流体を送る送入ポンプ
と、 前記測定槽に流入される前記浮遊物質混入流体の量を測
定する第1の流量計と、 前記測定槽に設けられ前記浮遊物質混入流体の浮遊物質
混入濃度を測定する浮遊物質濃度測定装置と、 前記測定槽に希釈された浮遊物質混入流体を注入する注
入ポンプと、 前記希釈された浮遊物質混入流体の注入量を測定する第
2の流量計と、 前記測定槽内の前記浮遊物質混入流体濃度が所定濃度と
なるように前記浮遊物質濃度測定装置,前記第1と第2
の流量計の測定信号に基づき前記送入,注入ポンプの動
作を制御する制御装置とを具備したことを特徴とする浮
遊物質量測定装置。
1. A measuring tank for storing a floating substance mixed fluid, a feed pump for sending the floating substance mixed fluid to the measuring tank, and a measuring tank for measuring an amount of the floating substance mixed fluid flowing into the measuring tank. A flow meter of 1, a floating substance concentration measuring device provided in the measuring tank for measuring a floating substance mixed concentration of the floating substance mixed fluid, and an injection pump for injecting the diluted floating substance mixed fluid into the measuring tank. A second flowmeter for measuring an injection amount of the diluted suspended substance-containing fluid; and a floating substance concentration measuring device, the first and the second components, such that the concentration of the suspended substance-containing fluid in the measurement tank becomes a predetermined concentration. Second
A controller for controlling the operation of the feed / injection pump based on the measurement signal of the flowmeter.
【請求項2】浮遊物質混入流体が予め蓄えられる調整槽
と、 浮遊物質混入流体が蓄えられる測定槽と、 この測定槽に前記調整槽から前記浮遊物質混入流体を送
る送入ポンプと、 前記測定槽に流入される前記浮遊物質混入流体の量を測
定する流量計と、 前記測定槽に設けられ前記浮遊物質混入流体の浮遊物質
混入濃度を測定する浮遊物質濃度測定装置と、 前記調整槽に希釈された浮遊物質混入流体を注入する注
入ポンプと、 前記調整槽内の前記浮遊物質混入流体濃度が所定濃度と
なるように前記浮遊物質濃度測定装置,前記流量計の測
定信号に基づき前記送入,注入ポンプの動作を制御する
制御装置とを具備したことを特徴とする浮遊物質量測定
装置。
2. An adjusting tank in which a floating substance mixed fluid is stored in advance, a measuring tank in which a floating substance mixed fluid is stored, a feed pump for sending the floating substance mixed fluid from the adjusting tank to the measuring tank, A flowmeter for measuring an amount of the suspended-substance-mixed fluid flowing into the tank; a suspended-substance-concentration measuring device provided in the measurement tank to measure a suspended-substance-concentrated concentration of the suspended-substance-mixed fluid; An injection pump for injecting the suspended-floating substance-mixed fluid, and the inflow and outflow based on the measurement signals from the suspended-substance-concentration measuring device and the flowmeter so that the concentration of the floating-substance-mixed fluid in the adjustment tank becomes a predetermined concentration. A floating substance amount measuring device, comprising: a control device for controlling an operation of an infusion pump.
【請求項3】前記流量計の測定信号と前記浮遊物質濃度
測定装置の測定信号とから浮遊物質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
の浮遊物質量測定装置。
3. The floating substance according to claim 1, further comprising an arithmetic unit for calculating a floating substance amount from a measurement signal of the flow meter and a measurement signal of the floating substance concentration measuring device. Quantity measuring device.
【請求項4】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3の何れかに記載
の浮遊物質量測定装置。
4. An apparatus according to claim 1, wherein an electromagnetic flowmeter is used as said flowmeter.
JP2001154998A 2001-05-24 2001-05-24 Suspended solids quantity measuring device Pending JP2002350315A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001154998A JP2002350315A (en) 2001-05-24 2001-05-24 Suspended solids quantity measuring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001154998A JP2002350315A (en) 2001-05-24 2001-05-24 Suspended solids quantity measuring device

Publications (1)

Publication Number Publication Date
JP2002350315A true JP2002350315A (en) 2002-12-04

Family

ID=18999253

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001154998A Pending JP2002350315A (en) 2001-05-24 2001-05-24 Suspended solids quantity measuring device

Country Status (1)

Country Link
JP (1) JP2002350315A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004271297A (en) * 2003-03-07 2004-09-30 Seishin Engineering Kk Test water supplying device
WO2007023705A1 (en) * 2005-08-25 2007-03-01 Ias Inc. Solution feeding device
JP2013024631A (en) * 2011-07-19 2013-02-04 Hazama Corp Density measurement device of muddy water or the like

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004271297A (en) * 2003-03-07 2004-09-30 Seishin Engineering Kk Test water supplying device
WO2007023705A1 (en) * 2005-08-25 2007-03-01 Ias Inc. Solution feeding device
US8453524B2 (en) 2005-08-25 2013-06-04 Ias Inc. Solution feeding device
JP2013024631A (en) * 2011-07-19 2013-02-04 Hazama Corp Density measurement device of muddy water or the like

Similar Documents

Publication Publication Date Title
CN211571596U (en) Dam burst test composite simulation device based on real-time storage capacity adjustment
CN202002684U (en) Metering device with wide measuring range
CN104501916A (en) Liquid calibration system and calibration method thereof
RU172725U1 (en) TURBINE GAS FLOW METER
JP2002350315A (en) Suspended solids quantity measuring device
CN204064392U (en) A kind of bubble method liquid level emasuring device
CN105256860A (en) Pressure-superposed water supply pressure-stabilized tank and method for measuring gas missing amount
RU168831U1 (en) Gas flow meter
CN101872200B (en) Flow control device
CN102435266B (en) The permanent head water system of flow measurement device
RU169460U1 (en) Gas flow meter
KR101208330B1 (en) Method for measuring non-full flow using multiple sensors
CN202372236U (en) Constant water head water supply system of flow measuring device
CN208818266U (en) A kind of field amount water installations
CN204575676U (en) A kind of ultrasonic device for measuring flow rate of liquid
CN110887536A (en) Water-blocking type flow measuring device
CN207523887U (en) A kind of marine fuel oil monitoring system of single current gauge
CN206975514U (en) Diversion automatic control system
CN213203535U (en) Detergent adding device
CN214474639U (en) Intelligent injection control device for trace gasoline antistatic agent
CN218211505U (en) Liquid level monitoring facilities is put in to medicament
CN211198708U (en) Water treatment medicine system
CN107543587A (en) Flow measuring apparatus is blended in a kind of gas-liquid two-phase
CN211813624U (en) Deoxygenated water preparation device based on PLC control
JPS61128124A (en) Flow meter