JP2000009510A - Device and method for measuring flow rate or flow velocity of slurried liquid - Google Patents

Device and method for measuring flow rate or flow velocity of slurried liquid

Info

Publication number
JP2000009510A
JP2000009510A JP10178702A JP17870298A JP2000009510A JP 2000009510 A JP2000009510 A JP 2000009510A JP 10178702 A JP10178702 A JP 10178702A JP 17870298 A JP17870298 A JP 17870298A JP 2000009510 A JP2000009510 A JP 2000009510A
Authority
JP
Japan
Prior art keywords
liquid
flow rate
slurry
pipeline
processing unit
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.)
Withdrawn
Application number
JP10178702A
Other languages
Japanese (ja)
Inventor
Susumu Hasegawa
進 長谷川
Akira Akashi
昭 赤司
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.)
Shinko Pantec Co Ltd
Original Assignee
Shinko Pantec Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shinko Pantec Co Ltd filed Critical Shinko Pantec Co Ltd
Priority to JP10178702A priority Critical patent/JP2000009510A/en
Publication of JP2000009510A publication Critical patent/JP2000009510A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To accurately measure a flow rate and a flow velocity even when the flow rate of slurried liquid is small by providing a pair of electrodes at one section in a pipeline, and detecting time when the liquid surface of the slurried liquid is brought into contact with both electrodes. SOLUTION: Electrodes 2 and 3 are provided at the lower and upper ends of one section of an upright feed pipe 1. Even after an on-off valve 5 of the feed pipe 1 is closed, time when slurried liquid surface that flows in the pipe 1 toward the on-off valve 5 and is continuously collected is brought into contact with the lower electrode 2, and time when the liquid level rises successively and is brought into contact with the upper electrode 3 are sent to an operation-processing device 4 as a detection signal, and then the on-off valve 5 is opened immediately. Based on the volume of one section of the feed pipe 1 and the detection signal of the contact time of the liquid surface with the electrodes 2 and 3, the flow rate of slurried liquid is calculated. Simultaneously, based on the value of the flow rate, flow velocity is calculated. Also, the internal diameter of the feed pipe 1 or a metering tank or the installation distance of the upper and lower electrodes is determined so that detection time difference should be within nearly 1 minute to quickly perform measuring work.

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、スラリー状液体、
特に、汚泥の流量または流速を計測するための装置と該
装置を用いたスラリー状液体の流量または流速の計測方
法に関する。
[0001] The present invention relates to a slurry-like liquid,
In particular, the present invention relates to an apparatus for measuring the flow rate or flow rate of sludge and a method for measuring the flow rate or flow rate of a slurry liquid using the apparatus.

【0002】[0002]

【従来の技術および発明が解決しようとする課題】管路
などの流路を流れる流体の計量・計測方法として、従来
より、電磁流量計や溢流堰などの、流体の物理的特性を
利用した方法が使われている。
2. Description of the Related Art As a method of measuring and measuring a fluid flowing through a flow path such as a pipeline, the physical properties of a fluid such as an electromagnetic flowmeter and an overflow weir have conventionally been used. The method is used.

【0003】すなわち、電磁流量計とは、水、海水、油
などの導電性流体が流れる管路内に、管路の軸方向に対
して直角方向に磁場を作用させることで、ファラデーの
法則によって、管路の軸方向および磁場方向のそれぞれ
の垂直方向に流速に比例して生じる起電力を検出するこ
とで管路内の流量を測定するものである。 ところが、
電磁流量計は、その計器自体が非常に高価なものである
上に、計測対象となる導電性流体を管路内に常に流動さ
せる必要があり、また、非導電性の物質が混入するとそ
の計測精度が極端に落ちるなど、その適用対象、適用箇
所が限定されているのが実情である。
[0003] In other words, an electromagnetic flowmeter applies a magnetic field to a pipe in which a conductive fluid such as water, seawater, oil, or the like flows, in a direction perpendicular to the axial direction of the pipe, and according to Faraday's law. The flow rate in the pipeline is measured by detecting an electromotive force generated in proportion to the flow velocity in each of the axial direction of the pipeline and the vertical direction of the magnetic field. However,
Electromagnetic flowmeters themselves are very expensive, and require the flow of a conductive fluid to be measured in the pipe at all times. The fact is that the application target and application location are limited, for example, the accuracy is extremely lowered.

【0004】一方で、後者の溢流堰とは、流路を堰き止
めて流体の水位を上昇させるように作られた構造体であ
る。 この溢流堰は、所定体積の流体の計量にはすこぶ
る簡便なものであるが、流体が所定体積に満たない場合
などは、流体の計量が正確にできず、また堰から溢れ出
た余剰の流体の計量もできないなど、その計量の精度の
悪さが難点とされている。
[0004] On the other hand, the latter overflow weir is a structure formed so as to block a flow passage and raise the level of fluid. This overflow weir is very simple for measuring a predetermined volume of fluid, but when the volume of the fluid is less than the predetermined volume, it is not possible to accurately measure the fluid and the excess overflowing from the weir is not possible. Poor accuracy of the measurement, such as the inability to measure the fluid, has been a drawback.

【0005】特に、スラリー状液体、とりわけ、小流量
のスラリー状液体の計量は、電磁流量計や溢流堰のいず
れによっても対応しきれないのが現状である。 これ
は、スラリー状液体、とりわけ、固形分(懸濁物質)を
含む汚泥などを、これらの計測器に適用すると、計測器
内部に汚物が付着したり、細い配管やフィルターなどで
目詰まりを生ずることなどによる。 また、これらスラ
リー状液体の流れをポンプなどで強制しても、汚泥成分
によって流路が閉塞されたり、前述したように細い配管
やフィルターなどが目詰まりを起こすなど、流体を継続
的に流動せしめることが困難であった。
In particular, at present, the measurement of a slurry-like liquid, especially a slurry-like liquid having a small flow rate, cannot be handled by any of an electromagnetic flow meter and an overflow weir. This is because, when a slurry-like liquid, especially sludge containing a solid (suspended substance), is applied to these measuring instruments, dirt adheres to the inside of the measuring instrument, and clogging occurs in thin piping and filters. It depends. In addition, even if the flow of the slurry-like liquid is forced by a pump or the like, the flow of the fluid is continuously performed, for example, the flow path is blocked by the sludge component, or the narrow pipe or the filter is clogged as described above. It was difficult.

【0006】このように、従来技術では、スラリー状液
体を的確に計量する手段の提供がなされておらず、かよ
うな計量技術の確立が当該技術分野では待望されている
のである。
As described above, the prior art does not provide a means for accurately measuring a slurry-like liquid, and the establishment of such a measuring technique is long-awaited in the technical field.

【0007】[0007]

【課題を解決するための手段】本発明は、このような当
該技術分野での実情に鑑みて発明されたものであって、
その要旨とするところは;スラリー状液体が流れる管
路、管路に接続されたスラリー状液体の流れを許容/遮
断するための開閉弁、開閉弁の上流側の管路内に管路の
軸方向に互い離間して設けられた一対の電極、および一
対の電極と連絡された演算処理装置を含むスラリー状液
体の流量または流速を計測するための装置;および管路
内を流れるスラリー状液体の流量または流速の計測方法
であって、(a)管路内の一区間の下端に位置する下位電
極にてスラリー状液体の液面の接触を検知し、その検知
信号(T0)を演算処理装置に送信し、(b)該一区間の上端
に位置する上位電極にてスラリー状液体の液面の接触を
検知し、その検知信号(T1)を演算処理装置に送信し、お
よび(c)演算処理装置で、検知信号の受信時間の差(T1
T0)と該一区間の容積に基づいて、管路内を流れるスラ
リー状液体の流量または流速を算出する、工程を含む管
路内を流れるスラリー状液体の流量または流速の計測方
法にある。
SUMMARY OF THE INVENTION The present invention has been made in view of such a situation in the technical field,
The gist thereof is as follows: a pipeline through which the slurry-like liquid flows, an on-off valve for allowing / cutting off the flow of the slurry-like liquid connected to the pipeline, and a shaft of the pipeline in the pipeline upstream of the on-off valve. A device for measuring a flow rate or a flow rate of a slurry-like liquid including a pair of electrodes provided apart from each other in a direction, and an arithmetic processing unit connected to the pair of electrodes; and a slurry-like liquid flowing in a pipeline. A method for measuring a flow rate or a flow velocity, in which (a) a lower electrode located at the lower end of one section in a pipeline detects contact of the liquid surface of a slurry-like liquid, and the detection signal (T 0 ) is processed. (B) detecting contact of the liquid surface of the slurry-like liquid with the upper electrode located at the upper end of the section, transmitting a detection signal (T 1 ) to the arithmetic processing unit, and (c) ) The difference in detection signal reception time (T 1
A method for measuring the flow rate or flow rate of the slurry-like liquid flowing through the pipeline, including the step of calculating the flow rate or flow rate of the slurry-like liquid flowing through the pipeline based on T 0 ) and the volume of the one section.

【0008】すなわち、本発明者等が鋭意研究を行った
結果、管路内の一区間に一対の電極を配置することによ
って、スラリー状液体、特に、汚泥などの粘稠で、固形
分(懸濁物質)を含む流体で、たとえ少流量であって
も、高い精度でその流量や流速を計測できることを知見
して、本発明の完成に至ったのである。
That is, as a result of diligent research conducted by the present inventors, by disposing a pair of electrodes in one section in a pipeline, a viscous solid content such as a slurry-like liquid, particularly sludge, is obtained. The inventor of the present invention has found out that the fluid and the flow velocity can be measured with high accuracy even if the flow rate is small even with a small flow rate.

【0009】[0009]

【発明の実施の態様】図1は、本発明の計量装置の一実
施例の概略図である。
FIG. 1 is a schematic view of one embodiment of a weighing device according to the present invention.

【0010】本発明では、スラリー状液体、例えば、下
水処理場、屎尿処理場などの下水処理プロセス、食品工
場、化学工場などの廃水処理プロセスなどから発生する
汚泥を計測対象とする。
In the present invention, the measurement target is a slurry-like liquid, for example, sludge generated from a sewage treatment process such as a sewage treatment plant and a human waste treatment plant, and a wastewater treatment process such as a food factory and a chemical factory.

【0011】図1に示したように、直立した送給管1の
一区間W(以下、単に「区間」と言う)の下端に下位電
極2と、下位電極2から上流方向に離間した位置、すな
わち、区間Wの上端に上位電極3が設けられている。
電極2、3は、送給管1の管壁に固定することも、ある
いは(管壁から離れて)送給管1内の所定位置に突き出
す/吊り下げるように設置することもできる。 下位電
極2と上位電極3は共に、演算処理装置4と電気的に連
絡されており、区間W部分の送給管1の容積と、汚泥A
と接触した下位電極2と上位電極3から送信される検知
信号(接触時間の情報)に基づいて、区間Wを流れる汚
泥の流量や流速が演算処理装置4で算出される。 な
お、送給管1の区間Wは、直同の管路上でも、あるいは
管路に接続した(管路の内径Dと異なる内径を有する)
計量槽上に設定してもよい。 また、送給管1を直立さ
せて設置する以外に、送給管1内を汚泥の液面が上昇す
る構成、例えば、送給管1を傾斜させて設置することも
できる。
As shown in FIG. 1, a lower electrode 2 is provided at a lower end of one section W (hereinafter, simply referred to as a “section”) of an upright feed pipe 1, a position which is separated from the lower electrode 2 in an upstream direction, That is, the upper electrode 3 is provided at the upper end of the section W.
The electrodes 2, 3 can be fixed to the tube wall of the feed tube 1, or can be arranged to protrude / hang from a predetermined position in the feed tube 1 (away from the tube wall). Both the lower electrode 2 and the upper electrode 3 are electrically connected to the arithmetic processing unit 4, and the volume of the feed pipe 1 in the section W and the sludge A
The flow rate and flow velocity of the sludge flowing in the section W are calculated by the arithmetic processing device 4 based on the detection signals (information of the contact time) transmitted from the lower electrode 2 and the upper electrode 3 that have come into contact. The section W of the feed pipe 1 is connected to the same pipe or connected to the pipe (having an inner diameter different from the inner diameter D of the pipe).
It may be set on the measuring tank. In addition to installing the feed pipe 1 upright, a configuration in which the liquid level of sludge rises inside the feed pipe 1, for example, the feed pipe 1 can be installed at an angle.

【0012】汚泥の流量や流速を算出するまでの手順を
説明する。 まず、自動的あるいは手動で開閉弁5を閉
止する。 開閉弁5を閉止した後もなお、開閉弁5に向
けて送給管1内を流れ/溜まり続ける汚泥Aの液面が下
位電極2に接触した時の時間(T0)が、検知信号として演
算処理装置4に送信される。 そして、ひき続き汚泥A
の液面が上昇して、汚泥Aの液面が上位電極3に接触し
た時の時間(T1)が、検知信号として演算処理装置4に送
信される。 上位電極3から演算処理装置4に検知信号
が送信され次第に、開閉弁5を開放する。 下位電極2
と上位電極3からの検知信号を受信した演算処理装置4
では、検知した時間の差(T1−T0)と、下位電極2と上位
電極3によって区画された区間W部分の管路1内の容積
から、汚泥の流量を算出する。 同時に、この流量値に
基づいて、管路内の汚泥の平均流速を求めることも可能
である。 なお、検知時間差(T1−T0)は、計測作業を迅
速に行うべく概ね1分以内に収まるよう、送給管1ある
いは計量槽(図示せず)の内径D、および/または下位
電極2と上位電極3の離間距離を決定する。
A procedure up to the calculation of the sludge flow rate and flow rate will be described. First, the on-off valve 5 is closed automatically or manually. Even after the on-off valve 5 is closed, the time (T 0 ) when the liquid level of the sludge A that continues to flow / remain in the feed pipe 1 toward the on-off valve 5 contacts the lower electrode 2 is a detection signal. It is transmitted to the arithmetic processing unit 4. And it is continued sludge A
The time (T 1 ) when the liquid level of the sludge A rises and the liquid level of the sludge A comes into contact with the upper electrode 3 is transmitted to the arithmetic processing unit 4 as a detection signal. As soon as the detection signal is transmitted from the upper electrode 3 to the arithmetic processing unit 4, the on-off valve 5 is opened. Lower electrode 2
And processing unit 4 which has received the detection signal from upper electrode 3
Then, the sludge flow rate is calculated from the detected time difference (T 1 −T 0 ) and the volume in the pipe 1 in the section W defined by the lower electrode 2 and the upper electrode 3. At the same time, it is possible to determine the average flow velocity of the sludge in the pipeline based on the flow rate value. Note that the detection time difference (T 1 −T 0 ) is set so that the measurement operation can be performed quickly within approximately one minute. And the upper electrode 3 are determined.

【0013】下位電極2と上位電極3を構成する電極と
しては、送給管1内の汚泥Aを検知できるものであれ
ば、いずれのタイプのものでも適用可能であるが、汚泥
Aの性状を考慮すれば、接液電極を用いるのが好まし
い。 また、電極の材質として、ステインレス、チタ
ン、タンタル、白金イリジウムなど、通常の電極で使用
されているものが利用できる。
As the electrodes constituting the lower electrode 2 and the upper electrode 3, any type can be used as long as the sludge A in the feed pipe 1 can be detected. Considering this, it is preferable to use a liquid contact electrode. Further, as a material of the electrode, a material used for a normal electrode such as stainless steel, titanium, tantalum, platinum iridium, or the like can be used.

【0014】本発明の一態様によれば、演算処理装置4
は開閉弁5と電気的に連絡される。すなわち、このよう
な構成を採ることで、汚泥の流量や流速が自動計測で
き、また、汚泥の流れの中断時間を最小限にできる。
具体的には、計測開始時に自動的に開閉弁5を閉止し、
そして、計測の終了時、つまり上位電極3から演算処理
装置4に検知信号が送信された時点で開閉弁5を開放す
る、という一連の動作の自動化が可能となる。
According to one aspect of the present invention, the arithmetic processing unit 4
Is electrically connected to the on-off valve 5. That is, by adopting such a configuration, the flow rate and the flow velocity of the sludge can be automatically measured, and the interruption time of the sludge flow can be minimized.
Specifically, at the start of measurement, the on-off valve 5 is automatically closed,
Then, at the end of the measurement, that is, when the detection signal is transmitted from the upper electrode 3 to the arithmetic processing device 4, the on-off valve 5 is opened, so that a series of operations can be automated.

【0015】さらに、演算処理装置4を記録計6と電気
的に連絡することで、演算処理装置4に入力された情報
/数値や、演算処理装置4で演算された情報/数値が、
記録計6に集約することができる。 記録計6に蓄積さ
れたデータを分析することで、汚泥Aの流量の変化を読
み取り、汚泥Aの供給量を、上位電極3のさらに上流側
に設けた流量調整弁(図示せず)などで加減する際の判
断指標とすることができる。
Further, by electrically communicating the arithmetic processing unit 4 with the recorder 6, information / numeric values input to the arithmetic processing unit 4 and information / numeric values calculated by the arithmetic processing unit 4 can be obtained.
It can be collected in the recorder 6. By analyzing the data accumulated in the recorder 6, a change in the flow rate of the sludge A is read, and the supply amount of the sludge A is measured by a flow control valve (not shown) provided further upstream of the upper electrode 3 or the like. It can be used as a judgment index when adjusting.

【0016】以下に、本発明をその実施例に沿って説明
するが、この実施例の開示に基づいて本発明が限定的に
解釈されるべきでないことは勿論である。
Hereinafter, the present invention will be described with reference to examples. However, it is needless to say that the present invention should not be limitedly interpreted based on the disclosure of the examples.

【0017】[0017]

【実施例】実施例1 直立した計量槽内を汚泥が鉛直方向に流れるように、計
量槽(胴体部の内径10cm)を汚泥送給管に接続した。
そして、下位電極と上位電極の間隔が127.5mmになるよ
うに、計量槽の胴体部内壁に一対の電極(先端を尖らし
たステンレス棒(φ5mm))を設置した。 次に、計量
槽下部にある開閉弁を閉止して、汚泥を計量槽内に蓄積
し、その液面を上昇せしめ、下位電極と上位電極に汚泥
の液面が接触した時間を測定した。 上位電極が汚泥の
液面を検知した時点で、開閉弁を開放した。 本実施例
の場合、下位電極で汚泥の液面を検知してから49.8秒後
に、上位電極で汚泥の液面が検知された。 この計測結
果と同区間の容積(1l)に基づいて算出したところ、
汚泥送給管での汚泥の流量は20.1cm3/secであった。
EXAMPLE 1 A measuring tank (inner diameter of the body was 10 cm) was connected to a sludge feeding pipe so that sludge flows vertically in an upright measuring tank.
Then, a pair of electrodes (a stainless steel rod with a sharpened tip (φ5 mm)) was placed on the inner wall of the body of the measuring tank so that the distance between the lower electrode and the upper electrode was 127.5 mm. Next, the on-off valve at the lower part of the measuring tank was closed, the sludge was accumulated in the measuring tank, the liquid level was raised, and the time during which the liquid level of the sludge contacted the lower electrode and the upper electrode was measured. The on-off valve was opened when the upper electrode detected the liquid level of the sludge. In the case of the present example, the sludge liquid level was detected by the upper electrode 49.8 seconds after the lower electrode detected the liquid level of the sludge. When calculated based on this measurement result and the volume (1 l) of the same section,
The sludge flow rate in the sludge feed pipe was 20.1 cm 3 / sec.

【0018】実施例2 計量槽胴体部の内径を5cm、下位電極と上位電極の間隔
が510mmとした以外は、実施例1と同一の手順・条件に
て汚泥の流速の計測を行った。 本実施例の場合、下位
電極で汚泥の液面を検知してから50.1秒後に、上位電極
で汚泥の液面が検知された。 この計測結果と同区間の
容積(1l)に基づいて算出したところ、汚泥送給管で
の汚泥の流量は20.0cm3/secであった。
Example 2 The sludge flow rate was measured in the same procedure and under the same conditions as in Example 1 except that the inner diameter of the body of the measuring tank was 5 cm and the distance between the lower electrode and the upper electrode was 510 mm. In the case of this example, the sludge liquid level was detected by the upper electrode 50.1 seconds after the lower electrode detected the liquid level of the sludge. When calculated based on this measurement result and the volume (1 l) of the same section, the flow rate of the sludge in the sludge feed pipe was 20.0 cm 3 / sec.

【0019】実施例1および2の結果から、計量槽の内
径や電極の離間距離を変化させても、実質的な影響を受
けずに、汚泥送給管を流れる汚泥の流量または流速が計
測できることが確認された。
From the results of Examples 1 and 2, even if the inner diameter of the measuring tank or the separation distance of the electrodes is changed, the flow rate or flow rate of the sludge flowing through the sludge feed pipe can be measured without being substantially affected. Was confirmed.

【0020】[0020]

【発明の効果】このように、本発明によると、所期の目
的であった、スラリー状液体の流量や流速を、その多少
にかかわらず的確に計測する手段が実現されたのであ
る。 また、送給管を通るスラリー状液体の流量や流速
を、汚泥処理系などのシステムを構成する複数の送給管
について計測を行うことで、システム上のスラリー状液
体の流量分布や滞留状況の把握までもが容易になるなど
の効果も奏する。
As described above, according to the present invention, a means for accurately measuring the flow rate and the flow rate of the slurry-like liquid, which is the intended purpose, regardless of the degree of the realization, has been realized. In addition, by measuring the flow rate and flow rate of the slurry-like liquid passing through the feed pipes for a plurality of feed pipes that constitute a system such as a sludge treatment system, the flow rate distribution and the retention status of the slurry-like liquid on the system are measured. It also has effects such as easy grasping.

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

【図1】 本発明の計測装置の一実施例の概略図であ
る。
FIG. 1 is a schematic view of an embodiment of a measuring device according to the present invention.

【符号の説明】[Explanation of symbols]

1……送給管(管路) 2……下位電極 3……上位電極 4……演算処理装置 5……開閉弁 6……記録計 A……汚泥 DESCRIPTION OF SYMBOLS 1 ... Feeding pipe (line) 2 ... Lower electrode 3 ... Upper electrode 4 ... Arithmetic processing unit 5 ... On-off valve 6 ... Recorder A ... Sludge

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 スラリー状液体の流量または流速を計測
するための装置であって、スラリー状液体が流れる管
路、スラリー状液体の流れを許容/遮断するための該管
路に接続された開閉弁、該開閉弁の上流側の管路内に該
管路の軸方向に互い離間して設けられた一対の電極、お
よび該一対の電極と連絡された演算処理装置を含む、こ
とを特徴とするスラリー状液体の流量または流速を計測
するための装置。
An apparatus for measuring a flow rate or a flow velocity of a slurry-like liquid, comprising a pipeline through which the slurry-like liquid flows, and an opening / closing connected to the pipeline for allowing / cutting off the flow of the slurry-like liquid. A valve, a pair of electrodes provided in the pipeline on the upstream side of the on-off valve so as to be separated from each other in the axial direction of the pipeline, and an arithmetic processing unit connected to the pair of electrodes. A device for measuring the flow rate or flow rate of a slurry liquid.
【請求項2】 前記演算処理装置が、前記開閉弁に連絡
している請求項1に記載の装置。
2. The apparatus according to claim 1, wherein the processing unit communicates with the on-off valve.
【請求項3】 前記演算処理装置が、演算記録および演
算結果を記録するための記録計に連絡している請求項1
または2に記載の装置。
3. The arithmetic processing unit is in communication with a recorder for recording an operation record and an operation result.
Or the apparatus according to 2.
【請求項4】 前記スラリー状液体が、汚泥である請求
項1乃至3のいずれかに記載の装置。
4. The apparatus according to claim 1, wherein the slurry-like liquid is sludge.
【請求項5】 管路内を流れるスラリー状液体の流量ま
たは流速の計測方法であって、以下の工程、すなわち; (a) 管路内の一区間の下端に位置する下位電極にてスラ
リー状液体の液面の接触を検知し、その検知信号(T0)を
演算処理装置に送信し、(b) 該管路内の一区間の上端に
位置する上位電極にてスラリー状液体の液面の接触を検
知し、その検知信号(T1)を演算処理装置に送信し、およ
び(c) 前記演算処理装置で、前記検知信号の受信時間の
差(T1−T0)と該一区間の容積に基づいて、管路内を流れ
るスラリー状液体の流量または流速を算出する、工程を
含む、ことを特徴とする管路内を流れるスラリー状液体
の流量または流速の計測方法。
5. A method for measuring a flow rate or a flow rate of a slurry-like liquid flowing in a pipeline, comprising the following steps: (a) using a lower electrode located at a lower end of a section in the pipeline to form a slurry. Detecting the contact of the liquid surface of the liquid, transmitting a detection signal (T 0 ) to the arithmetic processing unit, and (b) the liquid surface of the slurry-like liquid at the upper electrode located at the upper end of one section in the pipeline. And the detection signal (T 1 ) is transmitted to an arithmetic processing unit, and (c) the arithmetic processing unit detects a difference between the reception time of the detection signal (T 1 −T 0 ) and the one section. Calculating a flow rate or a flow rate of the slurry-like liquid flowing in the pipe line based on the volume of the slurry liquid.
【請求項6】 前記演算処理装置が、前記下位電極の下
流側の管路内に設けられた開閉弁に連絡している請求項
5に記載の方法。
6. The method according to claim 5, wherein the arithmetic processing unit communicates with an on-off valve provided in a pipeline downstream of the lower electrode.
【請求項7】 前記演算処理装置が、演算記録および演
算結果を記録するための記録計に連絡している請求項5
または6に記載の方法。
7. The arithmetic processing unit is in communication with a recorder for recording an arithmetic record and an arithmetic result.
Or the method of 6.
【請求項8】 前記スラリー状液体が、汚泥である請求
項5乃至7のいずれかに記載の方法。
8. The method according to claim 5, wherein the slurry-like liquid is sludge.
JP10178702A 1998-06-25 1998-06-25 Device and method for measuring flow rate or flow velocity of slurried liquid Withdrawn JP2000009510A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10178702A JP2000009510A (en) 1998-06-25 1998-06-25 Device and method for measuring flow rate or flow velocity of slurried liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10178702A JP2000009510A (en) 1998-06-25 1998-06-25 Device and method for measuring flow rate or flow velocity of slurried liquid

Publications (1)

Publication Number Publication Date
JP2000009510A true JP2000009510A (en) 2000-01-14

Family

ID=16053072

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10178702A Withdrawn JP2000009510A (en) 1998-06-25 1998-06-25 Device and method for measuring flow rate or flow velocity of slurried liquid

Country Status (1)

Country Link
JP (1) JP2000009510A (en)

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