JPH048367Y2 - - Google Patents

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Publication number
JPH048367Y2
JPH048367Y2 JP13701782U JP13701782U JPH048367Y2 JP H048367 Y2 JPH048367 Y2 JP H048367Y2 JP 13701782 U JP13701782 U JP 13701782U JP 13701782 U JP13701782 U JP 13701782U JP H048367 Y2 JPH048367 Y2 JP H048367Y2
Authority
JP
Japan
Prior art keywords
sludge
measurement chamber
sealed
pressure membrane
rod
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP13701782U
Other languages
Japanese (ja)
Other versions
JPS5941759U (en
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 filed Critical
Priority to JP13701782U priority Critical patent/JPS5941759U/en
Publication of JPS5941759U publication Critical patent/JPS5941759U/en
Application granted granted Critical
Publication of JPH048367Y2 publication Critical patent/JPH048367Y2/ja
Granted legal-status Critical Current

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  • Investigating Or Analyzing Materials By The Use Of Ultrasonic Waves (AREA)
  • Sampling And Sample Adjustment (AREA)

Description

【考案の詳細な説明】 この考案は汚泥等の濃度を測定する濃度測定装
置に関する。
[Detailed description of the invention] This invention relates to a concentration measuring device for measuring the concentration of sludge, etc.

懸濁液の中で、例えば汚水処理工程で発生する
汚泥等の場合には液中に微細気泡やガス泡を含ん
でいる。このような気泡が含まれていると超音波
で懸濁濃度を測定する場合には、この気液の界面
で大きく反射散乱されるため、実濃度より高濃度
側に誤差を生じ気泡量が多い場合は振り切つて測
定不能となる場合もある。
Among suspension liquids, for example, in the case of sludge generated in a sewage treatment process, the liquid contains fine bubbles and gas bubbles. If such bubbles are included, when measuring the suspended concentration using ultrasonic waves, they will be reflected and scattered significantly at the gas-liquid interface, resulting in an error on the higher concentration side than the actual concentration, resulting in a large amount of bubbles. In some cases, it may become impossible to measure.

一方、光線式放射線式の濃度計では気泡の分だ
け透過しやすくなるので、見かけ上の密度が薄く
なることにより、実濃度より低濃度側に誤差を生
ずることになる。
On the other hand, in a light beam type radiation type densitometer, since the air becomes more easily transmitted by the bubbles, the apparent density becomes thinner, resulting in an error in the lower concentration than the actual concentration.

従つて、従来この種の懸濁液の濃度測定におい
ては、汚泥管路から開閉弁により仕切られた加圧
測定室を設け、この室を開閉弁で締切るように
し、その締切り状態で懸濁液を一定値まで加圧し
て消泡した後、懸濁液の濃度を測定するようにし
ていた。つまり、懸濁液を加圧することにより気
体の飽和溶解度を高め液中に含まれる気泡を溶解
させ、気泡の影響を除去していた。
Therefore, conventionally, when measuring the concentration of this type of suspension, a pressurized measurement chamber is provided that is separated from the sludge pipe by an on-off valve, and this chamber is closed off with the on-off valve. After the liquid was pressurized to a certain value to defoam, the concentration of the suspension was measured. In other words, by pressurizing the suspension liquid, the saturated solubility of the gas is increased, and the air bubbles contained in the liquid are dissolved, thereby eliminating the influence of the air bubbles.

そして、従来はその加圧手段として、例えば実
開昭57−86453号公報に示されるように加圧空気
を用いていた。ところが、加圧空気を用いるため
には、予め必要空気圧力を保持するためにエアコ
ンプレツサを運転しておかなければならない。ま
た、このエアコンプレツサから空気圧を送るため
の配管が必要となり、この配管系に減圧弁、フイ
ルタ等の補機類を必要とし、その管理が面倒であ
つた。しかも、配管系、補機類にメンテナンスに
人手を要し、空気の圧縮に伴い発生する凝結水を
1日に1回程度排出しなければならない等の問題
点があつた。
Conventionally, pressurized air has been used as the pressurizing means, as shown in, for example, Japanese Utility Model Application Laid-Open No. 57-86453. However, in order to use pressurized air, the air compressor must be operated in advance to maintain the required air pressure. In addition, piping is required to send air pressure from the air compressor, and this piping system requires auxiliary equipment such as a pressure reducing valve and a filter, which is troublesome to manage. Moreover, there were other problems, such as the need for manpower to maintain the piping system and auxiliary equipment, and the condensed water generated as a result of air compression having to be discharged about once a day.

この考案は上記問題点を解決するためになされ
たものであつて、汚泥主管の一部に開閉弁を介し
て密閉測定室を設け、この密閉測定室の一部に設
けられた可動性の加圧膜にその両面に取付けた補
強板を介してロツドを設け、上記加圧膜を移動さ
せて上記密閉測定室内に閉じ込められた汚泥を加
圧するように上記ロツドに作用する機械的押圧機
構のカムとを備え、上記汚泥を加圧することによ
つて、気泡を消滅し正確な濃度測定が行える濃度
測定装置を提供することを目的とする。
This idea was made in order to solve the above problem, and a sealed measurement chamber was installed in a part of the main sludge pipe via an on-off valve, and a movable A rod is provided on the pressure membrane through reinforcing plates attached to both sides thereof, and a cam of a mechanical pressing mechanism acts on the rod to move the pressure membrane and pressurize the sludge trapped in the sealed measurement chamber. It is an object of the present invention to provide a concentration measuring device which can eliminate air bubbles and accurately measure the concentration by pressurizing the sludge.

以下、この考案の一実施例について図面を参照
して説明する。
An embodiment of this invention will be described below with reference to the drawings.

汚泥を流通させる汚泥主管1には、内面の隆起
部2に対向して一部が分岐して密閉測定室3が設
けられている。
A main sludge pipe 1 through which sludge flows is provided with a sealed measurement chamber 3 that is partially branched and opposed to a raised portion 2 on the inner surface.

上記密閉測定室3は一端の開口部4の位置に設
けられた弾性体から成る環状の弾性スペーサ5
と、他端にボルト締め等により着脱自在に固設さ
れた外箱6とを有し、この外箱6と上記弾性スペ
ーサ5との間の環状体には汚泥濃度検出子7が設
けられている。この汚泥濃度検出子7は、互いに
対向する一対の超音波の送信器および受信器とか
ら成り、その測定受信信号は記録装置(図示せ
ず)等にデータ伝送され処理される。
The hermetically sealed measurement chamber 3 has an annular elastic spacer 5 made of an elastic body provided at the opening 4 at one end.
and an outer box 6 detachably fixed to the other end by bolting or the like, and a sludge concentration detector 7 is provided in the annular body between the outer box 6 and the elastic spacer 5. There is. This sludge concentration detector 7 consists of a pair of ultrasonic transmitter and receiver that face each other, and the measurement reception signal is transmitted to a recording device (not shown) or the like and processed.

一方、上記開口部4に接した弾性スペーサ5の
内側には、その開口面に合わせ軸8によつて回動
自在に軸支された開閉弁9が設けられている。こ
の開閉弁9は実線で示すように弾性スペーサ5内
に内接および仮想線のごとく垂直位置に回動で
き、この動作によつて汚泥主管1を流れる汚泥を
サンプリングし、かつ測定室3を密閉室とする。
On the other hand, on the inside of the elastic spacer 5 in contact with the opening 4, an on-off valve 9 is provided which is rotatably supported by a shaft 8 aligned with the opening surface. This on-off valve 9 is inscribed within the elastic spacer 5 as shown by the solid line, and can be rotated to a vertical position as shown by the imaginary line. Through this operation, the sludge flowing through the sludge main pipe 1 is sampled and the measurement chamber 3 is sealed. A room.

そして、上記密閉測定室3の内部には、上記汚
泥濃度検出子7と共締めされた例えばゴム膜等の
可動性の加圧膜10が設けられ、この加圧膜10
の東部には該加圧膜の両面に取付けた補強板10
b,10cを介して、加圧手段11の駆動力を伝
達するロツド10aが取付けられている。また、
図示は省略しているが、加圧膜10には網目条に
補強線材が入れてあり、その中心部に補強板10
b,10cと密に接続されている。
A movable pressure membrane 10 such as a rubber membrane is provided inside the sealed measurement chamber 3 and is fastened together with the sludge concentration detector 7.
A reinforcing plate 10 is attached to both sides of the pressure membrane in the eastern part of the
A rod 10a is attached to transmit the driving force of the pressurizing means 11 via the rods b and 10c. Also,
Although not shown in the figure, the pressure membrane 10 has a reinforcing wire inserted in the mesh, and a reinforcing plate 10 is placed in the center of the reinforcing wire.
b and 10c.

上記加圧手段11は圧縮空気等を全く用いない
機械的な機構により構成され、この実施例では上
記ロツド10aを上下方向に摺動させるカム12
と、このカム12を回動させるモータ13とを有
し、このモータ13は上記開閉弁9、濃度検出子
7と共に制御装置(図示せず)により制御され
る。
The pressurizing means 11 is constituted by a mechanical mechanism that does not use compressed air or the like at all, and in this embodiment, a cam 12 that slides the rod 10a in the vertical direction is used.
and a motor 13 for rotating this cam 12, and this motor 13, together with the on-off valve 9 and the concentration detector 7, is controlled by a control device (not shown).

そして、密閉測定室3内を所定時間一定圧に保
つた後、濃度測定が行われる。加圧時間は調整可
能なタイマで行われ、被測定汚泥により適宜変更
できるようにするとよい。
Then, after keeping the inside of the sealed measurement chamber 3 at a constant pressure for a predetermined period of time, concentration measurement is performed. It is preferable that the pressurization time is performed using an adjustable timer and can be changed as appropriate depending on the sludge to be measured.

次に、密閉測定室3内の汚泥の加圧消泡および
サンプリング汚泥の入替動作について説明する。
Next, the pressurized defoaming of the sludge in the sealed measurement chamber 3 and the replacement operation of the sampling sludge will be described.

図において、仮想線で示すように開閉弁9を開
放状態下で、ロツド10aと係合したカム12を
回転させると、加圧膜10は実線で示す停止位置
から仮想線で示す加圧位置まで上下動し、この動
作を1〜数回繰り返すことによつて測定室3内の
汚泥を完全に入替えることができる。
In the figure, when the cam 12 engaged with the rod 10a is rotated with the on-off valve 9 in the open state as shown by the phantom line, the pressure membrane 10 moves from the stop position shown by the solid line to the pressurizing position shown by the phantom line. By moving up and down and repeating this operation one to several times, the sludge in the measurement chamber 3 can be completely replaced.

このように測定すべき汚泥の入れ変えが完了し
た後、開閉弁9を実線で示すように閉位置にし、
再びカム12を回転させ、加圧膜10を仮想線で
示す加圧位置に変位させると、測定室3は密閉さ
れているので、加圧膜10の圧縮変形により所定
の圧力値に高められ、汚泥中の気泡は溶解消滅
し、その状態で、濃度測定が行われる。測定後、
再びカム12を回転させ開閉弁9を開状態に復帰
させて測定行程を終了する。
After the replacement of the sludge to be measured is completed in this way, the on-off valve 9 is placed in the closed position as shown by the solid line.
When the cam 12 is rotated again and the pressure membrane 10 is displaced to the pressure position shown by the imaginary line, the measurement chamber 3 is sealed, so the pressure is increased to a predetermined pressure value by compressive deformation of the pressure membrane 10. The air bubbles in the sludge dissolve and disappear, and the concentration is measured in this state. After measurement,
The cam 12 is rotated again to return the on-off valve 9 to the open state, and the measurement process is completed.

従つて、この考案では上述の汚泥の加圧消泡、
入替の動作を圧縮空気等を全く使用しない機械的
な機構によつて行えるので、圧縮空気等を使用し
た場合と異なる全く煩雑な調整を不用とし、しか
もコンプレツサー等を必要としないので極めて簡
単な構造で足りる。
Therefore, in this invention, the above-mentioned pressurized defoaming of sludge,
Since the switching operation can be performed by a mechanical mechanism that does not use compressed air at all, there is no need for complicated adjustments that would be required when using compressed air, etc. Furthermore, there is no need for a compressor, etc., so the structure is extremely simple. That's enough.

なお、上記開閉弁9を特に電動弁とした場合、
加圧手段11等すべて電気系構造に統一できるの
で、より簡単な構造となる。
In addition, when the above-mentioned on-off valve 9 is especially an electric valve,
Since the pressurizing means 11 and the like can all be integrated into an electrical structure, the structure becomes simpler.

以上のように、この考案によれば、汚泥主管の
一部に開閉弁を介して密閉測定室を設け、この密
閉測定室の一部に設けられた可動性の加圧膜にそ
の両面に取付けた補強板を介してロツドを設け、
上記加圧膜を移動させて上記密閉測定室内に閉じ
込められた汚泥を加圧するように上記ロツドに作
用する機械的押圧機構のカムとを備え、上記汚泥
を加圧するように構成したので、汚泥中の気泡を
消滅し正確な濃度測定が行える。
As described above, according to this invention, a sealed measuring chamber is provided in a part of the main sludge pipe via an on-off valve, and a movable pressure membrane provided in a part of the sealed measuring chamber is attached to both sides of the sealed measuring chamber. A rod is installed through a reinforcing plate,
A cam of a mechanical pressing mechanism that acts on the rod to move the pressure membrane and pressurize the sludge trapped in the sealed measurement chamber is configured to pressurize the sludge. This eliminates air bubbles and allows accurate concentration measurements.

また、加圧膜にはその両面の一部に対向して補
強板を取付けてあるので、一点に集中して不均一
加圧力が加えられることがない。しかも、この加
圧膜にはロツドに作用する機械的押圧機構のカム
を作用させて、間接的に押圧力を伝達する構成で
あるので、カムの最大移動点以上の機械的押圧力
の伝達は起り得ない。従つて、過負荷保護装置と
して機能し、過負荷、不均等な押圧力による加圧
膜の疲労、破壊を確実に防止することができ、加
圧手段として機械的押圧機構を用いることの問題
点を解消することができたものである。
Further, since reinforcing plates are attached to the pressure membrane so as to face part of both sides thereof, uneven pressure is not concentrated on one point and is not applied. Moreover, since the pressure membrane is configured to indirectly transmit the pressing force by applying a cam of a mechanical pressing mechanism that acts on the rod, the transmission of mechanical pressing force exceeding the maximum movement point of the cam is impossible. It can't happen. Therefore, it functions as an overload protection device, and can reliably prevent fatigue and destruction of the pressurizing membrane due to overload and uneven pressing force, which solves the problem of using a mechanical pressing mechanism as a pressurizing means. It was possible to resolve this issue.

【図面の簡単な説明】[Brief explanation of the drawing]

図はこの考案の一実施例の縦断面図を示す。 1……汚泥主管、3……密閉測定室、7……汚
泥濃度検出子、9……開閉弁、10……加圧膜、
11……加圧手段。
The figure shows a longitudinal sectional view of one embodiment of this invention. 1... Sludge main pipe, 3... Sealed measurement chamber, 7... Sludge concentration detector, 9... Open/close valve, 10... Pressure membrane,
11...pressurizing means.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 汚泥主管より分岐した密閉測定室と、この密閉
測定室と上記汚泥主管との間に設けられた開閉弁
と、上記密閉測定室の一部に設けられた汚泥濃度
検出子と、上記密閉測定室の一部に設けられた可
動性の加圧膜と、この加圧膜にその両面に取付け
た補強板を介してロツドを設け、上記加圧膜を可
動させ上記密閉測定室内に閉じ込められた汚泥を
加圧するように上記ロツドに作用する機械的押圧
機構のカムとを備えた濃度測定装置。
A sealed measurement chamber branched from the sludge main pipe, an on-off valve provided between the sealed measurement chamber and the sludge main pipe, a sludge concentration detector provided in a part of the sealed measurement chamber, and the sealed measurement room. A movable pressure membrane is installed in a part of the chamber, and a rod is provided through reinforcing plates attached to both sides of the pressure membrane, and the pressure membrane is moved to remove the sludge trapped in the sealed measurement chamber. and a cam of a mechanical pressing mechanism that acts on the rod so as to pressurize the rod.
JP13701782U 1982-09-09 1982-09-09 concentration measuring device Granted JPS5941759U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13701782U JPS5941759U (en) 1982-09-09 1982-09-09 concentration measuring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13701782U JPS5941759U (en) 1982-09-09 1982-09-09 concentration measuring device

Publications (2)

Publication Number Publication Date
JPS5941759U JPS5941759U (en) 1984-03-17
JPH048367Y2 true JPH048367Y2 (en) 1992-03-03

Family

ID=30307888

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13701782U Granted JPS5941759U (en) 1982-09-09 1982-09-09 concentration measuring device

Country Status (1)

Country Link
JP (1) JPS5941759U (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0535329Y2 (en) * 1985-12-28 1993-09-08

Also Published As

Publication number Publication date
JPS5941759U (en) 1984-03-17

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