JPH09178525A - Flow rate measuring apparatus for sludge - Google Patents

Flow rate measuring apparatus for sludge

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Publication number
JPH09178525A
JPH09178525A JP7351044A JP35104495A JPH09178525A JP H09178525 A JPH09178525 A JP H09178525A JP 7351044 A JP7351044 A JP 7351044A JP 35104495 A JP35104495 A JP 35104495A JP H09178525 A JPH09178525 A JP H09178525A
Authority
JP
Japan
Prior art keywords
sludge
moisture
flow rate
water
jetting
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
JP7351044A
Other languages
Japanese (ja)
Inventor
Isao Hishikari
功 菱刈
Katsuyuki Miyauchi
克之 宮内
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.)
Chino Corp
Original Assignee
Chino 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 Chino Corp filed Critical Chino Corp
Priority to JP7351044A priority Critical patent/JPH09178525A/en
Publication of JPH09178525A publication Critical patent/JPH09178525A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To measure the flow rate of sludge effectively through a simple structure by jetting a specified quantity of water into an enclosed pipe for feeding sludge, measuring the moisture of sludge, and then operating the flow rate, based on the difference between the water jetting time and moisture measuring time and the distance between the water jetting point and moisture measuring point. SOLUTION: The switching means 22 for a jetting means 2 is opened, based on a signal e0 received from an operating means 5 at an appropriate timing t0 to jet a specified quantity of water W through a nozzle 22 to sludge B flowing through an enclosed pipe 1. Consequently, the sludge B containing water W flows through the pipe 1 at a specified current velocity. A moisture measuring means 30 detects the moisture through a photoconductor 31 at a moisture measuring tine t1 and delivers a measurement signal e1 to an operating means 5 if the detected value exceeds a specific threshold value. The operating means 5 operates the flow rate F of sludge B, based on the difference T1 between the water jetting time t0 of water jetting means 2 and the moisture measuring time t1 and the distance L1 between the water jetting means 2 and the measuring point (photoconductor 31).

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】この発明は、下水処理場等に
おける汚泥の流量を測定する装置に関するものである。
TECHNICAL FIELD The present invention relates to an apparatus for measuring the flow rate of sludge in a sewage treatment plant or the like.

【0002】[0002]

【従来の技術】例えば下水処理場では、下水を沈澱、濃
縮、脱水等の処理を行い、脱水汚泥ケーキとし、密閉配
管、スクリューコンベア、ベルトコンベア等で輸送し、
乾燥、焼却等の処理を行う。
2. Description of the Related Art For example, in a sewage treatment plant, sewage is subjected to treatments such as precipitation, concentration, and dehydration to obtain dehydrated sludge cake, which is transported by a closed pipe, a screw conveyor, a belt conveyor, etc.
Perform processing such as drying and incineration.

【0003】そして、汚泥を送る流量を測定し、乾燥、
焼却等の制御や管理に用いることが望まれている。
Then, the flow rate of sludge is measured and dried,
It is desired to use it for control and management such as incineration.

【0004】[0004]

【発明が解決しようとする課題】例えば、電磁流量計で
汚泥の流量を測定することが試みらているが、密閉配管
の内部の酸化膜、表面磨耗等の影響で、安定した正確な
測定は困難であった。
For example, although it has been attempted to measure the flow rate of sludge with an electromagnetic flow meter, stable and accurate measurement is not possible due to the influence of an oxide film inside the closed pipe, surface abrasion, etc. It was difficult.

【0005】この発明の目的は、以上の点に鑑み、簡単
な構成で、効果的に汚泥流量を測定できるようにした汚
泥水分測定装置を提供することである。
In view of the above points, an object of the present invention is to provide a sludge moisture measuring device having a simple structure and capable of effectively measuring the sludge flow rate.

【0006】[0006]

【課題を解決するための手段】この発明は、汚泥が送ら
れる密閉配管の外部から内部へ所定量の水を噴出する噴
出手段と、この噴出手段から所定距離に設けられ密閉配
管の外部から内部へ挿入された光導体を介し光を投受光
して汚泥の水分を測定する少なくとも1個の水分測定手
段と、前記噴出手段の水分噴出時刻や水分測定手段の水
分測定時刻等の時間差及び両者の距離に基いて汚泥の流
量を演算する演算手段とを備えるようにした汚泥流量測
定装置である。
According to the present invention, there is provided a jetting means for jetting a predetermined amount of water from the outside to the inside of a sealed pipe to which sludge is sent, and an outside to the inside of the sealed pipe provided at a predetermined distance from the jetting means. At least one moisture measuring means for projecting and receiving light through a light guide inserted into the sludge to measure the moisture content of the sludge, and the time difference between the moisture jetting time of the jetting means and the moisture measuring time of the moisture measuring means and the like. The sludge flow rate measuring device is provided with a calculating means for calculating the flow rate of sludge based on the distance.

【0007】[0007]

【発明の実施の形態】図1は、この発明の一実施例を示
す構成説明図である。図1において、1は汚泥Bが送ら
れる密閉配管で、この密閉配管1の所要箇所に内部へ水
Wを噴出することができる噴出手段2が設けられてい
る。この噴出手段2は、密閉配管1の外部から内部へ挿
入設置され密閉配管1の外部から内部へ所定量の水Wを
噴出するノズル21、及び水源から供給された水Wをノ
ズル21から噴出制御するための電磁弁等の開閉手段2
2等から構成されている。又、噴出手段2から所定距離
L1離れた位置の密閉配管1の外部から内部へ挿入され
た光導体31を介し光を投受光して汚泥の水分を測定す
る第1の水分測定手段30、及び第1の水分測定手段3
1から所定距離L2離れた位置の密閉配管1の外部から
内部へ挿入された光導体41を介し光を投受光して汚泥
の水分を測定する第2の水分測定手段40が設けられて
いる。そして、噴出手段2の水分噴出のタイミングを制
御するとともに、この水分噴出時刻や水分測定手段3
0、40の水分測定時刻等の時間差及び両者の距離L
1、L2等に基いて汚泥の流量を演算するパソコン、C
PU等の演算手段5が設けられている。なお、この光導
体31、41は光フアイバ等とされこれ介し水分に吸収
される波長の光と水分に吸収されない波長の光を投受光
してその比率から汚泥の水分を測定するいわゆるファイ
バ式水分計のような測定手段30、40とされている。
又、光導体21の先端部の端面の測定面はの投光軸に対
し傾けて形成され、先端の測定面は汚泥Bが常時近接し
て通過して擦るため研磨され平滑面が良好に保たれ、し
かも、測定面における正反射を防止して安定した測定を
可能としている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is an explanatory diagram showing the configuration of an embodiment of the present invention. In FIG. 1, reference numeral 1 is a closed pipe through which the sludge B is sent, and a jetting means 2 capable of jetting water W into the inside is provided at a required position of the closed pipe 1. The jetting means 2 controls the jetting of the nozzle 21 that is inserted and installed from the outside of the closed pipe 1 to jet a predetermined amount of water W from the outside of the closed pipe 1 and the water W supplied from a water source from the nozzle 21. Opening / closing means 2 such as a solenoid valve for operating
2 and so on. Also, a first moisture measuring means 30 for measuring the moisture content of sludge by projecting and receiving light through an optical conductor 31 inserted from the outside to the inside of the closed pipe 1 at a position separated by a predetermined distance L1 from the jetting means 2. First moisture measuring means 3
There is provided a second water content measuring means 40 for measuring the water content of the sludge by projecting and receiving light through an optical conductor 41 which is inserted from the outside to the inside of the closed pipe 1 at a position separated by a predetermined distance L2 from 1. Then, while controlling the timing of water ejection of the water ejection means 2, the water ejection time and the water content measuring means 3 are controlled.
The time difference between the moisture measurement times of 0 and 40 and the distance L between them
PC that calculates the flow rate of sludge based on 1, L2, etc., C
A calculation means 5 such as a PU is provided. The light guides 31 and 41 are optical fibers or the like, through which light of a wavelength absorbed by water and light of a wavelength not absorbed by water are projected and received to measure the water content of the sludge based on the ratio. The measuring means 30, 40 such as a meter is used.
Further, the measurement surface of the end surface of the tip of the light guide 21 is formed to be inclined with respect to the light projection axis, and the measurement surface at the tip is polished because sludge B always passes in close proximity and is rubbed to maintain a good smooth surface. Moreover, it prevents the specular reflection on the measurement surface and enables stable measurement.

【0008】次に、図2を参照して、動作を説明する。
適当なタイミングの時刻t0で、演算手段5の信号e0
により噴出手段2の開閉手段22を駆動し所定量の水W
をノズル21から密閉配管1の流れる汚泥Bに噴出す
る。すると、この多量の水分を含んだ汚泥Bは所定速度
で流れ、時刻t1で第1の光導体31を介し水分測定手
段30で通常より多い水分値を検出し、これが所定のし
きい値以上のとき測定信号e1を発生し、この信号が演
算手段5に出力される。
Next, the operation will be described with reference to FIG.
At time t0 of appropriate timing, the signal e0 of the calculation means 5
The opening / closing means 22 of the ejection means 2 is driven by the
From the nozzle 21 to the sludge B flowing through the closed pipe 1. Then, the sludge B containing a large amount of water flows at a predetermined speed, and at time t1, the water content measuring means 30 detects a water value higher than usual via the first light guide 31, and this is higher than a predetermined threshold value. At this time, a measurement signal e1 is generated, and this signal is output to the calculation means 5.

【0009】ここで、演算手段5は、噴出手段2の水分
噴出時刻t0と水分測定手段30の水分測定時刻t1の
時間差T1及び両者の距離L1に基いて汚泥Bの流量F
を概略、次式で演算する。
Here, the calculation means 5 calculates the flow rate F of the sludge B based on the time difference T1 between the water ejection time t0 of the ejection means 2 and the water measurement time t1 of the water measurement means 30 and the distance L1 between them.
Is roughly calculated by the following equation.

【0010】 F=S・L1/T1 (1) ここで、Sは、密閉配管1の断面積である。又、水分測
定手段30の出力信号e2を微分した微分信号e3を用
い、適当なしきい値と比較し、より精度良く時刻の検出
を行って流量測定してもよい。例えば、正の微分信号と
負の微分信号の発生時刻の平均を用いて、時刻t1の検
出を行って流量測定を行ってもよい。
F = S · L1 / T1 (1) where S is the cross-sectional area of the closed pipe 1. Alternatively, the differential signal e3 obtained by differentiating the output signal e2 of the water content measuring means 30 may be used to compare with an appropriate threshold value, and the time may be detected more accurately to measure the flow rate. For example, the average of the generation times of the positive differential signal and the negative differential signal may be used to detect the time t1 and measure the flow rate.

【0011】更に、多量の水分を含んだ汚泥Bは所定速
度で流れ、時刻t2で第2の光導体41を介し水分測定
手段40で通常より多い水分値を検出し、これが所定の
しきい値以上のとき測定信号e2を発生し、この信号が
演算手段5に出力される。
Further, the sludge B containing a large amount of water flows at a predetermined speed, and at time t2, the water content measuring means 40 detects a higher water content than usual through the second light guide 41, and this is a predetermined threshold value. In the above case, the measurement signal e2 is generated, and this signal is output to the calculation means 5.

【0012】ここで、演算手段5は、第1、第2の水分
測定手段30,40の水分測定時刻t1,t2の時間差
T2及び両者の距離L2に基いて汚泥Bの流量Fを概
略、次式で演算するようにしてもよい。
Here, the calculating means 5 roughly calculates the flow rate F of the sludge B based on the time difference T2 between the moisture measuring times t1 and t2 of the first and second moisture measuring means 30 and 40 and the distance L2 between them. You may make it calculate by a formula.

【0013】 F=S・L2/T2 (2) この場合、演算手段5は、噴出手段1の噴出時刻を知ら
なくても演算できる。又、水分測定手段40の出力信号
e2を微分した微分信号e3を用い、適当なしきい値と
比較し、同様により精度良く時刻の検出を行ってもよ
い。例えば、正の微分信号と負の微分信号の発生時刻の
平均を用いて、時刻t1,t2の検出を行って流量測定
を行ってもよい。
F = S · L2 / T2 (2) In this case, the calculation means 5 can perform the calculation without knowing the ejection time of the ejection means 1. Further, the differential signal e3 obtained by differentiating the output signal e2 of the water content measuring means 40 may be used and compared with an appropriate threshold value, and the time may be detected more accurately in the same manner. For example, the flow rate may be measured by detecting the times t1 and t2 by using the average of the generation times of the positive differential signal and the negative differential signal.

【0014】なお、上記噴出手段2の水Wの噴出周期、
のタイミングは、必要に応じて適宜定め、噴出動作をさ
せればよい。
The jetting cycle of the water W of the jetting means 2,
The timing may be appropriately determined as necessary and the ejection operation may be performed.

【0015】ところで、水分測定手段30,40は、複
数の波長の光に基き汚泥Bの水分率M及び有機物含有率
Nを求めるようにしても良い。例えば、出願人が、特開
平7−294426号で提案しているように、水分の吸
収される第1の波長の光の成分の信号sと、有機物に吸
収される第2の波長の光の成分の信号r1と、水分にも
有機物にも吸収されない第3の波長の光による成分の信
号r2に基き、互いに補正して、水分率M、及び有機物
含有率Nが次式で求まる。
By the way, the water content measuring means 30 and 40 may obtain the water content M and the organic matter content N of the sludge B based on the light of a plurality of wavelengths. For example, as proposed by the applicant in Japanese Unexamined Patent Publication No. 7-294426, the signal s of the light component of the first wavelength that absorbs water and the light of the second wavelength that is absorbed by the organic substance Based on the signal r1 of the component and the signal r2 of the component due to the light of the third wavelength which is not absorbed by moisture or organic matter, the moisture content M and the organic matter content rate N are calculated by the following equations by mutual correction.

【0016】 M=F(x)・G(y) (3) N=H(y)・I(x) (4) ここで、F、G、H、Iは、あらかじめ実験で求めた所
定の関数で、x=s/r2,y=r1/r2である。そ
して、汚泥量Zは流量Fから求まり、水分量Wは汚泥の
量Z=W+D(Dは絶乾重量)に水分率Mを乗じ次式と
なる。
M = F (x) · G (y) (3) N = H (y) · I (x) (4) Here, F, G, H, and I are predetermined values obtained by experiments in advance. In the function, x = s / r2 and y = r1 / r2. Then, the sludge amount Z is obtained from the flow rate F, and the water amount W is given by the following formula by multiplying the sludge amount Z = W + D (D is an absolute dry weight) by the water content M.

【0017】 W=Z・M (5) 絶乾重量Dは、有機物含有量Vと無機物含有量dの和で
あることから有機物含有率Nは次式となる。
W = Z · M (5) Since the absolute dry weight D is the sum of the organic matter content V and the inorganic matter content d, the organic matter content rate N is as follows.

【0018】 N=V/(V+d)=V/D (6) そこで、有機物含有率Vは、 V=N・D (7) で求めることができる。なお、D=Z−W=Z(1−
M)で既知である。このようにして、流量の他に、水分
量、有機物含有量の様々な物理量を求めることができ、
汚泥処理過程の大幅な自動化が可能となる。
N = V / (V + d) = V / D (6) Then, the organic matter content rate V can be calculated by V = N · D (7). Note that D = Z−W = Z (1−
M). In this way, in addition to the flow rate, various physical quantities such as water content and organic matter content can be obtained,
It is possible to greatly automate the sludge treatment process.

【0019】[0019]

【発明の効果】以上述べたように、この発明は、汚泥が
送られる密閉配管の外部から内部へ所定量の水を噴出す
る噴出手段と、この噴出手段から所定距離に設けられ密
閉配管の外部から内部へ挿入された光導体を介し光を投
受光して汚泥の水分を測定する少なくとも1個の水分測
定手段と、前記噴出手段の水分噴出時刻や水分測定手段
の水分測定時刻等の時間差及び両者の距離に基いて汚泥
の流量を演算する演算手段とを備えるようにした汚泥流
量測定装置である。つまり、流れる汚泥内に水分を噴出
し、離れた位置で水分を測定することで容易に汚泥流量
の測定ができ、更に流量の他に、水分測定手段で、水分
量、有機物含有量の様々な物理量を求めることができ、
汚泥処理過程の大幅な自動化、総合的な管理が十分に可
能となる。又、汚泥測定の際、水分測定信号の微分信号
を用いることで、より精度よく時刻が分り、高精度流量
測定が可能となる。又、水分測定手段を複数箇所に設け
ることで、水分の噴出手段の噴出時刻が分らなくても流
量測定でき、更に多数の水分測定手段を必要箇所の設け
ることで、流量分布等を知ることができ、総合的な汚泥
処理がいっそう容易に可能となる。
As described above, according to the present invention, the jetting means for jetting a predetermined amount of water from the outside to the inside of the closed pipe to which sludge is sent, and the outside of the closed pipe provided at a predetermined distance from the jetting means. From at least one moisture measuring means for measuring the moisture content of the sludge by projecting and receiving light through a light guide inserted inside, and a time difference between the moisture ejection time of the ejection means and the moisture measurement time of the moisture measurement means, and the like. The sludge flow rate measuring device is provided with a calculation means for calculating the flow rate of sludge based on the distance between the two. That is, it is possible to easily measure the sludge flow rate by ejecting water into the flowing sludge and measuring the water at a remote position. Physical quantity can be calculated,
The sludge treatment process can be fully automated and comprehensively managed. Further, by using the differential signal of the water content measurement signal when measuring the sludge, the time can be known with higher accuracy, and high-accuracy flow rate measurement becomes possible. Further, by providing the moisture measuring means at a plurality of locations, the flow rate can be measured without knowing the ejection time of the moisture ejecting means, and by providing a large number of moisture measuring means at the required locations, the flow rate distribution and the like can be known. Yes, comprehensive sludge treatment becomes even easier.

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

【図1】この発明の一実施例を示す構成説明図である。FIG. 1 is a configuration explanatory view showing one embodiment of the present invention.

【図2】この発明の一実施例を示す動作説明図である。FIG. 2 is an operation explanatory diagram showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 密閉配管 2、噴出手段 31、41 光導体 30、40 水分測定手段 5 演算手段 DESCRIPTION OF SYMBOLS 1 Sealed pipe 2, Jetting means 31, 41 Optical conductor 30, 40 Moisture measuring means 5 Computing means

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】汚泥が送られる密閉配管の外部から内部へ
所定量の水を噴出する噴出手段と、この噴出手段から所
定距離に設けられ密閉配管の外部から内部へ挿入された
光導体を介し光を投受光して汚泥の水分を測定する水分
測定手段と、前記噴出手段の水分噴出時刻と水分測定手
段の水分測定時刻との時間差及び両者の距離に基いて汚
泥の流量を演算する演算手段とを備えたことを特徴とす
る汚泥流量測定装置。
1. A spout means for spouting a predetermined amount of water from the outside to the inside of a sealed pipe to which sludge is sent, and a light conductor provided at a predetermined distance from the jet means and inserted from the outside to the inside of the sealed pipe. Moisture measuring means for projecting and receiving light to measure the moisture content of sludge, and computing means for computing the flow rate of sludge based on the time difference between the moisture ejection time of the ejection means and the moisture measurement time of the moisture measurement means and the distance between the two. And a sludge flow rate measuring device.
【請求項2】汚泥が送られる密閉配管の外部から内部へ
所定量の水を噴出する噴出手段と、この噴出手段から夫
々所定距離に設けられ密閉配管の外部から内部へ挿入さ
れた光導体を介し光を投受光して汚泥の水分を測定する
互いに離れて設けられた複数の水分測定手段と、これら
水分測定手段の水分測定時刻の時間差及び両者の距離に
基いて汚泥の流量を演算する演算手段とを備えたことを
特徴とする汚泥流量測定装置。
2. A jetting means for jetting a predetermined amount of water from the outside to the inside of a sealed pipe to which sludge is sent, and a light guide which is provided at a predetermined distance from the jetting means and is inserted from the outside to the inside of the sealed pipe. A plurality of moisture measuring means provided separately from each other for projecting and receiving light through to measure the moisture content of the sludge, and a computation for calculating the flow rate of the sludge based on the time difference between the moisture measurement times of these moisture measuring means and the distance between the two. And a means for measuring sludge flow rate.
【請求項3】前記演算手段は、前記水分測定手段の出力
信号を微分した微分信号を用いて流量を演算をすること
を特徴とする請求項1又は請求項2記載の汚泥流量測定
装置。
3. The sludge flow rate measuring device according to claim 1, wherein the calculating means calculates the flow rate by using a differential signal obtained by differentiating the output signal of the moisture measuring means.
【請求項4】前記水分測定手段は、複数の波長の光に基
き汚泥の水分率及び有機物含有率を求めることを特徴と
する請求項1から請求項3いずれかに記載の汚泥流量測
定装置。
4. The sludge flow rate measuring device according to claim 1, wherein the water content measuring means obtains the water content and the organic matter content of the sludge based on light of a plurality of wavelengths.
JP7351044A 1995-12-25 1995-12-25 Flow rate measuring apparatus for sludge Pending JPH09178525A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7351044A JPH09178525A (en) 1995-12-25 1995-12-25 Flow rate measuring apparatus for sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7351044A JPH09178525A (en) 1995-12-25 1995-12-25 Flow rate measuring apparatus for sludge

Publications (1)

Publication Number Publication Date
JPH09178525A true JPH09178525A (en) 1997-07-11

Family

ID=18414664

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7351044A Pending JPH09178525A (en) 1995-12-25 1995-12-25 Flow rate measuring apparatus for sludge

Country Status (1)

Country Link
JP (1) JPH09178525A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005338022A (en) * 2004-05-31 2005-12-08 Jasco Corp Supercritical fluid hydrometry apparatus and supercritical fluid apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005338022A (en) * 2004-05-31 2005-12-08 Jasco Corp Supercritical fluid hydrometry apparatus and supercritical fluid apparatus

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