JPH01316613A - Method for measuring flow rate transporting particle - Google Patents
Method for measuring flow rate transporting particleInfo
- Publication number
- JPH01316613A JPH01316613A JP14817788A JP14817788A JPH01316613A JP H01316613 A JPH01316613 A JP H01316613A JP 14817788 A JP14817788 A JP 14817788A JP 14817788 A JP14817788 A JP 14817788A JP H01316613 A JPH01316613 A JP H01316613A
- Authority
- JP
- Japan
- Prior art keywords
- differential pressure
- flow rate
- particles
- integrated value
- recorded
- 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.)
- Granted
Links
- 239000002245 particle Substances 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims description 8
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000006477 desulfuration reaction Methods 0.000 description 4
- 230000023556 desulfurization Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
Landscapes
- Measuring Volume Flow (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は粒子を気流搬送する際の輸送流量の計測方法に
関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for measuring the transport flow rate when particles are transported by air current.
[従来の技術]
乾式脱硫装置における酸化鉄脱硫剤のガス又は気流輸送
系(ライザーと呼ぶ)及び微粉炭装置等の微粉炭燃料輸
送系などにおいては、脱硫効果及び燃料流量等を把握す
る上で、気流輸送される粒子の流量を知ることか要求さ
れる。[Prior Art] In the gas or pneumatic transport system (referred to as a riser) for the iron oxide desulfurization agent in dry desulfurization equipment and the pulverized coal fuel transport system in pulverized coal equipment, etc., it is difficult to understand the desulfurization effect and fuel flow rate. , it is required to know the flow rate of air-borne particles.
[発明が解決しようとする課題]
しかし、従来においては、気流輸送される粒 ・子の流
量を直接計測するようなことはできなかった。[Problem to be solved by the invention] However, in the past, it was not possible to directly measure the flow rate of particles/particles transported by air current.
本発明は、こうした点に着目してなしたもので、気流輸
送される粒子の流量を精度良く計測する方法を提供する
ことを目的としている。The present invention has been made in view of these points, and an object of the present invention is to provide a method for accurately measuring the flow rate of particles transported by air current.
[課題を解決するための手段]
本発明は、上記技術的課題を解決しようとしたもので、
粒子を気流輸送する際、配管を介して下方から上方に向
けて輸送し、このときの前記配管における上下2点間の
差圧を検出し、更に該差圧を所要の単位時間毎に積分し
、該積分値から粒子の輸送流量を計測することを特徴と
する粒子輸送流量の計測方法、に係るものである。[Means for Solving the Problems] The present invention attempts to solve the above technical problems, and
When particles are transported by pneumatic flow, they are transported from below to above through piping, and the differential pressure between two points above and below in the piping at this time is detected, and the differential pressure is further integrated for each required unit time. , a method for measuring a particle transport flow rate, characterized in that the particle transport flow rate is measured from the integral value.
[作 用]
従って、本発明では、配管内に沿って粒子を下方から上
方に向けて気流輸送する際の上下2点間の差圧の積分値
が粒子の輸送流量に比例することから、粒子の輸送流量
を計測する。[Function] Therefore, in the present invention, since the integral value of the differential pressure between two points above and below when airflow transporting particles from the bottom to the top along the pipe is proportional to the transport flow rate of the particles, the particle to measure the transport flow rate.
[実 施 例] 以下本発明の実施例を図面を参照しつつ説明する。[Example] Embodiments of the present invention will be described below with reference to the drawings.
第1図は本発明の方法を酸化鉄脱硫剤の空気輸送系に適
用した場合の一例を示すもので、粒子lとリフトガス2
の供給により流動層3を形成する容器4によって気流輸
送される粒子を、垂直管5によって上方に導き、上部に
設けた分離器6により流体2と粒子1に分離する装置に
おいて、前記垂直管5の上下2点ASB間の差圧を計測
する差圧発信器7を設ける。Figure 1 shows an example of the case where the method of the present invention is applied to a pneumatic transport system for iron oxide desulfurization agent.
In this device, particles transported by pneumatic flow through a container 4 that forms a fluidized bed 3 by supplying the fluid are guided upward through a vertical pipe 5 and separated into fluid 2 and particles 1 by a separator 6 provided at the top. A differential pressure transmitter 7 is provided to measure the differential pressure between the upper and lower two points ASB.
更に、該差圧発信器7からの差圧信号8を記録計9に導
いてその差圧の変動を記録すると共に、前記差圧信号8
をプログラム演算器lOによって単位時間当りの積分を
行い、その積分値11を積分値記録計12に導いて記録
する。Further, the differential pressure signal 8 from the differential pressure transmitter 7 is guided to a recorder 9 to record fluctuations in the differential pressure, and the differential pressure signal 8 is
is integrated per unit time by a program calculator IO, and the integrated value 11 is led to an integral value recorder 12 and recorded.
一方、実際の輸送量と前記積分値との換算式を実験によ
って求め、その換算式が入力された流量演算装置13に
前記積分値11を人力することにより、粒子の流量を連
続的に演算し、同時に表示或いは記録させることができ
るようにしている。On the other hand, the flow rate of particles is continuously calculated by finding a conversion formula between the actual transport amount and the integral value through experiments, and manually inputting the integral value 11 into the flow rate calculation device 13 into which the conversion formula is input. , can be displayed or recorded at the same time.
前記差圧発信器7からの差圧信号8は例えば第2図のよ
うに変動し、これが記録計9に記録される。The differential pressure signal 8 from the differential pressure transmitter 7 fluctuates as shown in FIG. 2, for example, and this is recorded on the recorder 9.
又、プログラム演算器10は、前記第2図に示す差圧信
号8の斜線部分を単位時間(例えば3分)毎に積分し、
その積分値11を積分値記録計12に出力して記録する
。積分値記録計12には第3図或いは第4図に示すよう
に記録される。Further, the program calculator 10 integrates the shaded portion of the differential pressure signal 8 shown in FIG. 2 every unit time (for example, 3 minutes),
The integral value 11 is output to an integral value recorder 12 and recorded. The integral value recorder 12 records the result as shown in FIG. 3 or 4.
第3図は粒子流量が450kg/hの場合が示されてお
り、又第4図には第3図の場合と同一条件下において粒
子流量を半分(225kg/h )に減らした場合を示
している。Figure 3 shows the case where the particle flow rate is 450 kg/h, and Figure 4 shows the case where the particle flow rate is reduced to half (225 kg/h) under the same conditions as in Figure 3. There is.
上記実験を種々繰返した結果、粒子の輸送量が前記積分
値に比例していることが確認できた。As a result of various repetitions of the above experiment, it was confirmed that the amount of particles transported was proportional to the above integral value.
上記したように、差圧の積分値11が粒子の輸送量に比
例することから、輸送量の実測値と、積分値の換算式を
作り、連続的に求められる積分値11から粒子の輸送量
を連続的に推算することができる。従って、前記輸送量
の実測値と、積分値の換算式が入力された流量演算装置
13により、粒子の輸送量を連続的に演算、表示させる
ことができる。As mentioned above, since the integral value 11 of the differential pressure is proportional to the amount of particles transported, a conversion formula for the actual measured value of the transported amount and the integral value is created, and the amount of transported particles is calculated from the continuously obtained integral value 11. can be estimated continuously. Therefore, the amount of particles transported can be continuously calculated and displayed by the flow rate calculating device 13 into which the actual measured value of the transported amount and the conversion formula of the integral value are input.
又、上記において、積分のベースラインを差圧信号8の
振れに応じて調整し、運転条件の変化により逐次変化す
る差圧の振れの底(輸送量と無関係に生じる差圧)に前
記ベースラインを合わせることで、輸送量の推算精度を
向上することができる。In addition, in the above, the baseline of the integral is adjusted according to the swing of the differential pressure signal 8, and the baseline is set at the bottom of the swing of the differential pressure (differential pressure that occurs regardless of the amount of transport) that changes sequentially due to changes in operating conditions. By combining these, it is possible to improve the accuracy of estimating transportation volume.
尚、本発明は上記実施例にのみ限定されるものではなく
、気流輸送される種々の粒子の輸送流量を計測する際に
適用し得ること、その他本発明の要旨を逸脱しない範囲
内において種々変更を加え得ること、等は勿論である。It should be noted that the present invention is not limited to the above embodiments, but can be applied to measuring the transport flow rate of various particles transported by air current, and various other changes can be made without departing from the gist of the present invention. Of course, it is possible to add .
[発明の効果]
上記したように、本発明の粒子輸送流量の計測方法によ
れば、配管内に沿って粒子を下方から上方に向けて気流
輸送する際の上下2点間の差圧を検出し、該差圧の積分
値が粒子の輸送流量に比例することから、粒子の輸送流
量を精度良く計測することができる優れた効果を奏し得
る。[Effects of the Invention] As described above, according to the method for measuring the particle transport flow rate of the present invention, the differential pressure between two points above and below when particles are air-transported from the bottom to the top along the pipe is detected. However, since the integral value of the differential pressure is proportional to the particle transport flow rate, an excellent effect can be achieved in that the particle transport flow rate can be measured with high accuracy.
第1図は本発明の方法を実施する装置の一例を示す説明
図、第2図は差圧の経時変化を示す線図、第3図は差圧
の積分値の経時変化を示す線図、第4図は第3図に対し
粒子の輸送量を半減した際の差圧の積分値の経時変化を
示す線図である。
5は垂直管、7は差圧発信器、8は差圧信号、10はプ
ログラム演算器、11は積分値、12は積分値記録計、
13は流量演算装置を示す。FIG. 1 is an explanatory diagram showing an example of an apparatus for carrying out the method of the present invention, FIG. 2 is a diagram showing changes in differential pressure over time, and FIG. 3 is a diagram showing changes in integral value of differential pressure over time. FIG. 4 is a diagram showing the change over time in the integral value of the differential pressure when the transport amount of particles is halved compared to FIG. 3. FIG. 5 is a vertical tube, 7 is a differential pressure transmitter, 8 is a differential pressure signal, 10 is a program calculator, 11 is an integral value, 12 is an integral value recorder,
13 indicates a flow rate calculation device.
Claims (1)
に向けて輸送し、このときの前記配管における上下2点
間の差圧を検出し、更に該差圧を所要の単位時間毎に積
分し、該積分値から粒子の輸送流量を計測することを特
徴とする粒子輸送流量の計測方法。1) When particles are transported by pneumatic flow, they are transported from the bottom to the top through piping, and the differential pressure between the two points above and below in the piping at this time is detected, and the differential pressure is further measured every required unit time. 1. A method for measuring a particle transport flow rate, comprising integrating the particle transport flow rate and measuring the particle transport flow rate from the integrated value.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63148177A JPH0641861B2 (en) | 1988-06-17 | 1988-06-17 | Measuring method of particle flow rate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63148177A JPH0641861B2 (en) | 1988-06-17 | 1988-06-17 | Measuring method of particle flow rate |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01316613A true JPH01316613A (en) | 1989-12-21 |
JPH0641861B2 JPH0641861B2 (en) | 1994-06-01 |
Family
ID=15446973
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63148177A Expired - Lifetime JPH0641861B2 (en) | 1988-06-17 | 1988-06-17 | Measuring method of particle flow rate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0641861B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05281127A (en) * | 1992-03-30 | 1993-10-29 | Yayoi:Kk | Method of measuring viscosity of liquid |
JP2003287545A (en) * | 2002-03-28 | 2003-10-10 | Olympus Optical Co Ltd | Dispensing apparatus |
JP2005189057A (en) * | 2003-12-25 | 2005-07-14 | Nisshin Flour Milling Inc | Determinate quantity transportation method for powder and grain |
WO2008020762A1 (en) * | 2006-08-17 | 2008-02-21 | Rolls-Royce Marine As | Method for real time measurement of mass flow rate of bulk solids |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52152748A (en) * | 1976-06-14 | 1977-12-19 | Hitachi Shipbuilding Eng Co | Apparatus for detecting quantity of solid bodies transferred in fluid transportation |
JPS59108917A (en) * | 1982-12-14 | 1984-06-23 | Sumitomo Metal Ind Ltd | Method for measuring flow rate of powder body |
-
1988
- 1988-06-17 JP JP63148177A patent/JPH0641861B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52152748A (en) * | 1976-06-14 | 1977-12-19 | Hitachi Shipbuilding Eng Co | Apparatus for detecting quantity of solid bodies transferred in fluid transportation |
JPS59108917A (en) * | 1982-12-14 | 1984-06-23 | Sumitomo Metal Ind Ltd | Method for measuring flow rate of powder body |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05281127A (en) * | 1992-03-30 | 1993-10-29 | Yayoi:Kk | Method of measuring viscosity of liquid |
JP2003287545A (en) * | 2002-03-28 | 2003-10-10 | Olympus Optical Co Ltd | Dispensing apparatus |
JP2005189057A (en) * | 2003-12-25 | 2005-07-14 | Nisshin Flour Milling Inc | Determinate quantity transportation method for powder and grain |
WO2008020762A1 (en) * | 2006-08-17 | 2008-02-21 | Rolls-Royce Marine As | Method for real time measurement of mass flow rate of bulk solids |
GB2453696A (en) * | 2006-08-17 | 2009-04-15 | Rolls Royce Marine As | Method for real time measurement of mass flow rate of bulk solids |
GB2453696B (en) * | 2006-08-17 | 2012-02-15 | Rolls Royce Marine As | Method for real time measurement of mass flow rate of bulk solids |
US8423303B2 (en) | 2006-08-17 | 2013-04-16 | Rolls-Royce Marine As | Method for real time measurement of mass flow rate of bulk solids |
Also Published As
Publication number | Publication date |
---|---|
JPH0641861B2 (en) | 1994-06-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3430489A (en) | Modified turbine mass flow meter | |
US8423303B2 (en) | Method for real time measurement of mass flow rate of bulk solids | |
Gil et al. | Gas-particle flow inside cyclone diplegs with pneumatic extraction | |
US6729177B2 (en) | Method and apparatus for inspecting for airtightness failure | |
JPH01316613A (en) | Method for measuring flow rate transporting particle | |
CN207336480U (en) | Vertical pipeline flow of slurry bulk concentration measuring device | |
CN203011801U (en) | Online detection device applicable to particulate matters in high-pressure gas pipeline | |
JPS6047535B2 (en) | How to measure the flow rate of powder and granular materials | |
JPS6224123A (en) | Method and device for detecting leakage of tubular body | |
CN202599975U (en) | Portable dust-containing airflow air speed monitoring device | |
JPS6133555Y2 (en) | ||
JPS56111423A (en) | Measuring device for gas flow rate of nozzle valve or the like | |
JPS6360844B2 (en) | ||
GB1184887A (en) | Device and Method of Separating a Particulate Material from a Gas | |
JPS5760215A (en) | Method and device for measuring flow rate of solid particle | |
US3102422A (en) | Particulate material flow measuring | |
JP3396281B2 (en) | Particle flow meter | |
CN207472905U (en) | A kind of motor vehicle exhaust emission flow monitor | |
SU1721441A1 (en) | Device for measuring flow-rate of pulverulent medium | |
JPS6017727Y2 (en) | Multi-point gas detection device | |
SU1237955A1 (en) | Method and apparatus for measuring concentration of particles of dust-gas medium | |
Holton et al. | Some Notes on Dust-Sampling Equipment and Technique | |
CN105731076B9 (en) | Pneumatic conveying pipeline for gas-solid two-phase flow | |
JPH03221830A (en) | Instrument for measuring unburned component in ash | |
JPS58144726A (en) | Apparatus for monitoring leakage of pressure fluid |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |