JPH07158837A - Powder transporting apparatus - Google Patents

Powder transporting apparatus

Info

Publication number
JPH07158837A
JPH07158837A JP30795493A JP30795493A JPH07158837A JP H07158837 A JPH07158837 A JP H07158837A JP 30795493 A JP30795493 A JP 30795493A JP 30795493 A JP30795493 A JP 30795493A JP H07158837 A JPH07158837 A JP H07158837A
Authority
JP
Japan
Prior art keywords
powder
differential pressure
gas
clogging
alarm
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Withdrawn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
JP30795493A
Other languages
Japanese (ja)
Inventor
Masaaki Kinoshita
正昭 木下
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP30795493A priority Critical patent/JPH07158837A/en
Publication of JPH07158837A publication Critical patent/JPH07158837A/en
Withdrawn legal-status Critical Current

Links

Abstract

PURPOSE:To securely detect in an early time clogging of powder by measuring a difference between pressures at two points of a transport tube serving to gas-transport the powder, and actuating an alarming oscillator when variations of the measured difference pressure exceed a set value. CONSTITUTION:Powder in a powder hopper 1 is supplied to an ejector 4 by a rotary valve 2, and is entrained with gas introduced from a gas carrying piping 3 and is transported to a container 7 after passage through a transport tube 5. In this instance, a pressure difference detector 6 for detecting a pressure difference between two points of the transport tube 5 is disposed on the transport tube 5 and a detected output is inputted into a computer 9. When the variations of the difference pressure at the two points A, B exceed a set value in the computer 9, alarming is issued from an alarming generating 10 to open a flow rate adjusting valve 11 for prevention of clogging with the aid of increased carrying gas. When there is not yet eliminated the clogging, an interruption valve 12 is them closed and a purging gas interruption valve 14 is opened to introduce high pressure purging gas for elimination of the clogging of powder.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、微粉炭など粉体の気体
輸送に適用される粉体輸送装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a powder transportation device applied to gas transportation of powder such as pulverized coal.

【0002】[0002]

【従来の技術】図3は微粉炭など粉体の気体輸送に使用
されている従来の粉体輸送装置の説明図である。同図
(a)において、粉体用ホッパ1内に貯蔵されている粉
体は、ロータリバルブ2によりエゼクタ4に供給されて
搬送ガスの配管3から導入されるガスと混合され、輸送
管5を通って容器7内へ輸送される。輸送管5には途中
の2点A,B間の差圧を検出するために差圧計6が検出
用配管8を介して配設されており、この2点A,B間の
差圧が設定値よりも過大になった場合には搬送管5途中
の2点A,B間で粉体の詰まりが発生したものと判断さ
れて警報発信器9から警報が発せられるようになってい
る。
2. Description of the Related Art FIG. 3 is an explanatory view of a conventional powder transportation device used for gas transportation of powder such as pulverized coal. In FIG. 1A, the powder stored in the powder hopper 1 is mixed with the gas supplied to the ejector 4 by the rotary valve 2 and introduced from the pipe 3 for the carrier gas, and the powder is fed through the transport pipe 5. It is transported therethrough into the container 7. A differential pressure gauge 6 is arranged in the transport pipe 5 to detect a differential pressure between two points A and B on the way, and a differential pressure gauge between the two points A and B is set via a detection pipe 8. When the value becomes larger than the value, it is determined that the clogging of the powder has occurred between the two points A and B in the middle of the conveying pipe 5, and the alarm transmitter 9 gives an alarm.

【0003】[0003]

【発明が解決しようとする課題】上記のように、従来の
粉体輸送装置においては輸送管5途中の2点A,B間で
粉体の詰まりが発生すると差圧計6により詰まりの検出
が可能になっているが、仮に他の2点C,A間、或いは
2点B,D間で詰まりが発生した場合には、差圧計6に
よって検出される差圧が設定値よりも過大にならないた
めに検出されない。仮に、点Aがエゼクタ4に隣接して
設置されているとともに点Bが容器7に隣接していれ
ば、輸送管5の何処で詰まりが発生しても原理的にはそ
の検出が可能である。しかしながら、このような粉体輸
送装置においては実際には粉体及び搬送ガスの流量が常
に一定ではなく、粉体輸送装置の負荷変動とともに変化
するのが一般的であり、これに伴って差圧も大きく変動
するために詰まりを検出するための差圧の設定値を十分
に高い値に設定する必要がある。即ち、同図(b)は粉
体の供給量、搬送ガスの流量が変化したときの輸送管5
における差圧及び詰まりを検出するための差圧の設定値
を示しており、粉体の供給量や搬送ガスなどの流量が少
ない場合には、通常の運転中における差圧と設定値との
差が大きすぎるために輸送管5における粉体の詰まりを
早期に検出することができない。
As described above, in the conventional powder transport device, when the powder is clogged between two points A and B in the middle of the transport pipe 5, the clogging can be detected by the differential pressure gauge 6. However, if a blockage occurs between the other two points C and A, or between the two points B and D, the differential pressure detected by the differential pressure gauge 6 does not become larger than the set value. Not detected by. If the point A is installed adjacent to the ejector 4 and the point B is adjacent to the container 7, it is possible in principle to detect where the transport pipe 5 is clogged. . However, in such a powder transportation device, the flow rates of the powder and the carrier gas are not always constant in practice, and generally change with the load fluctuation of the powder transportation device. Since it also fluctuates greatly, it is necessary to set the set value of the differential pressure for detecting clogging to a sufficiently high value. That is, FIG. 3B shows the transport pipe 5 when the powder supply amount and the carrier gas flow rate are changed.
The differential pressure and the set value of the differential pressure for detecting clogging are shown.When the flow rate of powder supply amount or carrier gas is small, the difference between the differential pressure and the set value during normal operation is shown. Is too large, the clogging of the powder in the transport pipe 5 cannot be detected early.

【0004】[0004]

【課題を解決するための手段】本発明に係る粉体輸送装
置は上記課題の解決を目的にしており、粉体を気体輸送
する輸送管における2点間の差圧を計測する差圧計と、
該差圧計により計測される差圧の変動幅が設定値以上に
なると警報を発信する警報発信器とを備えた構成を特徴
とする。
A powder transporting device according to the present invention is intended to solve the above problems, and a differential pressure gauge for measuring a differential pressure between two points in a transport pipe for transporting powder by gas.
An alarm transmitter that issues an alarm when the fluctuation range of the differential pressure measured by the differential pressure gauge becomes equal to or greater than a set value.

【0005】また、本発明に係る粉体輸送装置は、粉体
を気体輸送する輸送管における2点間の差圧を計測する
差圧計と、該差圧計により計測される差圧の変動幅と差
圧の平均値との比が設定値以上になると警報を発信する
警報発信器とを備えた構成を特徴とする。
Further, the powder transport apparatus according to the present invention comprises a differential pressure gauge for measuring a differential pressure between two points in a transport pipe for transporting powder by gas, and a fluctuation range of the differential pressure measured by the differential pressure gauge. A feature is a configuration including an alarm transmitter that issues an alarm when the ratio of the differential pressure to the average value is equal to or greater than a set value.

【0006】また、本発明に係る粉体輸送装置は、粉体
を気体輸送する輸送管における2点間の差圧を計測する
差圧計と、該差圧計により計測される差圧の変動幅また
は差圧の変動幅と差圧の平均値との比が設定値以上にな
ると警報を発信する警報発信器と、上記警報の発信とと
もに粉体を気体輸送する搬送ガスの流量を自動的に増
加、或いは粉体の供給量を自動的に減少させる手段とを
備えた構成を特徴とする。
Further, the powder transport apparatus according to the present invention is a differential pressure gauge for measuring a differential pressure between two points in a transport pipe for transporting powder by gas, and a fluctuation range of the differential pressure measured by the differential pressure gauge or An alarm transmitter that issues an alarm when the ratio between the fluctuation range of the differential pressure and the average value of the differential pressure is greater than or equal to the set value, and the flow rate of the carrier gas that conveys the powder in gas is automatically increased when the above alarm is issued. Alternatively, it is characterized by a configuration including means for automatically reducing the amount of powder supplied.

【0007】また、本発明に係る粉体輸送装置は、粉体
を気体輸送する輸送管における2点間の差圧を計測する
差圧計と、該差圧計により計測される差圧の変動幅また
は差圧の変動幅と差圧の平均値との比が設定値以上にな
ると警報を発信する警報発信器と、上記警報の発信とと
もに粉体を気体輸送する搬送ガスに代えてパージ用ガス
を上記輸送管内へ導入する手段とを備えた構成を特徴と
する。
Further, the powder transporting apparatus according to the present invention comprises a differential pressure gauge for measuring the differential pressure between two points in a transport pipe for transporting powder by gas, and a fluctuation range of the differential pressure measured by the differential pressure gauge or When the ratio between the fluctuation range of the differential pressure and the average value of the differential pressure becomes equal to or greater than the set value, an alarm transmitter that issues an alarm, and when the alarm is issued, the purging gas is used instead of the carrier gas that gas-transports the powder. And a means for introducing it into the transportation pipe.

【0008】[0008]

【作用】即ち、本発明に係る粉体輸送装置においては、
粉体を気体輸送する輸送管における2点間の差圧が差圧
計により計測され計測される差圧の変動幅が設定値以上
になると警報発信器が警報を発信するようになってお
り、輸送管に粉体の詰まりがない場合は輸送管における
2点間の差圧の変動は小さいが輸送管の底部に粉体が滞
留し始めると粉体を気体輸送する搬送ガスの流速が上昇
して滞留し始めた粉体が浮遊して搬送されることにより
差圧の変動幅が大きくなる。輸送管に粉体の詰まりが発
生する場合にはこのような滞留と浮遊による搬送とを繰
り返しながら差圧の変動幅が次第に大きくなる。従っ
て、差圧の変動幅を監視して警報を発信することにより
輸送管における負荷変動が大きい場合でも粉体の詰まり
の検出を早期に行うことができる。
That is, in the powder transport apparatus according to the present invention,
The differential pressure between two points in a transport pipe that transports powder by gas is measured by a differential pressure gauge, and when the fluctuation range of the measured differential pressure exceeds a set value, an alarm transmitter will issue an alarm. When the powder is not clogged in the pipe, the fluctuation of the differential pressure between the two points in the transport pipe is small, but when the powder starts to stay at the bottom of the transport pipe, the flow velocity of the carrier gas that transports the powder by gas increases. The fluctuation range of the differential pressure becomes large because the powder that has started to stay is suspended and conveyed. When the transport pipe is clogged with powder, the fluctuation range of the differential pressure gradually increases while repeating such retention and transportation by floating. Therefore, by monitoring the fluctuation range of the differential pressure and issuing an alarm, the clogging of the powder can be detected early even when the load fluctuation in the transport pipe is large.

【0009】また、本発明に係る粉体輸送装置において
は、粉体を気体輸送する輸送管における2点間の差圧が
差圧計により計測され計測される差圧の変動幅と差圧の
平均値との比が設定値以上になると警報発信器が警報を
発信するようになっており、差圧の変動と差圧の平均値
との比を監視して警報を発信することにより輸送管にお
ける負荷変動が大きい場合でも粉体の詰まりの検出を早
期に行うことができる。
Further, in the powder transport apparatus according to the present invention, the differential pressure between two points in the transport tube for transporting the powder gas is measured by the differential pressure gauge, and the fluctuation range of the differential pressure and the average of the differential pressure are measured. When the ratio with the value exceeds the set value, the alarm transmitter issues an alarm.By monitoring the ratio between the fluctuation of the differential pressure and the average value of the differential pressure and issuing the alarm, Even if the load fluctuation is large, the clogging of the powder can be detected early.

【0010】また、本発明に係る粉体輸送装置において
は、粉体を気体輸送する輸送管における2点間の差圧が
差圧計により計測され計測される差圧の変動幅または差
圧の変動幅と差圧の平均値との比が設定値以上になると
警報発信器が警報を発信するとともに粉体を気体輸送す
る搬送ガスの流量を自動的に増加、或いは粉体の供給量
を自動的に減少させるようになっており、差圧の変動幅
または差圧の変動幅と差圧の平均値との比を監視して警
報を発信することにより輸送管における負荷変動が大き
い場合でも粉体の詰まりの検出を早期に行うことがで
き、また搬送ガスの流量を増加、或いは粉体の供給量を
減少させることにより自動的に詰まりの解消が可能にな
る。
Further, in the powder transport apparatus according to the present invention, the differential pressure between the two points in the transport tube for transporting the powder gas is measured by the differential pressure gauge, and the differential pressure fluctuation width or differential pressure fluctuation measured. When the ratio between the width and the average value of the differential pressure exceeds the set value, the alarm transmitter issues an alarm and automatically increases the flow rate of the carrier gas that conveys the powder as a gas, or automatically supplies the powder. Even if the load fluctuation in the transport pipe is large by monitoring the differential pressure fluctuation range or the ratio between the differential pressure fluctuation range and the average differential pressure value and issuing an alarm, The clogging can be detected at an early stage, and the clogging can be automatically cleared by increasing the flow rate of the carrier gas or decreasing the powder supply amount.

【0011】また、本発明に係る粉体輸送装置において
は、粉体を気体輸送する輸送管における2点間の差圧が
差圧計により計測され計測される差圧の変動幅または差
圧の変動幅と差圧の平均値との比が設定値以上になると
警報発信器が警報を発信するとともに粉体を気体輸送す
る搬送ガスに代えてパージ用ガスを輸送管内へ導入する
ようになっており、差圧の変動幅または差圧の変動幅と
差圧の平均値との比を監視して警報を発信することによ
り輸送管における負荷変動が大きい場合でも粉体の詰ま
りの検出を早期に行うことができ、またパージ用ガスを
輸送管内へ導入することにより自動的に詰まりの解消が
可能になる。
Further, in the powder transport apparatus according to the present invention, the differential pressure between the two points in the transport tube for transporting the powder by gas is measured by the differential pressure gauge and the fluctuation width of the differential pressure or the fluctuation of the differential pressure is measured. When the ratio between the width and the average value of the differential pressure exceeds the set value, the alarm transmitter issues an alarm and the purge gas is introduced into the transport pipe instead of the carrier gas that transports the powder by gas. By detecting the fluctuation range of the differential pressure or the ratio between the fluctuation range of the differential pressure and the average value of the differential pressure and issuing an alarm, the clogging of the powder can be detected early even if the load fluctuation in the transport pipe is large. Moreover, by introducing the purging gas into the transportation pipe, the clogging can be automatically cleared.

【0012】[0012]

【実施例】図1および図2は本発明の一実施例に係る粉
体輸送装置の説明図である。図において、本実施例に係
る粉体輸送装置は微粉炭など粉体の気体輸送に使用され
るもので、図における符号1は粉体用ホッパ、2はロー
タリバルブ、3は搬送ガスの配管、4はエゼクタ、5は
粉体の輸送管、6は差圧計、7は容器、8は検出用配
管、9は計算機(コンピュータ)、10は警報発信器、
11は搬送ガスの流量調整弁、12は搬送ガスの遮断
弁、13はパージ用ガスの配管、14はパージ用ガスの
遮断弁である。粉体用ホッパ1内に貯蔵されている粉体
は、ロータリバルブ2によりエゼクタ4に供給されて搬
送ガスの配管3から導入されるガスと混合され、輸送管
5を通って容器7内へ輸送される。輸送管5には途中の
2点A,B間の差圧を検出するために差圧計6が検出用
配管8を介して配設されており、差圧計6の出力が計算
機9に入力される。計算機9で2点A,B間の差圧の変
動幅X、差圧の絶対値の平均値Y、これらX,Yの比Z
=X/Yが連続して算出され、変動幅Xまたは比Zの値
が予め設定したそれぞれの設定値X0 ,Z0 を越えると
警報発信器10から警報が発信され、警報の発信と同時
に搬送ガスの流量調整弁11を開けて搬送ガスの流量を
増加させるようになっている。そして、一定の時間が経
過した後においてなおも警報の発信が継続している場合
には、ロータリバルブ2の回転数を遅くすることにより
粉体の供給量を減少させ、さらに一定の時間が経過した
後においてなおも警報が継続している場合には、搬送ガ
スの遮断弁12を閉めるとともにパージ用ガスの遮断弁
14を開けて高圧のパージ用ガスを粉体の輸送管5内に
導入し、輸送管5内における粉体の詰まりを除去するよ
うになっている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIGS. 1 and 2 are explanatory views of a powder transport device according to an embodiment of the present invention. In the figure, the powder transport device according to the present embodiment is used for transporting powder gas such as pulverized coal. Reference numeral 1 in the figure is a powder hopper, 2 is a rotary valve, 3 is a carrier gas pipe, 4 is an ejector, 5 is a powder transportation pipe, 6 is a differential pressure gauge, 7 is a container, 8 is detection pipe, 9 is a computer (computer), 10 is an alarm transmitter,
Reference numeral 11 is a carrier gas flow rate adjusting valve, 12 is a carrier gas cutoff valve, 13 is a purge gas pipe, and 14 is a purge gas cutoff valve. The powder stored in the powder hopper 1 is mixed with the gas supplied to the ejector 4 by the rotary valve 2 and introduced from the carrier gas pipe 3, and is transported into the container 7 through the transport pipe 5. To be done. A differential pressure gauge 6 is arranged on the transport pipe 5 to detect a differential pressure between two points A and B on the way, and a differential pressure gauge 6 is input to a calculator 9 via an output pipe 8. . In the computer 9, the fluctuation width X of the differential pressure between the two points A and B, the average value Y of the absolute values of the differential pressure, and the ratio Z of these X and Y.
= X / Y is continuously calculated, and when the value of the fluctuation range X or the ratio Z exceeds the preset set values X 0 and Z 0 , an alarm is issued from the alarm transmitter 10, and at the same time as the alarm is issued. The carrier gas flow rate adjusting valve 11 is opened to increase the carrier gas flow rate. Then, if the alarm is still being issued after the lapse of a certain period of time, the rotation speed of the rotary valve 2 is slowed to reduce the powder supply amount, and a certain period of time has elapsed. If the alarm still continues after that, the shutoff valve 12 for the carrier gas is closed and the shutoff valve 14 for the purge gas is opened to introduce the high-pressure purge gas into the powder transport pipe 5. The clogging of the powder in the transport pipe 5 is removed.

【0013】輸送管5内に詰まりがない場合は差圧の変
動幅Xは小さいが、輸送管5の底部に粉体が滞留し始め
ると搬送ガスの流速が上昇し、滞留し始めた粉体が浮遊
して搬送されるために差圧の変動が大きくなる。一般
に、輸送管5内に詰まりが発生する場合にはこのような
粉体の滞留と浮遊による搬送を繰り返しながら差圧の変
動幅Xが次第に大きくなっていく。従って、差圧の変動
幅Xを監視することにより、輸送管5における詰まりの
早期検出が可能である。特に、差圧の変動幅Xと、差圧
の絶対値の平均値Yとの比を監視することにより、負荷
の変動が大きい場合でも詰まりの検出を早期に行うこと
ができる。図2に示すように、差圧の変動幅X及び差圧
の変動幅Xと変動幅の絶対値の平均値Yとの比Zは輸送
管5が詰まり始めると顕著に増加するが、それぞれの設
定値X0 , 0 になると警報が発信されるとともに搬送
ガスの流量が直ちに増加されるので、差圧の変動幅X及
び平均値Yは詰まり始める前と略等しい値まで低下して
輸送管5の閉塞が防止される。なお、差圧の平均値Yも
この間に若干増加しているが、その平均値Yの増加は小
さく、従って差圧の平均値Yによる早期検出は不可能で
ある。このように、輸送管5の詰まりが速い速度で進行
する場合には、パージ用ガスの供給量を増加させるのみ
では差圧の変動幅Xを減少させることができないことも
あるが、その場合には粉体の供給量を減少させることに
より差圧の変動幅Xが低減して詰まりが防止される。ま
た、場合によっては何れの対策を実施しても差圧の変動
幅Xが減少しない場合もあり、そのような場合にそのま
ま放置するとやがて輸送管5が完全に閉塞してしまい、
詰まった粉体の除去に多大な労力を要するため、前述2
つの対策を実施しても効果がない場合には搬送ガスの遮
断弁12を閉めるとともにパージ用ガスの遮断弁14を
開けてパージ用ガスを輸送管5内に導入し、詰まりを除
去して輸送管5の完全な閉塞を防止することにより比較
的短時間内で運転を再開することができる。
When the transport pipe 5 is not clogged, the fluctuation range X of the differential pressure is small, but when the powder starts to stay at the bottom of the transport pipe 5, the flow velocity of the carrier gas increases, and the powder starts to stay. Since the particles are floated and conveyed, the fluctuation of the differential pressure becomes large. In general, when clogging occurs in the transport pipe 5, the fluctuation width X of the differential pressure gradually increases while repeating such powder retention and transportation. Therefore, by monitoring the fluctuation width X of the differential pressure, it is possible to detect clogging in the transport pipe 5 at an early stage. In particular, by monitoring the ratio between the fluctuation range X of the differential pressure and the average value Y of the absolute values of the differential pressure, the clogging can be detected early even when the fluctuation of the load is large. As shown in FIG. 2, the fluctuation range X of the differential pressure and the ratio Z of the fluctuation range X of the differential pressure and the average value Y of the absolute values of the fluctuation ranges increase remarkably when the transport pipe 5 starts to be clogged. When the set values X 0 and Z 0 are reached, an alarm is issued and the flow rate of the carrier gas is immediately increased. Therefore, the fluctuation width X and the average value Y of the differential pressure are reduced to substantially the same values as before clogging, and the transport pipe Blockage of 5 is prevented. Note that the average value Y of the differential pressures also increases slightly during this period, but the increase of the average value Y is small, so early detection by the average value Y of the differential pressures is impossible. As described above, when the clogging of the transport pipe 5 progresses at a high speed, it may not be possible to reduce the fluctuation width X of the differential pressure only by increasing the supply amount of the purge gas, but in that case. By reducing the powder supply amount, the fluctuation width X of the differential pressure is reduced and clogging is prevented. Further, depending on the case, the variation width X of the differential pressure may not be reduced even if any of the measures is taken, and in such a case, if left as it is, the transportation pipe 5 will be completely blocked, and
It takes a lot of work to remove the clogged powder, so
If the two measures are not effective, the carrier gas shutoff valve 12 is closed, the purge gas shutoff valve 14 is opened, and the purge gas is introduced into the transport pipe 5 to remove the clogging and transport it. By preventing the tube 5 from being completely closed, the operation can be restarted within a relatively short time.

【0014】従来の粉体輸送装置においては輸送管途中
の2点A,B間で粉体の詰まりが発生すると差圧計によ
り詰まりの検出が可能になっているが、仮に他の2点間
で詰まりが発生した場合には、差圧計によって検出され
る差圧が設定値よりも過大にならないために検出されな
い。仮に、点Aがエゼクタに隣接して設置されていると
ともに点Bが容器に隣接していれば、輸送管の何処で詰
まりが発生しても原理的にはその検出が可能である。し
かしながら、このような粉体輸送装置においては実際に
は粉体及び搬送ガスの流量が常に一定ではなく、粉体輸
送装置の負荷変動とともに変化するのが一般的であり、
これに伴って差圧も大きく変動するために詰まりを検出
するための差圧の設定値を十分に高い値に設定する必要
がある。即ち、粉体の供給量や搬送ガスなどの流量が少
ない場合には、通常の運転中における差圧と設定値との
差が大きすぎるために輸送管における粉体の詰まりを早
期に検出することができないが、本粉体輸送装置におい
てはこのような不具合を解決して負荷、或いは差圧計の
設置位置などに関係なく、詰まりの早期検出および詰ま
りの自動的な除去が可能なように、輸送管5の2点A,
B間の差圧を計測し、その差圧の変動幅Xが設定値以上
になった場合、またはその差圧の変動幅Xと差圧の絶対
値の平均値Yとの比Zが設定値以上になった場合にはそ
れらが設定値以下に下がるまで搬送ガスの流量を増加さ
せ、さらに粉体の供給量を減少させ、それでも差圧が設
定値以下に下がらない場合にはパージ用ガスを輸送管5
内へ自動的に導入するなどして輸送管5が詰まり気味の
状態からその検出が可能になるとともに自動的に詰まり
の解消が可能になる。
In the conventional powder transport device, when the powder is clogged between two points A and B in the middle of the transportation pipe, the clogging can be detected by the differential pressure gauge. When the clogging occurs, it is not detected because the differential pressure detected by the differential pressure gauge does not exceed the set value. If point A is installed adjacent to the ejector and point B is adjacent to the container, it is possible in principle to detect where the transport pipe is clogged. However, in such a powder transport apparatus, the flow rates of the powder and the carrier gas are not always constant in practice, and generally change with the load fluctuation of the powder transport apparatus,
Along with this, the differential pressure also fluctuates greatly, so it is necessary to set the set value of the differential pressure for detecting clogging to a sufficiently high value. That is, when the powder supply amount or carrier gas flow rate is low, the clogging of the powder in the transport pipe must be detected early because the difference between the differential pressure and the set value during normal operation is too large. However, in this powder transporter, such a problem can be solved to enable the early detection of clogging and the automatic removal of clogging regardless of the load or the installation position of the differential pressure gauge. 2 points A on tube 5,
When the differential pressure between B is measured and the fluctuation range X of the differential pressure becomes equal to or greater than the set value, or the ratio Z between the fluctuation range X of the differential pressure and the average value Y of the absolute values of the differential pressure is the set value. In case of above, increase the flow rate of carrier gas until they fall below the set value, further reduce the powder supply amount, and if the differential pressure still does not fall below the set value, purge gas Transport pipe 5
It is possible to automatically detect the clogging of the transportation pipe 5 by automatically introducing it into the inside, and to automatically eliminate the clogging.

【0015】[0015]

【発明の効果】本発明に係る粉体輸送装置は前記のよう
に構成されており、輸送管における負荷変動が大きい場
合でも粉体の詰まりの検出を早期に行うことができるの
で、輸送管が詰まり気味の状態から検出が可能になって
詰まりの解消が容易に行われる。
The powder transport apparatus according to the present invention is configured as described above, and the clogging of the powder can be detected early even when the load fluctuation in the transport tube is large. It becomes possible to detect from a clogged state, and clogging can be easily eliminated.

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

【図1】図1は本発明の一実施例に係る粉体輸送装置の
フロー系統図である。
FIG. 1 is a flow system diagram of a powder transportation apparatus according to an embodiment of the present invention.

【図2】図2はその運転結果を示す作用説明図である。FIG. 2 is an operation explanatory view showing the operation result.

【図3】図3(a)は従来の粉体輸送装置のフロー系統
図、同図(b)はその作用説明図である。
FIG. 3 (a) is a flow system diagram of a conventional powder transport device, and FIG. 3 (b) is an operation explanatory diagram thereof.

【符号の説明】[Explanation of symbols]

1 粉体用ホッパ 2 ロータリバルブ 3 搬送ガスの配管 4 エゼクタ 5 粉体の輸送管 6 差圧計 7 容器 8 検出用配管 9 計算機 10 警報発信器 11 搬送ガスの流量調整弁 12 搬送ガスの遮断弁 13 パージ用ガスの配管 14 パージ用ガスの遮断弁 1 Powder Hopper 2 Rotary Valve 3 Carrier Gas Pipe 4 Ejector 5 Powder Transport Pipe 6 Differential Pressure Meter 7 Container 8 Detection Pipe 9 Computer 10 Alarm Transmitter 11 Carrier Gas Flow Control Valve 12 Carrier Gas Shutoff Valve 13 Purge gas piping 14 Purge gas shutoff valve

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 粉体を気体輸送する輸送管における2点
間の差圧を計測する差圧計と、該差圧計により計測され
る差圧の変動幅が設定値以上になると警報を発信する警
報発信器とを備えたことを特徴とする粉体輸送装置。
1. A differential pressure gauge for measuring the differential pressure between two points in a transport pipe for transporting powder by gas, and an alarm for issuing an alarm when the fluctuation range of the differential pressure measured by the differential pressure gauge exceeds a set value. A powder transportation device comprising a transmitter.
【請求項2】 粉体を気体輸送する輸送管における2点
間の差圧を計測する差圧計と、該差圧計により計測され
る差圧の変動幅と差圧の平均値との比が設定値以上にな
ると警報を発信する警報発信器とを備えたことを特徴と
する粉体輸送装置。
2. A differential pressure gauge for measuring a differential pressure between two points in a transport pipe for transporting powder by gas, and a ratio between a fluctuation range of the differential pressure measured by the differential pressure gauge and an average value of the differential pressure is set. A powder transportation device, comprising: an alarm transmitter that outputs an alarm when the value exceeds a value.
【請求項3】 上記警報の発信とともに粉体を気体輸送
する搬送ガスの流量を自動的に増加、或いは粉体の供給
量を自動的に減少させる手段を備えたことを特徴とする
請求項1または請求項2に記載の粉体輸送装置。
3. A means for automatically increasing the flow rate of a carrier gas for gas-transporting powder or automatically decreasing the supply amount of powder when the alarm is issued. Alternatively, the powder transportation device according to claim 2.
【請求項4】 上記警報の発信とともに粉体を気体輸送
する搬送ガスに代えてパージ用ガスを上記輸送管内へ導
入する手段を備えたことを特徴とする請求項1または請
求項2に記載の粉体輸送装置。
4. The device according to claim 1, further comprising means for introducing a purging gas into the transportation pipe in place of the carrier gas for pneumatically transporting the powder when the alarm is issued. Powder transport device.
JP30795493A 1993-12-08 1993-12-08 Powder transporting apparatus Withdrawn JPH07158837A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30795493A JPH07158837A (en) 1993-12-08 1993-12-08 Powder transporting apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30795493A JPH07158837A (en) 1993-12-08 1993-12-08 Powder transporting apparatus

Publications (1)

Publication Number Publication Date
JPH07158837A true JPH07158837A (en) 1995-06-20

Family

ID=17975173

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30795493A Withdrawn JPH07158837A (en) 1993-12-08 1993-12-08 Powder transporting apparatus

Country Status (1)

Country Link
JP (1) JPH07158837A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997038789A1 (en) * 1996-04-16 1997-10-23 Toyo Engineering Corporation Method of detecting clogging and method of granulation
JPH11343029A (en) * 1998-06-02 1999-12-14 Toa Harbor Works Co Ltd Quantitative feeding device of expandable beads
JP2010006060A (en) * 2008-05-30 2010-01-14 Mitsubishi Gas Chemical Co Inc Method and apparatus for producing thermoplastic resin pellets
JP2010202701A (en) * 2009-02-27 2010-09-16 Sumitomo Chemical Co Ltd Transfer method for powder, method for manufacturing olefin polymer, transfer piping, and manufacturing apparatus
JP2014124583A (en) * 2012-12-26 2014-07-07 Shinagawa Refractories Co Ltd Device and method for transporting powder and granular material
WO2018200795A1 (en) 2017-04-27 2018-11-01 Oerlikon Metco (Us) Inc. Method for detecting and diagnosing powder flow stability
JP2020196601A (en) * 2019-06-05 2020-12-10 宇部興産機械株式会社 Gas conveyance apparatus

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997038789A1 (en) * 1996-04-16 1997-10-23 Toyo Engineering Corporation Method of detecting clogging and method of granulation
AU704922B2 (en) * 1996-04-16 1999-05-06 Toyo Engineering Corporation Method for detecting clogging and method of granulation
US5964901A (en) * 1996-04-16 1999-10-12 Toyo Engineering Corporation Method for detecting clogging and granulation method
JPH11343029A (en) * 1998-06-02 1999-12-14 Toa Harbor Works Co Ltd Quantitative feeding device of expandable beads
JP2010006060A (en) * 2008-05-30 2010-01-14 Mitsubishi Gas Chemical Co Inc Method and apparatus for producing thermoplastic resin pellets
JP2010202701A (en) * 2009-02-27 2010-09-16 Sumitomo Chemical Co Ltd Transfer method for powder, method for manufacturing olefin polymer, transfer piping, and manufacturing apparatus
JP2014124583A (en) * 2012-12-26 2014-07-07 Shinagawa Refractories Co Ltd Device and method for transporting powder and granular material
WO2018200795A1 (en) 2017-04-27 2018-11-01 Oerlikon Metco (Us) Inc. Method for detecting and diagnosing powder flow stability
JP2020517917A (en) * 2017-04-27 2020-06-18 エリコン メテコ(ユーエス)インコーポレイテッド Method for detecting and diagnosing powder flow stability
EP3615222A4 (en) * 2017-04-27 2021-01-06 Oerlikon Metco (US) Inc. Method for detecting and diagnosing powder flow stability
JP2020196601A (en) * 2019-06-05 2020-12-10 宇部興産機械株式会社 Gas conveyance apparatus

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