JPS59189953A - Method for preventing clogging of cyclone - Google Patents
Method for preventing clogging of cycloneInfo
- Publication number
- JPS59189953A JPS59189953A JP6301683A JP6301683A JPS59189953A JP S59189953 A JPS59189953 A JP S59189953A JP 6301683 A JP6301683 A JP 6301683A JP 6301683 A JP6301683 A JP 6301683A JP S59189953 A JPS59189953 A JP S59189953A
- Authority
- JP
- Japan
- Prior art keywords
- clogging
- cyclone
- blockage
- exhaust gas
- under
- 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
Abstract
Description
【発明の詳細な説明】
本発明は熱分解装置における流動層燃焼塔などの如く、
燃焼排ガスからダストを除去するサイクロンのダスト閉
塞を防止する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention applies to a fluidized bed combustion tower in a pyrolysis apparatus, etc.
The present invention relates to a method for preventing dust clogging of a cyclone for removing dust from combustion exhaust gas.
この種のサイクロンにおいては、サイクロンのアンダー
70−側の一部にダスト(灰や摩耗砂などの固形粒子)
が堆積しついには閉塞を起こし、運転に支障を来たすこ
とがあるが、従来は、ダストの偵−出がなくなったこと
により閉塞が生じたことを検知していた。従って、検知
されたとトには、閉塞の程度は大とく、これを解除する
ためには装置の運転を停止し、分1q?l’ して閉塞
物を取除ぎ、その後再び組立てを行なう必要があった。In this type of cyclone, dust (solid particles such as ash and abrasion sand) is present in a part of the under 70-side of the cyclone.
However, conventionally, the occurrence of a blockage was detected when the dust was no longer ejected. Therefore, when a blockage is detected, the degree of blockage is considered to be large, and in order to release the blockage, the operation of the device must be stopped and the blockage must be stopped for 1 minute. 1' to remove the obstruction and then reassembly.
従って装置の稼働率低下による処理能力の低下を招ト、
また、多大の手間と費用を要する欠点があった。Therefore, the processing capacity decreases due to a decrease in the operating rate of the equipment.
In addition, there was a drawback that it required a great deal of effort and cost.
本発明は、従来の方法の上記の欠点を除外、装置の運転
を停止することなく閉塞が生じたことを軽微なうちに発
見し、さらに閉塞解除を行なうことがで終る、サイクロ
ンの閉塞防止方法を提供することを目的とするものであ
る。The present invention eliminates the above-mentioned drawbacks of the conventional methods, and provides a method for preventing blockages in cyclones, which allows the occurrence of blockages to be detected before they are slight and the blockages to be cleared without stopping the operation of the equipment. The purpose is to provide the following.
本発明は、燃焼塔で発生する排ガスに含まれるダストを
分離するサイクロンの閉塞防止方法において、前記サイ
クロンのアンダーフロー側の閉塞を検知する閉塞検知機
構の閉塞信号により、アンダー70−側に備えられた圧
力遮断機構お間外、排ガスをアンダーフロー側に流して
、閉塞物を取除くことを特徴とするサイクロンの閉塞防
止方法である。The present invention provides a method for preventing blockage of a cyclone that separates dust contained in exhaust gas generated in a combustion tower, in which a blockage signal from a blockage detection mechanism that detects blockage on the underflow side of the cyclone is detected. This is a method for preventing blockage of a cyclone, which is characterized by removing the blockage by flowing the exhaust gas to the underflow side outside of the pressure cutoff mechanism.
本発明の実施例を図面を用いて説明する。Embodiments of the present invention will be described using the drawings.
第1図において、1は流動層式の燃焼塔であり、発生す
る排ガスは、サイクロン2,5でダストを除去し、排ガ
スボイラ8と熱交換器9,10によって排ガスの温度を
下げ電気集j賜磯14において微小なダストを除去した
後に排突15から大気へ放出される。一方サイクロン2
,5で捕集されたダストはサイクロン2,5のダストホ
ッパ3,6に短時[1旧6)留した後に、圧力遮断機構
を有するダスト抜出し装置7.4によってアッシュバン
カ11に貯留され適宜アッシュ抜出し装置13によって
熱分解装置系外へ搬出される。バイパス弁12はアッシ
ュバンカ11と電気集塵機14を接続するバイパス16
に設けられており、通常は閉じている。In Fig. 1, reference numeral 1 denotes a fluidized bed type combustion tower, and the generated exhaust gas is subjected to cyclones 2 and 5 to remove dust, and an exhaust gas boiler 8 and heat exchangers 9 and 10 to lower the temperature of the exhaust gas. After fine dust is removed at the rock bottom 14, it is released into the atmosphere from the exhaust port 15. On the other hand, cyclone 2
, 5 is stored in the dust hoppers 3, 6 of the cyclones 2, 5 for a short time [1 old 6), and then stored in the ash bunker 11 by the dust extraction device 7.4 having a pressure cut-off mechanism, where it is ashed as appropriate. The extraction device 13 carries out the pyrolyzer outside the pyrolysis system. The bypass valve 12 is a bypass 16 that connects the ash bunker 11 and the electrostatic precipitator 14.
and is normally closed.
第2図はサイクロン2,51;j近の3Y細を示す。Figure 2 shows the 3Y narrow near cyclones 2,51;j.
ダスト抜出し装置4,7は二重ダンパ式の圧力遮断機構
としてダンパ20,2 +、22.23を備え、上下の
ダンパをかわるがわる開閉し、サイクロン2.5内の正
圧の排ガスかアンダー70−側に吹抜けることを防ぎな
からダストを排出するようになっている。50.5 +
、52,53,54.55は温度検出器、56は制御装
置である。The dust extraction devices 4, 7 are equipped with dampers 20, 2 +, 22.23 as a double damper type pressure cutoff mechanism, and the upper and lower dampers are opened and closed in turn, and the positive pressure exhaust gas in the cyclone 2.5 is removed from the under 70 -. It is designed to prevent dust from blowing to the side and to exhaust the dust. 50.5 +
, 52, 53, 54, and 55 are temperature detectors, and 56 is a control device.
サイクロン2又は5のアンダー70−側、即ちダストホ
ッパ3又は6から下方の管路や装置に閉塞が起こるとサ
イクロン2.5又はダストホッパ3.6内の温度が上昇
するので、所定の)、1度を越えたときに閉塞が生じた
と判断して制御装置56より閉塞信号を発する。即ち、
温度検出器50゜51.52,53,54.55及び制
御装置56により閉塞検知機構を形成し、閉塞を早期に
発見することができる。If a blockage occurs in the under 70 side of the cyclone 2 or 5, that is, in the pipes or equipment below from the dust hopper 3 or 6, the temperature inside the cyclone 2.5 or the dust hopper 3.6 will rise, so the temperature within the cyclone 2.5 or the dust hopper 3.6 will rise. When the distance exceeds 1, it is determined that a blockage has occurred, and the control device 56 issues a blockage signal. That is,
The temperature detectors 50, 51, 52, 53, 54, 55 and the control device 56 form a blockage detection mechanism, allowing early detection of blockages.
閉塞検知(幾構より発せられた閉塞信号により、圧力遮
断機構を形成するダンパ20,2+、22゜23、バ′
イパス弁12が開かれ、サイクロン2,5内の高圧の排
ガスが吹抜けてアンダー70−側を流れてアッシュバン
カ11に入り、さらにバイパス弁12、電気集塵機14
を経て煙突15から掴出される。アッシュ抜出し装置1
3内のダンパは閉じて排ガスか漏洩しないようにしてお
く。Blockage detection (Dampers 20, 2+, 22° 23, and bar
The I-pass valve 12 is opened, and the high-pressure exhaust gas in the cyclones 2 and 5 blows through, flows through the under 70- side, enters the ash bunker 11, and then passes through the bypass valve 12 and the electrostatic precipitator 14.
After that, it is grabbed from chimney 15. Ash extraction device 1
Close the damper in 3 to prevent exhaust gas from leaking.
このとき、アンダー70−側の管路や機器を流れる排ガ
スにより、堆積していたダストが吹飛ばされて閉塞が解
消される。At this time, the accumulated dust is blown away by the exhaust gas flowing through the pipes and equipment on the under 70 side, and the blockage is eliminated.
所定時間後、又は、排ガスの流れ状態が正常となって閉
塞か′1屑消されたことを、アツシュバ・シカ11内圧
力又はバイパス弁+2(=I近の圧ツバ或いはこれらの
圧力とサイクロン2.5の内圧との差圧或いは排ガス流
量J1などにより検出して判定したとぎにバイパス弁1
2を閉し、圧力遮断(幾構の作動を定常の状態に復帰せ
しめる。After a predetermined period of time, or when the flow condition of exhaust gas becomes normal and the blockage has been eliminated, the internal pressure of Ashba Shika 11 or the bypass valve +2 (= I) When the bypass valve 1 is detected and judged based on the differential pressure with the internal pressure of .5 or the exhaust gas flow rate J1, etc.
2 is closed to shut off the pressure (returning several operations to normal conditions).
閉塞検知機構は次の如く構成してもよい。装置の運転中
に、適当な時期に、所定の時間の111.圧力遮断機構
を開放する。このときアンダーフロー側に流れる掴ガス
の流れ状態を直接又は間接に検知する。閉塞がないとき
の正常なアンダー70−側の排ガス流量を確認しておぎ
、この正常流量と検出流量とを比較すれば閉塞の状態が
わかり、許容限度を越えていれば閉塞と判定し所定時間
の間続けて圧力遮断機構を開き掴ガスをアンダー70−
側に流してダストの堆積を除外、閉塞を解消する。The occlusion detection mechanism may be configured as follows. 111 for a predetermined time at an appropriate time while the device is operating. Open the pressure cut-off mechanism. At this time, the flow state of the gripping gas flowing to the underflow side is detected directly or indirectly. Check the normal exhaust gas flow rate on the under 70- side when there is no blockage, and compare this normal flow rate with the detected flow rate to determine the state of blockage, and if it exceeds the allowable limit, it is determined that there is a blockage and the flow is continued for a predetermined period of time. Continue to open the pressure cutoff mechanism and release the gas under 70-
Run it to the side to exclude dust accumulation and eliminate blockages.
排ガス流れが正常であるかどうかは、流量計により直接
検知したり、各部の圧力又はそれらの圧力とサイクロン
2,5内の圧力との差圧などにより間接的に検知するこ
とがでトる。また、燃焼塔1の塔頂圧力の変化によって
も検知することかできる。Whether the exhaust gas flow is normal can be detected directly by a flow meter or indirectly by the pressure of each part or the differential pressure between those pressures and the pressure inside the cyclones 2 and 5. It can also be detected by changes in the pressure at the top of the combustion tower 1.
また、排ガスの流れにより閉塞の解除作業を行なうとと
ハンマやパイブレークにより振動を与えると堆積したダ
ストをくずしたり、固着したダストをはがし落とすのに
効果かある。In addition, if the flow of exhaust gas is used to release the blockage, applying vibration with a hammer or pie break is effective in breaking up accumulated dust and peeling off adhered dust.
以上は、単一のブロワ(押込ブロワ17)によつて流動
層1!!1焼塔及び仙ガス経路の通気を行なう場合の実
施例であって、サイクロン2,5における排ガスの圧力
は大気圧よりも犬と<シであるか、電気集塵(幾14と
煙突15との開に誘引送風機(図示せず)を追加して設
けて本発明を実施することも可能であり、その場合には
サイクロン2,5の掴゛ガスj王力は負j王にすること
が′望ましい。The above is a fluidized bed 1! using a single blower (pushing blower 17). ! This is an example in which the exhaust gas pressure in cyclones 2 and 5 is less than atmospheric pressure, or the electrostatic precipitator (14 and chimney 15) It is also possible to carry out the present invention by additionally installing an induced blower (not shown) in the opening of the cyclones 2 and 5. 'desirable.
本発明により、燃焼装置の運転を停止することなく、閉
塞を早期に発見し、かつ閉塞物の除去を短時間内に行な
い、装置の稼働率を損なうことなく簡単に確実に閉塞1
1イ消を行なうことかで外るサイクロンの閉塞防雨方法
を提供することかでき、実用に極めて大なる効果を奏す
る。According to the present invention, a blockage can be detected early without stopping the operation of the combustion equipment, and the blockage can be removed within a short time.
It is possible to provide a rain-proofing method for blocking a cyclone, which can be removed by one extinguishing operation, and is extremely effective in practical use.
図面は本発明の実施例を示し第1図は全体のフロー図、
第2図はサイクロン付近の詳細なフロー図である。
1・・燃焼塔、2・・サイクロン、3・・ダストホッパ
、4・・ダスト抜出し装置、5・・サイクロン、6・・
ダストホッパ、7・・ダスト抜出シ装置、8・・徘力゛
スポイラ、9,10・・熱交換器1.lI・・アッシュ
バンカ、12・・バイパス弁、13・・アッシュ抜出し
装置、14・・電気集塵機、15・・煙突、1日・・バ
イパス、17・・押込ブロワ、20.2 +、22.2
3・・ダンパ、 50.5+、52,53,54.5
5・・温度検出器、56・・制御装置。The drawings show embodiments of the present invention, and FIG. 1 is an overall flow diagram.
FIG. 2 is a detailed flow diagram around the cyclone. 1... Combustion tower, 2... Cyclone, 3... Dust hopper, 4... Dust extraction device, 5... Cyclone, 6...
Dust hopper, 7. Dust extraction device, 8. Spoiler, 9, 10. Heat exchanger 1. lI...Ash bunker, 12...Bypass valve, 13...Ash extraction device, 14...Electric dust collector, 15...Chimney, 1st...Bypass, 17...Force blower, 20.2 +, 22.2
3. Damper, 50.5+, 52, 53, 54.5
5...Temperature detector, 56...Control device.
Claims (1)
離するサイクロンの閉塞防止方法において、前記サイク
ロンのアンダー70−側の閉塞を検知する閉塞検知機構
の閉塞信号により、アンダーフロー側に備えられた圧力
遮断機構を開ト、徘力゛スをアンダーフロー側に流して
、閉塞物を取除くことを特徴とするサイクロンの閉塞防
止方法。 2、 前記閉塞検知(幾構が、前記圧力遮断機構を所定
時間の間開いて、前記アンダーフロー側の排ガスの流れ
状態により閉塞の状態を検知する機構である特許請求の
範囲第1項記載の方法。 3、 前記閉塞検知(幾構が゛、前記サイクロン内の温
度を検出することにより閉塞の状態を検知する(幾描で
ある特許請求の範囲第1項記載の方法。[Claims] 1. In a method for preventing blockage of a cyclone that separates dust contained in exhaust gas generated in a combustion tower, a blockage signal from a blockage detection mechanism that detects blockage on the under 70 side of the cyclone is used. A method for preventing blockage of a cyclone, which is characterized in that a pressure cutoff mechanism provided on the underflow side is opened, and a wandering force is allowed to flow to the underflow side to remove the blockage. 2. The blockage detection mechanism is a mechanism that opens the pressure cutoff mechanism for a predetermined period of time and detects the blockage state based on the flow state of the exhaust gas on the underflow side. Method. 3. The method according to claim 1, wherein the blockage detection includes detecting the state of blockage by detecting the temperature within the cyclone.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6301683A JPS59189953A (en) | 1983-04-12 | 1983-04-12 | Method for preventing clogging of cyclone |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6301683A JPS59189953A (en) | 1983-04-12 | 1983-04-12 | Method for preventing clogging of cyclone |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59189953A true JPS59189953A (en) | 1984-10-27 |
JPS6341622B2 JPS6341622B2 (en) | 1988-08-18 |
Family
ID=13217097
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6301683A Granted JPS59189953A (en) | 1983-04-12 | 1983-04-12 | Method for preventing clogging of cyclone |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59189953A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007315686A (en) * | 2006-05-26 | 2007-12-06 | Chugoku Electric Power Co Inc:The | Fly ash amount management method following coal type changing in fluidized bed boiler |
CN102261930A (en) * | 2010-08-24 | 2011-11-30 | 鞍钢集团矿业公司 | Method for indirectly detecting cyclone blockage |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0369710A (en) * | 1989-08-08 | 1991-03-26 | Tokyu Constr Co Ltd | Step block and construction thereof |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54142885U (en) * | 1978-03-29 | 1979-10-03 |
-
1983
- 1983-04-12 JP JP6301683A patent/JPS59189953A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54142885U (en) * | 1978-03-29 | 1979-10-03 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007315686A (en) * | 2006-05-26 | 2007-12-06 | Chugoku Electric Power Co Inc:The | Fly ash amount management method following coal type changing in fluidized bed boiler |
CN102261930A (en) * | 2010-08-24 | 2011-11-30 | 鞍钢集团矿业公司 | Method for indirectly detecting cyclone blockage |
Also Published As
Publication number | Publication date |
---|---|
JPS6341622B2 (en) | 1988-08-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0077222B1 (en) | Bypass control system | |
JPS59189953A (en) | Method for preventing clogging of cyclone | |
JPS5936519A (en) | Dust discharging device of dust collector for blast furnace gas | |
JP3740200B2 (en) | Blast furnace bleeder valve and operation control method thereof | |
JPH04274731A (en) | Method and apparatus for detecting glanular material contained in high-temperature gas flow | |
JP3469489B2 (en) | Circulating fluidized bed furnace | |
JP4129703B2 (en) | Dedusting device | |
JPS596691B2 (en) | Foreign matter removal method | |
JP3605224B2 (en) | Granular material transport device | |
JPS6021202B2 (en) | Processing method for gas generated in a blast furnace when blowing down the furnace | |
JPS6043886B2 (en) | Waste gas recovery method in converter waste gas treatment equipment | |
JPS5974206A (en) | Safety device for top pressure recovering device of blast furnace | |
CN111664715B (en) | Waste heat recovery system | |
CN208465404U (en) | It can guarantee the device of flue gas separative efficiency | |
JP2573437B2 (en) | Operating method of blast furnace gas energy recovery equipment | |
JP4031771B2 (en) | Fly ash delivery method and system | |
JP3327743B2 (en) | Dust collection device | |
JPH07284622A (en) | Ceramic filter provided with safety device | |
CN218944571U (en) | Gravity dust removal ash discharging nitrogen back-blowing device | |
KR200308395Y1 (en) | A device for preventing the blocking of line in a dust recycling system | |
JP2763245B2 (en) | Emergency exhaust gas relief device | |
JPS5941407A (en) | Dry dust separator for exhaust gas from blast furnace | |
JPS6387517A (en) | Fluidized-bed incinerator | |
WO2006017964A1 (en) | A drip-type dusting installation having discharge function | |
JPS5974207A (en) | Safety device of top pressure energy recovering device of blast furnace |