JP2655875B2 - Crusher - Google Patents

Crusher

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Publication number
JP2655875B2
JP2655875B2 JP11886088A JP11886088A JP2655875B2 JP 2655875 B2 JP2655875 B2 JP 2655875B2 JP 11886088 A JP11886088 A JP 11886088A JP 11886088 A JP11886088 A JP 11886088A JP 2655875 B2 JP2655875 B2 JP 2655875B2
Authority
JP
Japan
Prior art keywords
air
raw material
coal
pipe
supply pipe
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 - Lifetime
Application number
JP11886088A
Other languages
Japanese (ja)
Other versions
JPH01288348A (en
Inventor
克昭 田中
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 Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP11886088A priority Critical patent/JP2655875B2/en
Publication of JPH01288348A publication Critical patent/JPH01288348A/en
Application granted granted Critical
Publication of JP2655875B2 publication Critical patent/JP2655875B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、固体原料を粉砕する粉砕装置に係り、特に
投入原料の供給管部における原料の詰まりの早期検出を
可能にした粉砕装置に関する。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pulverizing apparatus for pulverizing a solid raw material, and more particularly to a pulverizing apparatus capable of early detection of clogging of a raw material in a supply pipe section of an input raw material.

〔従来の技術〕[Conventional technology]

従来の粉砕装置における原料供給管部詰まりの検出方
法を第4図に示す縦形微粉炭機を例にとり説明する。
A method for detecting clogging of a raw material supply pipe in a conventional pulverizer will be described with reference to a vertical pulverizer shown in FIG. 4 as an example.

給炭機(図示せず)より送られてきた原料石炭10は、
微粉炭機1の中央に設けられた給炭管2に投入され、電
動機3、減速機4を介して駆動され回転する円盤状の下
部リング5と上部粉砕リング6の間に投入され、両リン
グに挟まれて回転する粉砕ボール7により粉砕される。
粉砕された石炭10は、下部リング下側の空気室8から送
入される乾燥および搬送用の熱風20により細粉10aおよ
び粗粉10bに粗分級され、細粉10aは粉砕機上部に設けら
れた分級器9によりさらに微粉10cと細粉10dに分級さ
れ、微粉10cは燃焼装置のバーナは、細粉10dはシュート
を通って再び下部リングの中央部へ戻り再粉砕される。
Raw coal 10 sent from a coal feeder (not shown)
It is put into a coal feed pipe 2 provided at the center of the pulverized coal machine 1, and is put between a disc-shaped lower ring 5 and an upper crushing ring 6 which are driven and rotated via an electric motor 3 and a speed reducer 4. Is pulverized by a pulverizing ball 7 which is sandwiched between and rotated.
The pulverized coal 10 is roughly classified into fine powder 10a and coarse powder 10b by hot air 20 for drying and transporting from the air chamber 8 below the lower ring, and the fine powder 10a is provided at the top of the pulverizer. The fine powder 10c is further classified into fine powder 10c and fine powder 10d by the classifier 9, and the fine powder 10c returns to the center of the lower ring again through the burner of the combustion device, passes through the chute, and is crushed again.

このような粉砕装置において、下部リング外側に設け
られた乾燥用空気の通過隙間21の上部には、上記の粗粉
10bおよび細粉10dが常時乾燥用空気によって浮遊状態と
なり、流動層を形成している。この流動層は、投入され
る原炭量の増減に従ってほぼ比例して層の厚さが変化す
る。
In such a pulverizing device, the above coarse powder is provided above the gap 21 for drying air provided outside the lower ring.
10b and the fine powder 10d are always in a floating state by the drying air, forming a fluidized bed. In this fluidized bed, the thickness of the bed changes substantially in proportion to the increase or decrease in the amount of raw coal supplied.

従来の装置では、粉砕装置の空気入口部22および分級
器入口部23に各々圧力検出座11および12を設け、流動層
を空気が通過する際の圧力差を求めるようにしている。
給炭管2内部に原料炭中の微粉が付着し堆積することに
より詰まりが発生し、粉砕機への供給炭が減少し、流動
層が薄くなると上記圧力差が減少する。これにより給炭
管の詰まりを検出している。通常運転範囲における上記
差圧は、300〜750mmAqと広範囲であり、低差圧の検出設
定値は100〜150mmAqとされている。
In the conventional apparatus, pressure detecting seats 11 and 12 are provided at the air inlet 22 and the classifier inlet 23 of the pulverizer, respectively, so as to obtain a pressure difference when air passes through the fluidized bed.
The fine powder in the raw coal is deposited and deposited in the coal feed pipe 2 to cause clogging, the amount of coal supplied to the pulverizer decreases, and when the fluidized bed becomes thinner, the pressure difference decreases. This detects the blockage of the coal pipe. The differential pressure in the normal operation range is as wide as 300 to 750 mmAq, and the detection set value of the low differential pressure is 100 to 150 mmAq.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

上記従来技術は、粉砕後の被粉砕物の流動層の上下差
圧の変化を検出することにより閉塞状況を探知するよう
になっているため、給炭管がほとんど閉塞し、原料炭の
供給が停止に近い状態になって初めて閉塞が発見される
という状況であった。そのため、詰まりが検出されるま
での時間的なロスが生じ、検出時点では給炭管内部に原
炭が閉塞し、粉砕機を停止して給炭管内の清掃をしなけ
ればならず、連続運転が不可能となるという問題があっ
た。また、付着防止のために給炭管内部に常時水を流す
等の方式も実施されているが、粉砕機内で石炭を乾燥し
つつ粉砕するという主旨と相反する方法である。
In the above prior art, since the clogging condition is detected by detecting a change in the pressure difference between the upper and lower sides of the fluidized bed of the material to be crushed, the coal feed pipe is almost blocked, and the supply of raw coal is reduced. It was a situation where blockage was discovered only when the condition was close to stopping. As a result, a time loss occurs until the clogging is detected. At the time of detection, the raw coal is clogged in the coal feed pipe, and the pulverizer must be stopped to clean the feed pipe. There was a problem that became impossible. Further, a method of constantly flowing water inside the coal feed pipe to prevent adhesion is also implemented, but this is a method contradicting the purpose of drying and pulverizing coal in a pulverizer.

本発明の目的は、給炭管内部への原料が付着し始めた
時点で付着を検出し、早期に給炭管内を清掃することに
より上記の問題なく粉砕機を連続運転することにある。
An object of the present invention is to continuously operate the pulverizer without the above-mentioned problem by detecting the adhesion at the time when the raw material starts to adhere to the inside of the coal feed pipe and cleaning the inside of the coal feed pipe early.

〔課題を解決するための手段〕[Means for solving the problem]

上記した従来技術の問題点は、固体原料を粉砕する粉
砕部と、粉砕されるべき固体原料を上記粉砕部へ供給す
る原料供給管と、粉砕された原料の微粒粉を外部へ搬送
する排出部とを備えた粉砕装置において、上記原料供給
管の管壁に開口した空気孔と、該原料供給管の外部に設
けられた、上記空気孔を包囲する空気室と、この空気室
に空気を供給する空気管路と、空気管路を介して空気室
に供給する空気量および、または空気圧により前記原料
供給管の閉塞状況を検知する閉塞検知装置とを設けたこ
とを特徴とする粉砕装置により解決される。
The above-mentioned problems of the prior art include a pulverizing unit for pulverizing a solid raw material, a raw material supply pipe for supplying the solid raw material to be pulverized to the pulverizing unit, and a discharge unit for conveying the fine powder of the pulverized raw material to the outside. In the pulverizing device provided with: an air hole opened in the tube wall of the raw material supply pipe, an air chamber provided outside the raw material supply pipe and surrounding the air hole, and supplying air to the air chamber. A pulverizing device, comprising: an air line to be closed; and a blockage detection device that detects a blockage state of the raw material supply tube by an amount of air supplied to the air chamber through the air line and / or air pressure. Is done.

〔実施例〕〔Example〕

本発明の具体的な実施例を図に基づいて説明する。第
1図は、本発明の付着検知装置付給炭管を備えた粉砕装
置の側面図である。第2図、第3図は、検知装置部の拡
大詳細図である。
A specific embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a side view of a pulverizing apparatus provided with a coal feeding pipe with an adhesion detecting device according to the present invention. 2 and 3 are enlarged detailed views of the detection device.

第1図、第2図において、微粉炭機1には上部粉砕リ
ング6と下部粉砕リング5、粉砕ボール7および給炭管
2を有し、石炭は給炭管2から供給され、粉砕ボール7
により粉砕される。粉砕された石炭10は下部リング5の
下側の空気室から送入される乾燥および搬送用の熱風に
より乾燥分級され、細粉は80℃前後の温度で粉砕機上部
に設けられた分級器9によりさらに微粉10cおよび細粉1
0dに分級され、微粉10cはバーナへ、細粉10dはシュート
25を通って再び下部リング5の中央部へ戻り再粉砕され
る。付着検知装置は給炭管2の外側に設けられる。また
検知装置には、エアチャンバ(空気室)13、空気管14、
圧力計15、圧力調整弁16、接点付流量計17および給炭管
2の管壁周囲に複数の空気孔18が設けられる。
1 and 2, the pulverized coal machine 1 has an upper crushing ring 6, a lower crushing ring 5, a crushing ball 7, and a coal supply pipe 2. Coal is supplied from the coal supply pipe 2, and
Crushed. The pulverized coal 10 is dried and classified by hot air for drying and transporting from an air chamber below the lower ring 5, and the fine powder is classified at a temperature of about 80 ° C. in a classifier 9 provided at the upper part of the pulverizer. Further fine powder 10c and fine powder 1
Classified as 0d, fine powder 10c goes to burner, fine powder 10d shoots
After passing through 25 again, it returns to the center of the lower ring 5 and is crushed again. The adhesion detecting device is provided outside the coal feed pipe 2. The detection device includes an air chamber (air chamber) 13, an air pipe 14,
A plurality of air holes 18 are provided around the pipe wall of the pressure gauge 15, the pressure regulating valve 16, the flow meter 17 with a contact point, and the coal feed pipe 2.

付着検知装置に送られる空気は、空気孔18を通って微
粉炭機内へ送入される。微粉炭機1の内部圧力は、微粉
炭機1からバーナまでの通気抵抗のみであり、ほぼ一定
圧力である。空気量は従って正常運転状態においては一
定量が微粉炭機内部へ流入するが、給炭管の内部に石炭
の微粉が付着して空気口の数個所が塞がれることにより
流量が変化するため、給炭管の内部閉塞に到る前に付着
を検知することが可能である。
The air sent to the adhesion detecting device is sent into the pulverized coal machine through the air holes 18. The internal pressure of the pulverized coal machine 1 is only a ventilation resistance from the pulverized coal machine 1 to the burner, and is a substantially constant pressure. Therefore, a certain amount of air flows into the pulverizer during normal operation, but the flow rate changes due to coal fines adhering to the inside of the coal supply pipe and blocking several places of the air port. Further, it is possible to detect the adhesion before reaching the internal blockage of the coal feed pipe.

したがって、付着検知により早期に清掃装置、例えば
パイプクリーナ等により給炭管内部を清掃することによ
り、連続して安定した運転が可能である。
Accordingly, by continuously cleaning the inside of the coal feed pipe with a cleaning device, for example, a pipe cleaner or the like at an early stage by detecting the adhesion, continuous stable operation is possible.

第3図は、第1図におけるI−I線断面視図であり、
給炭管2の管壁周囲に空気孔が設けられている状況を示
す。なお、給炭管内面に微粉炭が付着して空気孔が閉塞
されると、空気管14の圧力が上昇するので、圧力計15の
指示圧力の変化により閉塞を検出することができる。な
お、閉塞は給炭管の下端部付近から発生し始めるので、
閉塞検知用空気孔は給炭管下方部位に設けるのが望まし
い。
FIG. 3 is a sectional view taken along line II in FIG.
The situation where an air hole is provided around the pipe wall of the coal feed pipe 2 is shown. If the pulverized coal adheres to the inner surface of the coal feed pipe and the air hole is closed, the pressure of the air pipe 14 increases. Therefore, the change in the pressure indicated by the pressure gauge 15 can detect the blockage. Since the blockage starts to occur near the lower end of the coal feed pipe,
The air hole for detecting blockage is desirably provided in a lower portion of the coal feed pipe.

〔発明の効果〕〔The invention's effect〕

本発明によれば、原料供給管内部に原料が付着し始め
た時点で、その付着を検知できるので、上記供給管が詰
まる前の段階で早期に対応策を実施できる効果がある。
According to the present invention, when the raw material starts to adhere to the inside of the raw material supply pipe, the adhesion can be detected, so that there is an effect that a countermeasure can be taken at an early stage before the supply pipe is clogged.

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

第1図は、本発明の実施になる給炭管閉塞検出装置を備
えた粉砕装置を示す側面図、第2図は、第1図の検出装
置の部分拡大図、第3図は、第1図のI−I線断面視
図、第4図は、従来技術による粉砕装置の側面図であ
る。 1……微粉炭機、2……給炭管、5……下部粉砕リン
グ、6……上部粉砕リング、7……粉砕ボール、9……
分級器、10……原料石炭、13……空気室、14……空気
管、15……圧力計、16……圧力調整弁、17……接点付流
量計、18……空気孔。
FIG. 1 is a side view showing a pulverizing device provided with a coal feed pipe blockage detecting device according to the present invention, FIG. 2 is a partially enlarged view of the detecting device of FIG. 1, and FIG. FIG. 4 is a side view of a conventional crushing apparatus, taken along a line II in FIG. 1 ... pulverized coal machine, 2 ... coal feed pipe, 5 ... lower crushing ring, 6 ... upper crushing ring, 7 ... crushing ball, 9 ...
Classifier, 10: Coal raw material, 13: Air chamber, 14: Air tube, 15: Pressure gauge, 16: Pressure regulating valve, 17: Flow meter with contacts, 18: Air hole.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】固体原料を粉砕する粉砕部と、粉砕される
べき固体原料を上記粉砕部へ供給する原料供給管と、粉
砕された原料の微粒粉を外部へ搬送する排出部とを備え
た粉砕装置において、上記原料供給管の管壁に開口した
空気孔と、該原料供給管の外部に設けられた、上記空気
孔を包囲する空気室と、この空気室に空気を供給する空
気管路と、空気管路を介して空気室に供給する空気量お
よび、または空気圧により前記原料供給管の閉塞状況を
検知する閉塞検知装置とを設けたことを特徴とする粉砕
装置。
A crushing section for crushing the solid raw material, a raw material supply pipe for supplying the solid raw material to be crushed to the crushing section, and a discharge section for conveying fine powder of the crushed raw material to the outside. In the pulverizer, an air hole opened in a tube wall of the raw material supply pipe, an air chamber provided outside the raw material supply pipe and surrounding the air hole, and an air pipe for supplying air to the air chamber A pulverization device comprising: a blockage detection device configured to detect a blockage state of the raw material supply pipe based on an amount of air supplied to an air chamber via an air pipe and / or air pressure.
JP11886088A 1988-05-16 1988-05-16 Crusher Expired - Lifetime JP2655875B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11886088A JP2655875B2 (en) 1988-05-16 1988-05-16 Crusher

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11886088A JP2655875B2 (en) 1988-05-16 1988-05-16 Crusher

Publications (2)

Publication Number Publication Date
JPH01288348A JPH01288348A (en) 1989-11-20
JP2655875B2 true JP2655875B2 (en) 1997-09-24

Family

ID=14746927

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11886088A Expired - Lifetime JP2655875B2 (en) 1988-05-16 1988-05-16 Crusher

Country Status (1)

Country Link
JP (1) JP2655875B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109465073A (en) * 2018-10-18 2019-03-15 安徽国润电力检修工程有限责任公司 A kind of wet ball mill of blanking smoothness

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002143714A (en) * 2000-11-10 2002-05-21 Babcock Hitachi Kk Monitoring device for operating state of pulverizer
JP5504629B2 (en) * 2009-01-05 2014-05-28 株式会社リコー Airflow type pulverization classification device
JP6345580B2 (en) * 2014-11-28 2018-06-20 三菱日立パワーシステムズ株式会社 Solid fuel pulverizer and control method thereof
JP7348778B2 (en) * 2019-09-04 2023-09-21 川崎重工業株式会社 Vertical roller mill

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109465073A (en) * 2018-10-18 2019-03-15 安徽国润电力检修工程有限责任公司 A kind of wet ball mill of blanking smoothness

Also Published As

Publication number Publication date
JPH01288348A (en) 1989-11-20

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