JP2523646B2 - Clinker ash transportation system - Google Patents

Clinker ash transportation system

Info

Publication number
JP2523646B2
JP2523646B2 JP62147093A JP14709387A JP2523646B2 JP 2523646 B2 JP2523646 B2 JP 2523646B2 JP 62147093 A JP62147093 A JP 62147093A JP 14709387 A JP14709387 A JP 14709387A JP 2523646 B2 JP2523646 B2 JP 2523646B2
Authority
JP
Japan
Prior art keywords
clinker
ash
conveyor
silo
transportation system
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 - Fee Related
Application number
JP62147093A
Other languages
Japanese (ja)
Other versions
JPS63311016A (en
Inventor
健一 武藤
隆 富井
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 JP62147093A priority Critical patent/JP2523646B2/en
Publication of JPS63311016A publication Critical patent/JPS63311016A/en
Application granted granted Critical
Publication of JP2523646B2 publication Critical patent/JP2523646B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は微粉炭焚ボイラに係り、特にボトムクリンカ
灰の含水率の調整と輸送効率改善に好適な輸送システム
に関する。
Description: TECHNICAL FIELD The present invention relates to a pulverized coal burning boiler, and more particularly to a transportation system suitable for adjusting the water content of bottom clinker ash and improving transportation efficiency.

(従来の技術) 従来、微粉炭焚ボイラにおいては火炉内において燃焼
により発生するクリンカ及び灰は、火炉底部に降下堆積
し、水封式クリンカコンベアにより排出されるが、この
際、10mm内外の大きい粒度のものを含むクリンカ灰の水
きりは重力に依存しており、火炉底部に配置された水封
構造のクリンカホッパと、その内部に構成されたクリン
カコンベアによって外部へ排出される。通常このクリン
カコンベアは水封構造を有する部分にのみ設置されるた
め、クリンカサイロまでのクリンカ輸送については別の
サイロコンベアによりサイロ上部まで輸送されている。
(Prior Art) Conventionally, in a pulverized coal burning boiler, clinker and ash generated by combustion in the furnace descend and accumulate at the bottom of the furnace and are discharged by a water-sealed clinker conveyor. Draining of clinker ash including particles of particle size is dependent on gravity, and is discharged to the outside by a clinker hopper having a water-sealed structure arranged at the bottom of the furnace and a clinker conveyor configured inside. Normally, this clinker conveyor is installed only in a portion having a water-sealing structure, and therefore, for transporting the clinker to the clinker silo, it is transported to the upper part of the silo by another silo conveyor.

しかし最近の技術進歩により、微粉炭粉砕装置の性能
が改善された結果、微粉炭の粒度が向上しこれに伴い燃
焼灰も微細になった。併せて窒素酸化物低減対策のため
に、火炉の断面積も大きくとる傾向にあり、火炉内での
燃焼ガスの上昇スピードが低下するなどの原因で、火炉
底部に配置されたクリンカホッパには細かいクリンカ灰
が落下る傾向にあった。このため水封部からクリンカコ
ンベアによって排出される灰に随伴する水分量も増加す
る傾向があった。
However, due to the recent technological progress, the performance of the pulverized coal pulverizer has been improved, and as a result, the particle size of the pulverized coal has been improved and the combustion ash has become finer accordingly. At the same time, as a measure to reduce nitrogen oxides, the cross-sectional area of the furnace tends to be large, and the rising speed of the combustion gas in the furnace slows down.Therefore, the clinker hopper arranged at the bottom of the furnace has a small size. Clinker ash tended to fall. Therefore, the amount of water associated with the ash discharged from the water sealing section by the clinker conveyor also tends to increase.

(発明が解決しようとする問題点) ボトムアッシュはクリンカコンベア出口において含水
率が50%〜55%の範囲にあるが、含水率の高くなったク
リンカ灰は、その輸送効率が極端に低下すると共にこれ
がサイロ内に堆積貯蔵されることにより、含水率が41〜
45%以上になると水分だけが分離してサイロの上部に表
面水として停溜する。この表面水は、クリンカサイロか
らトラックへの排出時などに突然落下する不具合があっ
た。またコンベアの構造を水きりの良い構造とした場合
にも、灰の輸送効率は低下するという問題点があった。
本発明は上記問題点を解決し、ボトムクリンカ灰を効率
良く輸送するシステムを提供することを目的としてい
る。
(Problems to be solved by the invention) Although the bottom ash has a water content in the range of 50% to 55% at the clinker conveyor outlet, the clinker ash with a high water content has an extremely low transportation efficiency. By storing this in a silo, the water content of 41 ~
When it exceeds 45%, only water separates and stays at the top of the silo as surface water. This surface water had a problem that it suddenly dropped when it was discharged from the clinker silo to a truck. Further, even when the structure of the conveyor is well drained, there is a problem that the ash transportation efficiency is lowered.
An object of the present invention is to solve the above problems and provide a system for efficiently transporting bottom clinker ash.

(問題点を解決するための手段) 上記目的は、含水率の高いボトムアッシュに乾燥した
フライアッシュを混入し適当な含水率に調整することに
よって達成される。
(Means for Solving Problems) The above object is achieved by mixing bottom ash having a high water content with dry fly ash to adjust the water content to an appropriate value.

(作用) 含水率が高く比較的粒度の大きいクリンカに、乾燥し
た細かいフライアッシュを混入することでクリンカ灰は
細密充填の状態となって均一で適当な含水率を保持する
ことができる。
(Function) By mixing dry fine fly ash into a clinker having a high water content and a relatively large particle size, the clinker ash is in a densely packed state and can maintain a uniform and appropriate water content.

(実施例) 本発明の一実施例を図面と共に説明する。第1図にお
いて、1はクリンカホッパ、2はクリンカコンベア、3
はロータリバルブ、4はフライアッシュシュート、5は
サイロコンベア、6はクリンカサイロ、7は油圧ゲー
ト、8は微粉炭バーナ、9は火炉、10はフライアッシュ
ホッパ、11は煙突である。火炉9内において燃焼により
発生したクリンカ及び灰は火炉9底部に降下堆積し、水
封式クリンカコンベア2により火炉9外に搬送され、こ
こで図示しない集塵器等の捕集手段によって捕集された
フライアッシュは、フライアッシュホッパ10からフライ
アッシュシュート4を経て所定量サイロコンベア5に投
入され、細粒と粗粒とが均一に混合される。上記のよう
に含水率が高く10mm内外の大きい粒度のものを含むクリ
ンカ灰に、乾燥した200メッシュ内外の細かいフライア
ッシュを程よく混合することでクリンカ灰は均一で適当
な含水率を有するいわゆる水持ちの良い細密充填状態に
調整され、クリンカコンベア5を経由してクリンカサイ
ロ6の上部へ順次堆積される。従ってこのような均一で
適当な含水率に調整された細密充填の状態にあるクリン
カは表面水を発生させない。上記捕集手段及びフライア
ッシュとクリンカの混合手段は図示実施例に限定しない
が、クリンカサイロ内で上記のように水持ちの良い細密
充填状態が保持されるように、フライアッシュとクリン
カの混合割合は、クリンカコンベアの走行速度と共に火
炉9内の燃焼条件、炭種等により最適に調整制御され
る。
Embodiment An embodiment of the present invention will be described with reference to the drawings. In FIG. 1, 1 is a clinker hopper, 2 is a clinker conveyor, and 3 is a clinker conveyor.
Is a rotary valve, 4 is a fly ash chute, 5 is a silo conveyor, 6 is a clinker silo, 7 is a hydraulic gate, 8 is a pulverized coal burner, 9 is a furnace, 10 is a fly ash hopper, and 11 is a chimney. The clinker and the ash generated by the combustion in the furnace 9 are deposited on the bottom of the furnace 9 and transported to the outside of the furnace 9 by the water-sealed clinker conveyor 2, where they are collected by a collecting means such as a dust collector (not shown). The fly ash is introduced from the fly ash hopper 10 through the fly ash chute 4 into the silo conveyor 5 in a predetermined amount, and fine particles and coarse particles are uniformly mixed. As mentioned above, clinker ash containing a large water content of 10 mm and a large particle size of 10 mm inside and outside is properly mixed with fine fly ash of 200 mesh inside and outside, so that the clinker ash has a uniform and appropriate water content. It is adjusted to a finely packed state of good quality and is sequentially deposited on the upper part of the clinker silo 6 via the clinker conveyor 5. Therefore, such a clinker in a finely packed state in which the water content is uniform and adjusted to an appropriate water content does not generate surface water. Although the collection means and the fly ash and clinker mixing means are not limited to the illustrated embodiment, the mixing ratio of fly ash and clinker is maintained so that the finely packed state with good water retention is maintained in the clinker silo as described above. Is optimally adjusted and controlled according to the traveling speed of the clinker conveyor, combustion conditions in the furnace 9, coal type, and the like.

(発明の効果) 本発明の実施により、クリンカコンベアの水きり装置
を必要とせず輸送効率が向上し、クリンカ灰の含水率は
概ね41%内外の値に調整されクリンカサイロ内で表面水
を生ずることがなくなった。
(Effect of the invention) By carrying out the present invention, transport efficiency is improved without requiring a water draining device for a clinker conveyor, and the water content of the clinker ash is adjusted to a value of approximately 41% or less to generate surface water in the clinker silo. Is gone.

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

第1図は本発明に係るクリンカ灰輸送システムの一実施
例を示す配置図である。 1……クリンカホッパ、2……クリンカコンベア 3……ロータリバルブ、4……フライアッシュシュート 5……サイロコンベア、6……クリンカサイロ 7……油圧ゲート、8……微粉炭バーナ 9……火炉、10……フライアッシュホッパ 11……煙突
FIG. 1 is a layout showing an embodiment of a clinker ash transportation system according to the present invention. 1 ... Clinker hopper, 2 ... Clinker conveyor 3 ... Rotary valve, 4 ... Fly ash chute 5 ... Silo conveyor, 6 ... Clinker silo 7 ... Hydraulic gate, 8 ... Pulverized coal burner 9 ... Furnace , 10 …… Fly ash hopper 11 …… Chimney

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】微粉炭焚ボイラ火炉の底部に配設された水
封構造のクリンカホッパと、このクリンカホッパ内に構
成されたクリンカコンベアと、このクリンカコンベアの
終端部からクリンカサイロへ架設したサイロコンベアを
有するクリンカ灰輸送システムにおいて、フライアッシ
ュ捕集手段から前記サイロコンベアの始動部にフライア
ッシュを投入混合させる手段と、前記混合によるクリン
カ灰の含水率を調整する手段を備えることを特徴とする
クリンカ灰輸送システム。
1. A clinker hopper having a water-sealed structure arranged at the bottom of a pulverized coal burning boiler furnace, a clinker conveyor configured in the clinker hopper, and a silo installed from a terminal end of the clinker conveyor to a clinker silo. A clinker ash transportation system having a conveyor, characterized by comprising means for introducing and mixing fly ash from a fly ash collecting means into a starting portion of the silo conveyor, and means for adjusting the water content of the clinker ash by the mixing. Clinker ash transportation system.
JP62147093A 1987-06-15 1987-06-15 Clinker ash transportation system Expired - Fee Related JP2523646B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62147093A JP2523646B2 (en) 1987-06-15 1987-06-15 Clinker ash transportation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62147093A JP2523646B2 (en) 1987-06-15 1987-06-15 Clinker ash transportation system

Publications (2)

Publication Number Publication Date
JPS63311016A JPS63311016A (en) 1988-12-19
JP2523646B2 true JP2523646B2 (en) 1996-08-14

Family

ID=15422317

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62147093A Expired - Fee Related JP2523646B2 (en) 1987-06-15 1987-06-15 Clinker ash transportation system

Country Status (1)

Country Link
JP (1) JP2523646B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20120091171A (en) 2009-10-02 2012-08-17 에누오케 가부시키가이샤 Seal device

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1188247B (en) * 1986-01-10 1988-01-07 Magaldi Mario PROCEDURE AND EQUIPMENT FOR THE CONTINUOUS DRY EXTRACTION OF HEAVY ASH
IT1241408B (en) * 1990-03-02 1994-01-14 Mario Magaldi HEAVY ASH DISCHARGE SYSTEM FROM BOILERS FOR STEAM PRODUCTION

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20120091171A (en) 2009-10-02 2012-08-17 에누오케 가부시키가이샤 Seal device

Also Published As

Publication number Publication date
JPS63311016A (en) 1988-12-19

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