JPH022042B2 - - Google Patents

Info

Publication number
JPH022042B2
JPH022042B2 JP56049420A JP4942081A JPH022042B2 JP H022042 B2 JPH022042 B2 JP H022042B2 JP 56049420 A JP56049420 A JP 56049420A JP 4942081 A JP4942081 A JP 4942081A JP H022042 B2 JPH022042 B2 JP H022042B2
Authority
JP
Japan
Prior art keywords
ash
hopper
furnace
slope
recirculated
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
JP56049420A
Other languages
Japanese (ja)
Other versions
JPS57164216A (en
Inventor
Masanori Funakura
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 JP56049420A priority Critical patent/JPS57164216A/en
Publication of JPS57164216A publication Critical patent/JPS57164216A/en
Publication of JPH022042B2 publication Critical patent/JPH022042B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J1/00Removing ash, clinker, or slag from combustion chambers
    • F23J1/08Liquid slag removal

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Air Transport Of Granular Materials (AREA)

Description

【発明の詳細な説明】 この発明はボイラ火炉底部を構成するホツパ部
の灰付着を防止した火炉の構造に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a furnace structure that prevents ash from adhering to a hopper portion constituting the bottom of a boiler furnace.

石炭燃焼ボイラは重油燃焼ボイラに比較して多
量の灰分が排出されるが、火炉底部においてはこ
れら灰分は炉内の高熱により溶融し下方へと流下
する。第1図は灰分の除去方法の一例を示す。図
において、灰分は火炉1の高熱により溶融しホツ
パ部3を伝つて流下し、アツシユホツパ4に流入
して冷却させた後外部に排出される。この形式の
ボイラは溶融灰(スラツグ)を自重により流下さ
れるものであるため、灰の排出を良好に行うため
にはホツパ部3を急傾斜構造とせねばならず、こ
のためボイラ全体は大型かつ大重量化する。しか
し灰の性状によつては相当に粘性の高いものもあ
り、このような灰の場合にはホツパ部を急傾斜構
造とするのみでは対応し切れず灰の付着によるア
ツシユホツパ4の閉塞、ホツパ部3を形成する水
管の受熱量の低下等の問題を生ずる。
Coal-fired boilers emit a larger amount of ash than heavy oil-fired boilers, but at the bottom of the furnace, these ash melt due to the high heat inside the furnace and flow downward. FIG. 1 shows an example of a method for removing ash. In the figure, ash is melted by the high heat of the furnace 1, flows down through the hopper section 3, flows into the ash hopper 4, is cooled, and then discharged to the outside. Since this type of boiler allows molten ash (slug) to flow down under its own weight, the hopper section 3 must have a steeply sloping structure in order to properly discharge the ash. Increases weight. However, depending on the nature of the ash, some ash is quite viscous, and in the case of such ash, simply making the hopper part with a steep slope structure is not enough to deal with it, and the ash adhesion may cause the ash hopper 4 to become clogged, or the hopper part to become clogged. This causes problems such as a decrease in the amount of heat received by the water pipes forming part 3.

この発明は上述した問題点を除去し、ホツパ部
を急傾斜に形成することなく灰分の除去を良好に
行うことのできるホツパを提供することにある。
The object of the present invention is to eliminate the above-mentioned problems and to provide a hopper that can remove ash content well without forming the hopper part with a steep slope.

要するにこの発明は側部にバーナを有する火炉
の炉底部にホツパーを設け、このホツパーの斜面
に軸心を平行かつ近接して前記火炉より送出され
る燃焼排ガスの一部を再循環供給し溶融スラツグ
の排出を促進する圧力気体噴出用ノズルを一以上
前記斜面に夫々設けた灰分除去手段を有する火炉
であることを特徴とする。
In short, this invention provides a hopper at the bottom of a furnace having a burner on the side, and the axis of the hopper is parallel to and close to the slope of the hopper, and a part of the combustion exhaust gas sent out from the furnace is recirculated and supplied to the molten slag. The furnace is characterized in that it has ash removal means in which one or more nozzles for ejecting pressurized gas are provided on each of the slopes to promote the discharge of ash.

以下この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 below with reference to the drawings.

第2図において、ボイラ本体10の底部にはホ
ツパ部3が形成してある。火炉1を形成する側壁
とホツパ部3との接続部、つまりホツパ部を形成
する斜面の上端部には圧力気体噴出用ノズル5を
形成し、ボイラ本体から排出された燃焼ガスを再
循環排ガスGとして供給しホツパ部3の斜面に沿
つて吹き下ろし、斜面に付着した灰分12の流下
を促進させる。斜面を流下した灰分はアツシユホ
ツパ4に至り冷却される。なお符号2はバーナ側
部に設けたバーナを示す。この実施例においては
灰分付着防止用として再循環ガスを使用するため
排ガス中の窒素酸化物(NOx)濃度を低減する
効果も期待できる。なお、再循環ガスを火炉内に
供給することは知られている。火炉での熱吸収の
調整による過熱蒸気温度制御、時に低負荷の場合
にその効果は大きい。加えて再循環排ガスの供給
は負荷の変化に関係なく定量の供給ですむもので
ある。
In FIG. 2, a hopper section 3 is formed at the bottom of the boiler body 10. A pressure gas injection nozzle 5 is formed at the connection between the side wall forming the furnace 1 and the hopper part 3, that is, at the upper end of the slope forming the hopper part, and the combustion gas discharged from the boiler body is recirculated as exhaust gas G. The ash is supplied as ash and blown down along the slope of the hopper section 3 to promote the flow of the ash 12 adhering to the slope. The ash flowing down the slope reaches the ash hopper 4 and is cooled. In addition, the code|symbol 2 shows the burner provided in the burner side part. In this embodiment, since recirculated gas is used to prevent ash adhesion, the effect of reducing the concentration of nitrogen oxides (NOx) in the exhaust gas can be expected. Note that it is known to supply recirculated gas into the furnace. Superheated steam temperature control by adjusting heat absorption in the furnace is sometimes very effective at low loads. In addition, the recirculated exhaust gas can be supplied at a constant rate regardless of changes in load.

この発明を実施することによりホツパ部に対す
る灰の付着を効果的に防止でき、かつホツパ傾斜
角度を緩くできるのでボイラ全体を小型かつ軽量
に形成でき、しかも過熱蒸気温度の保持、低
Nox排ガスの効果も奏する。
By carrying out this invention, it is possible to effectively prevent ash from adhering to the hopper, and the hopper inclination angle can be made gentler, making it possible to make the entire boiler compact and lightweight.
It also has the effect of reducing Nox exhaust gas.

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

第1図は従来の灰付着防止方法を示すホツパ部
の断面図、第2図はこの発明に係る方法を実施す
るためのボイラホツパ部を示す断面図である。 3……ホツパ部、4……アツシユホツパ、10
……ボイラ本体、12……灰分(スラツグ)、G
……再循環排ガス、A……高圧空気。
FIG. 1 is a sectional view of a hopper section showing a conventional method for preventing ash adhesion, and FIG. 2 is a sectional view of a boiler hopper section for implementing the method according to the present invention. 3... Hotsupa part, 4... Atsushi hopsupa, 10
... Boiler body, 12 ... Ash content (slug), G
...Recirculated exhaust gas, A...High pressure air.

Claims (1)

【特許請求の範囲】[Claims] 1 側部にバーナを有する火炉の炉底部にホツパ
ーを設け、このホツパーの斜面に軸心を平行かつ
近接して前記火炉より送出される燃焼排ガスの一
部を再循環供給し溶融スラツグの排出を促進する
圧力気体噴出用ノズルを一以上前記斜面に夫々設
けたことを特徴とする灰分除去手段を有する火
炉。
1 A hopper is provided at the bottom of a furnace having a burner on the side, and a part of the combustion exhaust gas sent out from the furnace is recirculated and supplied with the axis parallel to and close to the slope of the hopper to discharge molten slag. A furnace having ash removal means, characterized in that one or more nozzles for ejecting pressurized gas are provided on each of the slopes.
JP56049420A 1981-04-03 1981-04-03 Removing method for ash by hopper Granted JPS57164216A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56049420A JPS57164216A (en) 1981-04-03 1981-04-03 Removing method for ash by hopper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56049420A JPS57164216A (en) 1981-04-03 1981-04-03 Removing method for ash by hopper

Publications (2)

Publication Number Publication Date
JPS57164216A JPS57164216A (en) 1982-10-08
JPH022042B2 true JPH022042B2 (en) 1990-01-16

Family

ID=12830577

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56049420A Granted JPS57164216A (en) 1981-04-03 1981-04-03 Removing method for ash by hopper

Country Status (1)

Country Link
JP (1) JPS57164216A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61168718A (en) * 1985-01-18 1986-07-30 Central Res Inst Of Electric Power Ind Slag-tap furnace
JPS6391414A (en) * 1986-10-02 1988-04-22 Kawasaki Heavy Ind Ltd Coal combustion apparatus and method of using the same
US7731411B2 (en) * 2005-04-04 2010-06-08 Schlumberger Technology Corporation Circulating fluid system for powder fluidization and method of performing same
JP6022270B2 (en) * 2012-09-10 2016-11-09 住友重機械工業株式会社 Exhaust gas equipment
JP6129372B1 (en) * 2016-02-27 2017-05-17 三久股ふん有限公司 Automatic ash discharge device

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5316632A (en) * 1976-07-01 1978-02-15 Iwatsu Electric Co Ltd Dry developing method for electrophotography
JPS5534144U (en) * 1978-08-25 1980-03-05
CH640336A5 (en) * 1979-03-29 1983-12-30 Von Roll Ag Method for the melting of slag from an incineration plant, in particular a refuse incineration plant, with grate firing and melt chamber firing for carrying out the method

Also Published As

Publication number Publication date
JPS57164216A (en) 1982-10-08

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