JP2001056104A - Oxygen combustion once-through boiler - Google Patents

Oxygen combustion once-through boiler

Info

Publication number
JP2001056104A
JP2001056104A JP11230099A JP23009999A JP2001056104A JP 2001056104 A JP2001056104 A JP 2001056104A JP 11230099 A JP11230099 A JP 11230099A JP 23009999 A JP23009999 A JP 23009999A JP 2001056104 A JP2001056104 A JP 2001056104A
Authority
JP
Japan
Prior art keywords
boiler
combustion chamber
burner
combustion
once
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.)
Pending
Application number
JP11230099A
Other languages
Japanese (ja)
Inventor
Hiroaki Imatani
今谷浩昭
Ikuo Ishizuka
石塚郁夫
Masashige Kinoshita
木下正成
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.)
JAPAN SOC OF IND MACHINERY MAN
JAPAN SOCIETY OF INDUSTRIAL MACHINERY MANUFACTURERS
Original Assignee
JAPAN SOC OF IND MACHINERY MAN
JAPAN SOCIETY OF INDUSTRIAL MACHINERY MANUFACTURERS
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 JAPAN SOC OF IND MACHINERY MAN, JAPAN SOCIETY OF INDUSTRIAL MACHINERY MANUFACTURERS filed Critical JAPAN SOC OF IND MACHINERY MAN
Priority to JP11230099A priority Critical patent/JP2001056104A/en
Publication of JP2001056104A publication Critical patent/JP2001056104A/en
Pending legal-status Critical Current

Links

Classifications

    • Y02E20/344

Landscapes

  • Air Supply (AREA)

Abstract

PROBLEM TO BE SOLVED: To facilitate heat absorption in a combustion chamber by a burner mounting method and the like, and simultaneously stabilize a water level and simplify a water level control system, and ensure the reasonable design for the combustion chamber. SOLUTION: An oxygen combustion once-through boiler is provided, in which a combustion chamber of a once-through boiler is constructed into a longitudinal cylindrical shape, and a burner 2 is installed below a boiler body by 1/2 to 1/5 of the height thereof. The boiler is disposed with a displacement from the center of the longitudinal cylindrical combustion chamber 1 by 0 to 1/2 of the outer diameter of the cylindrical combustion chamber 1 or by 0-3 times of the burner tip end diameter to form a burner flame tangential along a combustion chamber structure. Hereby, a simple flow pattern found in the prior art is formed to ensure excellent combustion and heat transfer and simple water level control.

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、簡便燃焼室設計及び
簡易な水位制御を可能にする酸素燃焼貫流ボイラーに関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a once-through boiler for oxyfuel combustion, which enables simple combustion chamber design and simple water level control.

【0002】[0002]

【従来の技術】 従来の縦形円筒形燃焼室を有する貫流
ボイラーは、バーナを本体上部中央に設置し燃焼させて
いた。しかし、この燃焼方法では、燃焼室内における火
炎及び燃焼ガスのフローパタ−ンが複雑となり、かつ、
火炉負荷(伝熱面熱負荷)の分布が不均一になるため、
複雑な燃焼室設計が必要であった。また、上記従来のボ
イラーの構造ではボイラー水の流動方向と火炎温度、若
しくは、火炉負荷(伝熱面熱負荷)の高低方向とが逆に
なるため、水管内のボイラー水の流動が不安定となり、
ボイラーの水位制御が複雑化するという問題点があっ
た。
2. Description of the Related Art In a conventional once-through boiler having a vertical cylindrical combustion chamber, a burner is installed at the center of an upper portion of a main body and burns. However, in this combustion method, the flow pattern of the flame and the combustion gas in the combustion chamber becomes complicated, and
Since the distribution of furnace load (heat transfer surface heat load) becomes uneven,
Complex combustion chamber design was required. In addition, in the above-described conventional boiler structure, the flow direction of the boiler water and the direction of the flame temperature or the height of the furnace load (heat transfer surface heat load) are reversed, so that the flow of the boiler water in the water pipe becomes unstable. ,
There was a problem that boiler water level control became complicated.

【0003】[0003]

【発明が解決しようとする課題】 本発明は、上記従来
の縦形円筒形燃焼室を有する貫流ボイラーの前記のよう
な問題点を解決して、良好な燃焼と伝熱とを確保するこ
とによって、従来にはない新規にして、簡便な燃焼室設
計と簡易な水位制御とを実現することを目的とするもの
である。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems of the once-through boiler having the conventional vertical cylindrical combustion chamber, and secures good combustion and heat transfer. An object of the present invention is to realize a new and simple combustion chamber design and a simple water level control, which are new in the related art.

【0004】[0004]

【課題を解決するための手段】 上記の目的を達成する
ために本発明の第1は、酸素燃焼貫流ボイラーの水管を
円周方向に円筒形状を形成する様に設置し、水管と水管
の間は帯鋼により溶接、水管上部に蒸気ヘッダーと下部
に水室ヘッダーとを設けることにより、メンブレン構造
の縦型円筒形燃焼室を形成し、その燃焼室の側面にバー
ナを設置、バーナ設置部には水管を設けず、縦型円筒形
燃焼室に対して水平方向に火炎を形成させ、バーナ設置
位置近傍に設けた燃焼ガス出口部より燃焼ガスを水管群
内に流入させることを特徴とする。本発明の第2は、上
記縦型円筒形燃焼室に、バーナをボイラー本体高さの2
〜5分の1下部に設置することを特徴とする。本発明の
第3は、バーナを上記縦形円筒形燃焼室の中心より円筒
形燃焼室外径の0〜2分の1、若しくは、バーナ先端径
の0〜3倍中心より偏心させて設置し、燃焼室構造に沿
ったタンジェンシャルなバーナ火炎を形成せしめてなる
ことを特徴とする。本発明の第4は、上記酸素燃焼貫流
ボイラーの構造により、良好な燃焼と伝熱及び簡易な水
位制御を可能ならしめたことを特徴とする請求項1、
2、3、4記載の酸素燃焼貫流ボイラーである。
Means for Solving the Problems In order to achieve the above object, a first aspect of the present invention is to install a water pipe of an oxyfuel combustion once-through boiler so as to form a cylindrical shape in a circumferential direction, and to provide a water pipe between water pipes. By welding with steel strip, providing a steam header at the top of the water pipe and a water chamber header at the bottom, a vertical cylindrical combustion chamber with a membrane structure is formed, a burner is installed on the side of the combustion chamber, and the burner installation part Is characterized by forming a flame in a horizontal direction with respect to a vertical cylindrical combustion chamber without providing a water pipe, and causing combustion gas to flow into a group of water pipes from a combustion gas outlet provided near a burner installation position. The second aspect of the present invention is that a burner is installed in the vertical cylindrical combustion chamber at a height of the boiler main body.
It is characterized in that it is installed at a lower part of about 1/5. The third aspect of the present invention is that the burner is installed eccentrically from the center of the vertical cylindrical combustion chamber to 0 to 1/2 of the outer diameter of the cylindrical combustion chamber or 0 to 3 times the center of the burner tip diameter, and the combustion is performed. It is characterized by forming a tangential burner flame along the chamber structure. A fourth aspect of the present invention is that the structure of the oxyfuel combustion once-through boiler enables good combustion, heat transfer, and simple water level control.
2. An oxygen combustion once-through boiler according to 2, 3, or 4.

【0005】[0005]

【作用】 本発明の酸素燃焼貫流ボイラーは、縦形円筒
形燃焼室にバーナをボイラー本体高さの2〜5分の1下
部にかつ、円筒形燃焼室外形の0〜2分の1、若しく
は、バーナ先端径の0〜3倍中心より偏心させて設置し
ているため、燃焼室内には火炎及び燃焼ガスによるタン
ジェンシャルな流れ場が形成される。燃焼室内に形成さ
れる火炎は酸素燃焼特有の短炎等であるため、火炎が炉
壁に衝突することなく、バーナ取付側半円部分で燃焼反
応を完結し、残りの半円部分で高温ガスを充満させ、バ
ーナ取付口横に設けた火炉出口より水管群内に流入、従
来にないシンプルなフローパターンを形成し、良好な燃
焼と伝熱を可能にする。また、前記により、局部的な伝
熱面の過熱をなくすることが容易となり、ほぼ均一な火
炉負荷(伝熱面熱負荷)が得られる。その結果、バーナ
取付方法等により燃焼室における熱吸収が容易になると
同時に、水位が安定し、水位制御方式が簡略化されると
共に無理のない燃焼室設計が可能となる。
According to the oxyfuel combustion once-through boiler of the present invention, a burner is provided in a vertical cylindrical combustion chamber at a lower portion of one-fifth of the height of the boiler body and at a half of the outer shape of the cylindrical combustion chamber, or Since it is installed eccentrically from the center of 0 to 3 times the burner tip diameter, a tangential flow field by the flame and the combustion gas is formed in the combustion chamber. Since the flame formed in the combustion chamber is a short flame peculiar to oxyfuel combustion, the flame does not collide with the furnace wall, completes the combustion reaction in the semicircle on the burner mounting side, and the high-temperature gas in the remaining semicircle. And flows into the water tube group from the furnace outlet provided at the side of the burner mounting port to form an unprecedented simple flow pattern, enabling good combustion and heat transfer. Further, by the above, it is easy to eliminate local overheating of the heat transfer surface, and a substantially uniform furnace load (heat transfer surface heat load) can be obtained. As a result, heat absorption in the combustion chamber is facilitated by the burner mounting method and the like, and at the same time, the water level is stabilized, the water level control method is simplified, and a reasonable combustion chamber design becomes possible.

【0006】[0006]

【実施例】 添付図面の図1は本発明の酸素燃焼貫流ボ
イラーの側面図である。1は縦形円筒形燃焼室、2はそ
の側面に設置されたバーナ、3は縦型円筒形燃焼室を構
成する水管、4は水管間に設置された帯鋼、5は水管上
部に設けられた蒸気ヘッダー、6は水管下部に設けられ
た水室ヘッダーであり、本構造を持って酸素燃焼貫流ボ
イラーが構成されている。図中H1は本体高さの寸法、
H2は本体中心からバーナ2までの設置高さを示す。本
体高さH1とバーナ設置高さH2との間には次の関係が
成立する。 H2=1/2×H1〜1/5×H1 図2は酸素燃焼貫流ボイラーの平面図であり、W1は円
筒形燃焼室外径、W2はバーナ先端径、W3はバーナの
偏心設置距離を示す。偏心設置距離W3と円筒径W1及
びバーナ先端径W2との間には、次の関係が成立する。 W3=0×W1〜1/2×W1 及び W3=0×W2〜3×W2 図3は酸素燃焼貫流ボイラーの燃焼室内における火炎及
び燃焼ガスのフローパターンを示す。上記の寸法で縦形
円筒形燃焼室にバーナを設置することにより、燃焼室内
には火炎及び燃焼ガスによるタンジェンシャルな流れ場
が形成される。燃焼室内に形成される火炎は、酸素燃焼
特有の短炎等であるため、火炎が炉壁に衝突することな
く、バーナ取付側半円部分で燃焼反応を完結し、残りの
半円部分で高温ガスを充満させ、バーナ取付口横に設け
られた火炉出口より水管群内に流入し、従来にないシン
プルなフローパターンを形成し、良好な燃焼と伝熱を可
能ならしめる。また、上記によって、局部的な伝熱面の
過熱をなくすることが容易となり、ほぼ均一な火炉負荷
(伝熱面熱負荷)が得られる。その結果、バーナ取付方
法等により燃焼室における熱吸収が容易になると同時
に、水位が安定し水位制御方式が簡略化されると共に、
無理のない燃焼室設計が可能となる利点がある。
FIG. 1 of the accompanying drawings is a side view of an oxygen-fired once-through boiler of the present invention. 1 is a vertical cylindrical combustion chamber, 2 is a burner installed on its side, 3 is a water pipe constituting the vertical cylindrical combustion chamber, 4 is a steel strip installed between the water pipes, and 5 is provided on the upper part of the water pipe. The steam header 6 is a water chamber header provided at the lower part of the water pipe, and has an oxygen combustion once-through boiler having this structure. In the figure, H1 is the height of the main body,
H2 indicates the installation height from the center of the main body to the burner 2. The following relationship is established between the main body height H1 and the burner installation height H2. H2 = 1/2 × H11 / 1/5 × H1 FIG. 2 is a plan view of the oxyfuel combustion once-through boiler, where W1 is the outer diameter of the cylindrical combustion chamber, W2 is the burner tip diameter, and W3 is the eccentric installation distance of the burner. The following relationship is established between the eccentric installation distance W3, the cylindrical diameter W1, and the burner tip diameter W2. W3 = 0 × W11〜1 / 2 × W1 and W3 = 0 × W2-3 × W2 FIG. 3 shows the flow pattern of the flame and the combustion gas in the combustion chamber of the oxyfuel once-through boiler. By installing a burner in the vertical cylindrical combustion chamber with the above dimensions, a tangential flow field is created in the combustion chamber by the flame and the combustion gas. Since the flame formed in the combustion chamber is a short flame peculiar to oxyfuel combustion, the flame does not collide with the furnace wall, completes the combustion reaction in the semicircle on the burner mounting side, and the high temperature occurs in the remaining semicircle. It is filled with gas and flows into the water pipe group from the furnace outlet provided at the side of the burner mounting port, forming an unprecedented simple flow pattern, enabling good combustion and heat transfer. Further, by the above, it is easy to eliminate local overheating of the heat transfer surface, and a substantially uniform furnace load (heat transfer surface heat load) can be obtained. As a result, the heat absorption in the combustion chamber is facilitated by the burner mounting method and the like, and the water level is stabilized and the water level control method is simplified.
There is an advantage that a reasonable combustion chamber design is possible.

【0007】[0007]

【発明の効果】 本発明の酸素燃焼貫流ボイラーは、縦
形円筒形燃焼室に本設定のバーナをボイラー本体高さの
2〜5分の1下方に、かつ縦形円筒形燃焼室の中心より
円筒形燃焼室外径の0〜2分の1、若しくは、バーナ先
端径の0〜3倍中心より偏心させて設置することによ
り、燃焼室内の火炎及び燃焼ガスのフローパターンがシ
ンプルとなり、良好な燃焼と伝熱が可能となり、その結
果、従来にない簡便な燃焼室設計と簡易な水位制御が可
能になる効果を奏する。
According to the present invention, in the oxyfuel combustion once-through boiler, the burner of this setting is provided in the vertical cylindrical combustion chamber at a height two to one-fifth below the height of the boiler main body and at the center of the vertical cylindrical combustion chamber. By eccentrically installing from the center of the outer diameter of the combustion chamber 0 to 1/2 or 0 to 3 times the center diameter of the burner tip, the flow pattern of the flame and the combustion gas in the combustion chamber is simplified, resulting in good combustion and transmission. Heat is made possible, and as a result, there is an effect that an unprecedentedly simple combustion chamber design and simple water level control become possible.

【0008】[0008]

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

【図1】酸素燃焼貫流ボイラーの側面図である。FIG. 1 is a side view of an oxygen combustion once-through boiler.

【図2】酸素燃焼貫流ボイラーの平面図である。FIG. 2 is a plan view of an oxygen combustion once-through boiler.

【図3】酸素燃焼貫流ボイラーの燃焼室内における火炎
及び燃焼ガスのフローパターンを示すものである。
FIG. 3 shows a flow pattern of a flame and a combustion gas in a combustion chamber of an oxyfuel once-through boiler.

【符号の説明】[Explanation of symbols]

1 縦形円筒形燃焼室 2 縦形円筒形燃焼室の側面に設置されたバーナ 3 縦型円筒形燃焼室を構成する水管 4 水管間に設置された帯鋼 5 水管上部に設けられた蒸気ヘッダー 6 水管下部に設けられた水室ヘッダー Reference Signs List 1 vertical cylindrical combustion chamber 2 burner installed on side of vertical cylindrical combustion chamber 3 water pipe constituting vertical cylindrical combustion chamber 4 steel strip installed between water pipes 5 steam header provided above water pipe 6 water pipe Water chamber header provided at the bottom

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 貫流ボイラーにおいて、水管を円周方向
に円筒形状を形成する様に設置し、水管と水管の間は帯
鋼により溶接、水管上部に蒸気ヘッダーと下部に水室ヘ
ッダーとを設けることにより、メンブレン構造の縦型円
筒形燃焼室を形成し、その燃焼室の側面に酸素燃焼用バ
ーナ(以下バーナ)を設置、バーナ設置部には水管を設
けず、縦型円筒形燃焼室に対して水平方向に火炎を形成
させ、バーナ設置位置近傍に設けた燃焼ガス出口部より
燃焼ガスを水管群内に流入させることを特徴とする、酸
素燃焼貫流ボイラー。
In a once-through boiler, a water pipe is installed so as to form a cylindrical shape in a circumferential direction, a space between the water pipes is welded by a steel strip, a steam header is provided at an upper part of the water pipe, and a water chamber header is provided at a lower part. As a result, a vertical cylindrical combustion chamber with a membrane structure is formed, and a burner for oxyfuel combustion (hereinafter referred to as a burner) is installed on the side of the combustion chamber. An oxyfuel combustion once-through boiler, characterized in that a flame is formed in a horizontal direction, and combustion gas flows into a group of water pipes from a combustion gas outlet provided near a burner installation position.
【請求項2】 縦形円筒形燃焼室に、バーナをボイラー
本体高さの2〜5分の1だけ下部に設置することを特長
とする、請求項1記載の酸素燃焼貫流ボイラー。
2. The once-through boiler for oxyfuel combustion according to claim 1, wherein the burner is installed in the vertical cylindrical combustion chamber at a position lower than one-fifth of the height of the boiler body.
【請求項3】 縦形円筒形燃焼室の中心より円筒形燃焼
室外径の0〜2分の1、若しくは、バーナ先端径の0〜
3倍中心より偏心させて設置し、燃焼室構造に沿ったタ
ンジェンシャルなバーナ火炎を形成させることを特長と
する、請求項1記載の酸素燃焼貫流ボイラー。
3. A combustion chamber having an outer diameter of 0 to 1/2 of the outer diameter of the cylindrical combustion chamber from the center of the vertical cylindrical combustion chamber, or 0 to 0 of the tip diameter of the burner.
2. The once-through boiler for oxyfuel combustion according to claim 1, wherein the boiler is disposed eccentrically from the center of three times to form a tangential burner flame along the combustion chamber structure.
【請求項4】 請求項1〜3記載のボイラー構造と酸素
燃焼特有の短炎等により、火炎が炉壁に衝突することな
く、バーナ取付側半円部分で燃焼反応を完結し、残りの
半円部分で高温ガスを充満させ、バーナ取付口横に設け
た火炉出口より水管群内に流入、従来にないシンプルな
フローパターンを形成し、良好な燃焼と伝熱及び簡易な
水位制御を可能とすることを特徴とする、酸素燃焼貫流
ボイラー。
4. Due to the boiler structure and the short flame peculiar to oxyfuel combustion according to claims 1 to 3, the combustion reaction is completed in the semicircular portion on the burner mounting side without the flame colliding with the furnace wall, and the other half. High-temperature gas is filled in the circle and flows into the water tube group from the furnace outlet provided next to the burner mounting port, forming an unprecedented simple flow pattern, enabling good combustion, heat transfer, and simple water level control. An oxygen-fired once-through boiler, characterized in that:
JP11230099A 1999-08-16 1999-08-16 Oxygen combustion once-through boiler Pending JP2001056104A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11230099A JP2001056104A (en) 1999-08-16 1999-08-16 Oxygen combustion once-through boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11230099A JP2001056104A (en) 1999-08-16 1999-08-16 Oxygen combustion once-through boiler

Publications (1)

Publication Number Publication Date
JP2001056104A true JP2001056104A (en) 2001-02-27

Family

ID=16902548

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11230099A Pending JP2001056104A (en) 1999-08-16 1999-08-16 Oxygen combustion once-through boiler

Country Status (1)

Country Link
JP (1) JP2001056104A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6568185B1 (en) 2001-12-03 2003-05-27 L'air Liquide Societe Anonyme A'directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Combination air separation and steam-generation processes and plants therefore
US6619041B2 (en) 2001-06-29 2003-09-16 L'air Liquide - Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Steam generation apparatus and methods
US6745573B2 (en) 2001-03-23 2004-06-08 American Air Liquide, Inc. Integrated air separation and power generation process

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6745573B2 (en) 2001-03-23 2004-06-08 American Air Liquide, Inc. Integrated air separation and power generation process
US6619041B2 (en) 2001-06-29 2003-09-16 L'air Liquide - Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Steam generation apparatus and methods
US6568185B1 (en) 2001-12-03 2003-05-27 L'air Liquide Societe Anonyme A'directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Combination air separation and steam-generation processes and plants therefore

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