JP2001349502A - Steam generator and vertical water tube boiler - Google Patents

Steam generator and vertical water tube boiler

Info

Publication number
JP2001349502A
JP2001349502A JP2000165596A JP2000165596A JP2001349502A JP 2001349502 A JP2001349502 A JP 2001349502A JP 2000165596 A JP2000165596 A JP 2000165596A JP 2000165596 A JP2000165596 A JP 2000165596A JP 2001349502 A JP2001349502 A JP 2001349502A
Authority
JP
Japan
Prior art keywords
evaporating
flow path
side wall
cylindrical
water tube
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
JP2000165596A
Other languages
Japanese (ja)
Inventor
Akira Mori
朗 森
Toshihiko Tanaka
俊彦 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.)
Takuma Co Ltd
Original Assignee
Takuma Co Ltd
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 Takuma Co Ltd filed Critical Takuma Co Ltd
Priority to JP2000165596A priority Critical patent/JP2001349502A/en
Publication of JP2001349502A publication Critical patent/JP2001349502A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To reduce the manufacturing cost of a steam generator in which a plurality of evaporating pipes 3 vertically arranged with, providing an upper header and a lower header to the top ends and the bottom ends thereof and connecting the top ends to the upper header and the bottom ends to the lower header are arranged along a side wall section 11 or a vertical water tube boiler in which the inside space of the arranged evaporating pipes 3 is constituted as a combustion chamber and, at the same time, to improve the efficiency of heat transfer of the generator or boiler by making use of advantage of the compact constitution of the generator or boiler. SOLUTION: A cylindrical water tube group 4 is formed by arranging the evaporating pipes 3 at narrow intervals along a cylindrical surface formed along the side wall section 11 and the spaces among the adjacent water tubes 3 of the group 4 are formed as radial flow passages 5 through which a heat- source gas is made to flow outward. It is better to constitute the external surfaces of the evaporating pipes 3 facing an outer peripheral flow passage 6 which leads the heat-source gas to an outlet section O along the outer periphery of the water tube group 4 as a contact heat transfer section 9 that promotes contact heat transfer with the heat-source gas.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、上下に上部ヘッダ
と下部ヘッダとを設け、上端部を前記上部ヘッダに接続
し、下端部を前記下部ヘッダに接続して、縦方向に設け
た複数の蒸発管を、上下方向に形成される筒状の側壁部
に沿って配置してある蒸気発生器、及び複数の蒸発管
を、上下方向に形成される円筒状の側壁部に沿って配置
すると共に、前記配列された蒸発管の内側空間を燃焼室
に構成して、前記燃焼室内に向けて火炎を形成する燃焼
器を配置してある竪型水管ボイラに関する。とりわけ、
側壁部に耐火物を施すことなく鉄皮で形成してある小型
の蒸気発生器及び竪型水管ボイラに効果的なものであ
る。
BACKGROUND OF THE INVENTION The present invention relates to a plurality of vertical headers provided with an upper header and a lower header at the top and bottom, an upper end connected to the upper header, and a lower end connected to the lower header. A steam generator in which the evaporating tubes are arranged along a cylindrical side wall formed in a vertical direction, and a plurality of evaporating tubes are arranged along a cylindrical side wall formed in a vertical direction. The present invention relates to a vertical water pipe boiler in which a space inside the arranged evaporating tubes is configured as a combustion chamber and a combustor that forms a flame toward the combustion chamber is disposed. Above all,
The present invention is effective for small steam generators and vertical water tube boilers made of steel without applying refractories to the side walls.

【0002】[0002]

【従来の技術】竪型水管ボイラとしては、例えば特開平
2000−18502号公報や特開平2000−391
01号公報に示されているように、円筒状の缶体の上部
に環状の上部ヘッダを、前記缶体の下部に環状の下部ヘ
ッダを、夫々設け、上端部を前記上部ヘッダに接続し、
下端部を前記下部ヘッダに接続して縦方向に設けた複数
の蒸発管を、円筒状に二列に配置して構成したものを先
に提案した。この構成においては、前記円筒状に配列さ
れた蒸発管の内側空間を燃焼室に構成し、側壁部の一箇
所に排ガス出口を設けてある。そして、円筒面に沿って
配置された蒸発管は、隣接するもの同士の間にフィンプ
レートを溶接して、前記複数の蒸発管からなる円筒状水
管群を形成してある。そして、その内の一部の蒸発管の
間には前記フィンプレートを取り付けず、その間を前記
燃焼室で生成する燃焼ガスの外側に向かう径方向流路と
して形成し、前記内側の環状水管列と前記外側の円筒状
水管群との間を、前記排ガス出口に向かう燃焼ガスの周
方向流路として形成したものである。この竪型水管ボイ
ラにおいては、前記周方向流路で前記燃焼ガスから前記
円筒状水管群への熱伝達をさせるものである。前記径方
向流路は、燃焼室で生成した燃焼ガスを前記周方向流路
に導き、また、その周方向流路から外側の周方向流路に
導くものである。この点は、同様に構成された蒸気発生
器であっても同様である。
2. Description of the Related Art As a vertical water tube boiler, for example, JP-A-2000-18502 and JP-A-2000-391 are known.
As shown in Japanese Patent Publication No. 01, an annular upper header is provided at an upper portion of a cylindrical can body, and an annular lower header is provided at a lower portion of the can body, and an upper end portion is connected to the upper header,
A structure in which a plurality of evaporating tubes having a lower end connected to the lower header and provided in a vertical direction and arranged in two rows in a cylindrical shape has been previously proposed. In this configuration, an inner space of the cylindrically arranged evaporating tubes is configured as a combustion chamber, and an exhaust gas outlet is provided at one location on a side wall portion. The fin plates are welded between adjacent ones of the evaporating tubes arranged along the cylindrical surface to form a group of cylindrical water tubes composed of the plurality of evaporating tubes. Then, the fin plate is not attached between some of the evaporating tubes, and a portion between the evaporating tubes is formed as a radial flow path toward the outside of the combustion gas generated in the combustion chamber. A portion between the outer cylindrical water pipe group and the outer cylindrical water tube group is formed as a circumferential flow path of the combustion gas toward the exhaust gas outlet. In this vertical water tube boiler, heat is transferred from the combustion gas to the cylindrical water tube group in the circumferential flow path. The radial flow path guides the combustion gas generated in the combustion chamber to the circumferential flow path, and guides the combustion gas from the circumferential flow path to an outer circumferential flow path. This point is the same even in a steam generator configured similarly.

【0003】[0003]

【発明が解決しようとする課題】ところで、上記竪型水
管ボイラを含む同様の構成を有する蒸気発生器において
は、熱源ガスが前記円筒状水管群に沿って複数の周方向
流路を経由するものであるから、熱源ガス流が複雑な経
路を通ることになり、燃焼室から排ガス出口に至る熱源
ガスの流路としての燃焼ガス流路の流路抵抗が高くなる
ことを避けられないという問題があった。さらに、上述
のように円筒状水管群を構成する蒸発管の間をフィンプ
レートで接続すれば、その溶接に多大の時間と手間を要
し、簡易構造のものであってもコストが嵩むという問題
を有している。また、二重の円筒状水管群を形成すれ
ば、小径のものであれば、先に内側の円筒状水管群を組
み上げた上で外側の円筒状水管群を組み立てなければな
らないという工程上の制約も生ずる。
By the way, in a steam generator having a similar configuration including the above vertical water tube boiler, a heat source gas passes through a plurality of circumferential flow paths along the cylindrical water tube group. Therefore, the heat source gas flow passes through a complicated path, and the problem that the flow resistance of the combustion gas flow path as the flow path of the heat source gas from the combustion chamber to the exhaust gas outlet cannot be avoided is increased. there were. Furthermore, if the fin plate is used to connect the evaporating tubes constituting the cylindrical water tube group as described above, the welding requires a great deal of time and labor, and the cost is increased even with a simple structure. have. In addition, if a double cylindrical water pipe group is formed, if the diameter is small, the process restriction that the inner cylindrical water pipe group must be assembled first and then the outer cylindrical water pipe group must be assembled. Also occurs.

【0004】上記問題に対処するために、蒸発管列で形
成する円筒状水管群を一重とし、例えば図8に平断面図
を示すように、この円筒状水管群4を構成する蒸発管3
の中の排ガス出口E近傍のものだけを、隣接するもの同
士の間を密接させ、この箇所以外の隣接する蒸発管3の
間隙を燃焼ガスの外方に向けた径方向流路5とし、前記
蒸発管3と側壁部11との間に周方向流路15を形成す
ることが考えられる。しかし、この構成においては、蒸
発管3の間にフィンプレートを溶接しないから、製造コ
ストは低減できたが、径方向流路5を大部分の蒸発管3
の間に形成した結果、前記側壁部11には燃焼ガスの温
度があまり低下しないままに達するため、前記側壁部1
1の温度が上昇してしまうという問題があり、この点に
おいて不満の残るものであった。そこで、図9に示すよ
うに、上記円筒状水管群4を内側と外側に二重に設け
て、前記径方向流路5を通過した燃焼ガスを外側の前記
円筒状水管群で受けさせることも考られるが、前記側壁
部11の温度を高めることはなく、排ガス出口に至る燃
焼ガスの温度は十分に低くなることが期待されるもの
の、上述のコストアップの問題と、排ガス経路の延長に
よって流路抵抗の増大とに問題が残る。そこで、発明者
等は、上記径方向流路の隙間を狭くすることで伝熱効率
が向上する点に着目し、さらなる改良を試みて、本願発
明をなすに至ったのである。
In order to cope with the above problem, the cylindrical water pipe group formed by the evaporating pipe row is made single, and as shown in a plan sectional view of FIG.
Only those in the vicinity of the exhaust gas outlet E are closely contacted between adjacent ones, and the gap between the adjacent evaporating pipes 3 other than this point is defined as a radial flow path 5 directed outward of the combustion gas. It is conceivable to form a circumferential channel 15 between the evaporating tube 3 and the side wall 11. However, in this configuration, since the fin plate is not welded between the evaporating tubes 3, the manufacturing cost can be reduced.
As a result, the temperature of the combustion gas reaches the side wall portion 11 without decreasing so much.
However, there was a problem that the temperature of No. 1 increased, and this point was unsatisfactory. Therefore, as shown in FIG. 9, the cylindrical water pipe group 4 may be provided double inside and outside, and the combustion gas passing through the radial flow path 5 may be received by the outside cylindrical water pipe group. Although it is conceivable that the temperature of the combustion gas reaching the exhaust gas outlet is expected to be sufficiently low without increasing the temperature of the side wall portion 11, the above-described cost increase problem and the extension of the exhaust gas path have Problems remain with the increase in road resistance. Therefore, the inventors have paid attention to the point that the heat transfer efficiency is improved by reducing the gap in the radial flow path, and have attempted further improvement, thereby completing the present invention.

【0005】そこで、本発明に係る蒸気発生器及び竪型
水管ボイラは、コンパクトである竪型水管ボイラの特長
を活かしながら、製造コストを低減し、且つ伝熱効率を
向上できる手段を提供することを目的とする。
[0005] Therefore, the steam generator and the vertical water tube boiler according to the present invention provide means capable of reducing the manufacturing cost and improving the heat transfer efficiency while utilizing the features of the compact vertical water tube boiler. Aim.

【0006】[0006]

【課題を解決するための手段】[Means for Solving the Problems]

【0007】〔本発明の特徴構成〕本発明に係る蒸気発
生器及び竪型水管ボイラは、上下に上部ヘッダと下部ヘ
ッダとを設け、上端部を前記上部ヘッダに接続し、下端
部を前記下部ヘッダに接続して、縦方向に設けた複数の
蒸発管を、上下方向に形成される円筒状の炉壁に沿って
配置し、円筒状水管群を形成してある蒸気発生器、又は
それに加えて、前記円筒状水管群の内側空間を燃焼室に
構成して、前記燃焼室内に向けて火炎を形成する燃焼器
を配置してある竪型水管ボイラにおいて、前記円筒状水
管群を構成する隣接する蒸発管同士の間隙を狭く配置し
てある点に特徴を有するものであり、夫々に以下のよう
な特徴を備えるものである。
The steam generator and the vertical water tube boiler according to the present invention are provided with an upper header and a lower header on the upper and lower sides, an upper end is connected to the upper header, and a lower end is connected to the lower part. Connected to the header, a plurality of vertically provided evaporator tubes are arranged along a cylindrical furnace wall formed in a vertical direction, a steam generator forming a cylindrical water tube group, or in addition thereto In a vertical water tube boiler in which the inner space of the cylindrical water tube group is configured as a combustion chamber and a combustor that forms a flame toward the combustion chamber is disposed, an adjacent space forming the cylindrical water tube group is provided. It is characterized in that the gap between the evaporating tubes is narrowly arranged, and each has the following features.

【0008】本発明に係る蒸気発生器の第1特徴構成
は、請求項1に記載のごとく、蒸発管を、炉壁に沿った
円筒面に沿って狭い間隙で配列して円筒状水管群を形成
し、その円筒状水管群の隣接する蒸発管の間隙を熱源ガ
スを外方に向けて通流する径方向流路として形成してあ
る点にある。
According to a first feature of the steam generator according to the present invention, as set forth in claim 1, the evaporating tubes are arranged at a narrow gap along a cylindrical surface along the furnace wall to form a cylindrical water tube group. And the gap between the evaporating pipes adjacent to the cylindrical water pipe group is formed as a radial flow path through which the heat source gas flows outward.

【0009】本発明に係る蒸気発生器の第2特徴構成
は、請求項2に記載のごとく、上記蒸気発生器の第1特
徴構成における円筒状水管群に沿って側壁部との間で熱
源ガスを円筒状水管群の外周に沿って出口部に導く外周
流路を形成し、その外周流路に臨む前記蒸発管の外面
を、前記熱源ガスとの接触伝熱を促進する接触伝熱部と
して構成してある点にある。
According to a second aspect of the steam generator according to the present invention, a heat source gas is formed between the side wall and the cylindrical water pipe group in the first aspect of the steam generator. Is formed along the outer periphery of the cylindrical water tube group to the outlet portion, and the outer surface of the evaporator tube facing the outer peripheral passage is used as a contact heat transfer portion that promotes contact heat transfer with the heat source gas. The point is that it is structured.

【0010】本発明に係る竪型水管ボイラの第1特徴構
成は、請求項3に記載のごとく、蒸発管を、炉壁に沿う
単一の円筒面に沿って隣接するもの同士の間隙を狭く配
列した円筒状水管群を形成し、燃焼器を天井部に配置し
て下方に向けて火炎を形成するように構成し、側壁部の
一側方に前記燃焼器で生成する燃焼ガスを排出する排ガ
ス出口を設け、前記排ガス出口近傍の蒸発管は密接配置
すると共に、その他の部位に配置する蒸発管の間隙を、
前記燃焼ガスが前記側壁部に向かう外向きの径方向流路
として形成してある点にある。
A first characteristic configuration of the vertical water tube boiler according to the present invention is that, as described in claim 3, the gap between adjacent ones of the evaporating tubes along a single cylindrical surface along the furnace wall is narrowed. An array of cylindrical water tubes is formed, the combustor is arranged on the ceiling to form a flame downward, and the combustion gas generated by the combustor is discharged to one side of the side wall. An exhaust gas outlet is provided, and the evaporating pipes in the vicinity of the exhaust gas outlet are closely arranged, and a gap between the evaporating pipes arranged in other parts is provided.
The combustion gas is formed as an outward radial flow path toward the side wall.

【0011】本発明に係る竪型水管ボイラの第2特徴構
成は、請求項4に記載のごとく、上記竪型水管ボイラの
第1特徴構成における円筒状水管群と側壁部との間に、
径方向流路から流出した燃焼ガスを、排ガス出口に向け
て周方向に導く外周流路を形成し、前記外周流路に臨む
蒸発管の外面を、前記燃焼ガスとの接触伝熱を促進する
接触伝熱部として構成してある点にある。
According to a second aspect of the vertical water pipe boiler according to the present invention, the vertical water pipe boiler includes a cylindrical water pipe group and a side wall portion in the first characteristic configuration of the vertical water pipe boiler.
Forming an outer peripheral flow path that guides the combustion gas flowing out from the radial flow path in the circumferential direction toward the exhaust gas outlet, and promotes the heat transfer in contact with the combustion gas on the outer surface of the evaporator tube facing the outer peripheral flow path. The point is that it is configured as a contact heat transfer section.

【0012】〔特徴構成の作用及び効果〕上記本発明に
係る蒸気発生器及び竪型水管ボイラによれば、隣接する
蒸発管同士の間隙を狭くして、伝熱効率の高い径方向流
路として形成し、蒸気発生器の組み立て工数を節減して
製造コストを低減し、同時に熱効率も改善できるもの
で、夫々に、以下のような独特の作用効果を奏する。
According to the steam generator and the vertical water tube boiler according to the present invention, the gap between adjacent evaporating tubes is narrowed to form a radial passage having high heat transfer efficiency. In addition, the number of assembling steps of the steam generator can be reduced to reduce the manufacturing cost, and at the same time, the thermal efficiency can be improved, and each has the following unique effects.

【0013】上記本発明に係る蒸気発生器の第1特徴構
成によれば、円筒状水管群の内側空間と外側空間との間
に、隣接する蒸発管同士の間の狭い間隙を径方向流路と
することで、この径方向流路における伝熱効率を高く維
持し、その結果として、側壁部に達する熱源ガスの温度
が低下するから、耐火物を施さなくても側壁部の温度を
十分に低く維持できるようになる。また、単一の円筒状
水管群で伝熱管群を構成するから、その蒸発管の組み込
み順序に制約がなく、蒸発気の組立が容易になる。しか
も、前記蒸発管は溶接しなくてもよいから、蒸発器を組
み立てるのに手間と時間を低減できる。
According to the first characteristic configuration of the steam generator according to the present invention, a narrow gap between the adjacent evaporating tubes is formed between the inner space and the outer space of the cylindrical water tube group in the radial flow path. By keeping the heat transfer efficiency in this radial flow path high, as a result, the temperature of the heat source gas reaching the side wall decreases, so that the temperature of the side wall can be sufficiently reduced without applying a refractory. Be able to maintain. Further, since the heat transfer tube group is constituted by a single cylindrical water tube group, there is no restriction on the order of assembling the evaporating tubes, and the assembling of the evaporating air is facilitated. In addition, since the evaporator tube does not need to be welded, labor and time for assembling the evaporator can be reduced.

【0014】上記本発明に係る蒸発器の第2特徴構成に
よれば、上記蒸気発生器の第1特徴構成の作用効果を奏
する中で、円筒状水管群の外周に沿って形成した外周流
路に臨む蒸発管の外面に接触伝熱部を構成することで、
径方向流路で効率よく熱交換した結果温度の低下した熱
源ガスとの接触伝熱を促進し、コンパクトな構造であり
ながら、さらに伝熱効率を向上することが可能になる。
According to the second characteristic configuration of the evaporator according to the present invention, the outer circumferential flow path formed along the outer circumference of the cylindrical water pipe group while exhibiting the operation and effect of the first characteristic configuration of the steam generator. By forming a contact heat transfer section on the outer surface of the evaporator tube facing
As a result of efficient heat exchange in the radial flow path, contact heat transfer with the heat source gas whose temperature has decreased is promoted, and the heat transfer efficiency can be further improved while having a compact structure.

【0015】上記本発明に係る竪型水管ボイラの第1特
徴構成によれば、炉壁に沿う単一の円筒状水管群を形成
し、その円筒状水管群における隣接する蒸発管の間隙を
狭くして、燃焼ガスを外方に通流させる径方向流路とし
て形成してあることで、この径方向流路の高い伝熱効率
を活用でき、しかも、狭い隙間であっても前記円筒状水
管群全体の間隙の合計流路断面積は十分にとれるから、
流路抵抗を低く抑えることができる。また、燃焼ガスの
流路における流路抵抗を低く抑えることで、燃焼器の圧
力を高める必要がなくなり、そのコストを低減できる。
さらに、蒸発管群を単一の円筒状水管群で構成すること
で、蒸発管の取り付け順序に制約がなくなり、竪型水管
ボイラの組み立て作業性を向上し、その組み立てに要す
る時間と手間とを低減できる。
According to the first characteristic configuration of the vertical water tube boiler according to the present invention, a single cylindrical water tube group is formed along the furnace wall, and the gap between adjacent evaporating tubes in the cylindrical water tube group is narrowed. And, by being formed as a radial flow path through which the combustion gas flows outward, the high heat transfer efficiency of this radial flow path can be utilized, and even in a narrow gap, the cylindrical water pipe group is formed. Since the total flow path cross-sectional area of the entire gap is sufficient,
The flow path resistance can be kept low. Further, by suppressing the flow resistance in the flow path of the combustion gas to be low, it is not necessary to increase the pressure of the combustor, and the cost can be reduced.
Furthermore, by configuring the evaporating tube group with a single cylindrical water tube group, there is no restriction on the mounting order of the evaporating tubes, improving the workability of assembling the vertical water tube boiler, and reducing the time and labor required for the assembly. Can be reduced.

【0016】上記本発明に係る竪型水管ボイラの第2特
徴構成によれば、蒸気竪型水管ボイラの第1特徴構成の
作用効果を奏する中で、十分に温度低下して燃焼ガスが
外周流路に至っても、接触伝熱部に接して効率よく熱を
蒸発管内に伝達するのである。
According to the second characteristic configuration of the vertical water tube boiler according to the present invention, while exhibiting the operation and effect of the first characteristic configuration of the steam vertical water tube boiler, the temperature is sufficiently lowered and the combustion gas is discharged to the outer peripheral flow. Even on the road, the heat is efficiently transferred into the evaporator tube by contacting the contact heat transfer section.

【0017】[0017]

【発明の実施の形態】以下、本発明に係る蒸気発生器及
び竪型水管ボイラに関する実施の形態に関して、蒸気発
生器は一つの例につき、竪型水管ボイラは二つの例につ
いて図面を参照しながら説明する。尚、先の図8及び図
9により説明した要素と同一若しくは類似の機能を有す
る要素には、同一若しくは類似の符号を付し、重複する
説明の一部は省略する。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of a steam generator and a vertical water tube boiler according to the present invention will be described with reference to the drawings for one example of a steam generator and two examples of a vertical water tube boiler. explain. Elements having the same or similar functions as the elements described with reference to FIGS. 8 and 9 are denoted by the same or similar reference numerals, and a part of the overlapping description will be omitted.

【0018】〔第一の実施の形態〕[First Embodiment]

【0019】蒸気発生器は、図1及び図2に基本的構成
を示すように、天井部12に配置した蒸気ドラムとして
機能する上部ヘッダ1と、底部13に配置した給水ドラ
ムとして機能する下部ヘッダ2とを設け、上端部を前記
上部ヘッダ1に接続し、下端部を前記下部ヘッダ2に接
続して、縦方向に設けた複数の蒸発管3を、上下方向に
形成される円筒状の側壁部11に沿って配置して構成し
てある。そして、前記蒸発管3を、前記側壁部11に沿
った円筒面に沿って狭い間隙で配列して円筒状水管群4
を形成する。この円筒状水管群4の隣接する蒸発管3の
間隙を熱源ガスを内外方向に通流する径方向流路5とし
て形成する。この間隙は狭い方がよいが、あまり狭いと
煤塵による間隙の閉塞を招くおそれがあり、また、前記
蒸発管3に結露が生じた場合にも、前記間隙があまりに
狭い場合には、隣接する蒸発管3同士の外面に繋がった
水滴を生ずることで腐食を招くおそれもあり、少なくと
も0.5mm以上の間隙とする。尚、この間隙が2mm
を超える間隔になると、伝熱効率低下するから好ましく
ない。前記円筒状水管群4に沿って周方向に熱源ガスを
通流する外周流路6を形成し、その外周流路6に臨む部
位に位置する蒸発管3の前記外周流路6に臨む外面を、
前記熱源ガスとの接触伝熱を促進する吸熱フィン14を
設けて接触伝熱部9として構成する。前記蒸気発生器の
円筒状の側壁部11の一側方には、前記熱源ガスの出口
部Oが開口し、前記下部ヘッダ2を環状に形成して、そ
の下部ヘッダ2の内側の底部13には、前記熱源ガスの
導入部Iが開口している。前記円筒状水管群4の周方向
の前記出口部Oの近傍においては、前記隣接する蒸発管
3同士の間を密接させておく。
As shown in FIGS. 1 and 2, the steam generator has an upper header 1 functioning as a steam drum disposed on a ceiling 12 and a lower header functioning as a water supply drum disposed on a bottom 13. 2, the upper end portion is connected to the upper header 1, the lower end portion is connected to the lower header 2, and a plurality of evaporating tubes 3 provided in a vertical direction are connected to a cylindrical side wall formed in a vertical direction. It is arranged and arranged along the part 11. Then, the evaporating tubes 3 are arranged with a narrow gap along a cylindrical surface along the side wall portion 11 to form a cylindrical water tube group 4.
To form The gap between the evaporating pipes 3 adjacent to the cylindrical water pipe group 4 is formed as a radial flow path 5 through which the heat source gas flows inward and outward. The gap is preferably narrow. However, if the gap is too narrow, the dust may block the gap. Also, if dew condensation occurs in the evaporating pipe 3, if the gap is too narrow, adjacent evaporation Water droplets connected to the outer surfaces of the pipes 3 may cause corrosion, and the gap should be at least 0.5 mm or more. In addition, this gap is 2 mm
If the distance exceeds the range, the heat transfer efficiency is undesirably reduced. An outer peripheral channel 6 that allows a heat source gas to flow in the circumferential direction along the cylindrical water pipe group 4 is formed, and an outer surface of the evaporating pipe 3 located at a portion facing the outer peripheral channel 6 facing the outer peripheral channel 6 is formed. ,
Heat absorbing fins 14 for promoting the contact heat transfer with the heat source gas are provided to constitute the contact heat transfer section 9. On one side of the cylindrical side wall 11 of the steam generator, an outlet O of the heat source gas is opened, and the lower header 2 is formed in an annular shape. The opening I of the heat source gas is open. In the vicinity of the outlet portion O in the circumferential direction of the cylindrical water tube group 4, the adjacent evaporating tubes 3 are kept in close contact with each other.

【0020】図示ように、円筒状水管群4は一重に形成
してあり、前記円筒状水管群4の周方向領域で前記出口
部O近傍を除く位置の前記蒸発管3の間隙で、前記熱源
ガスの径方向流路5が形成され、前記径方向流路5から
両側に、前記円筒状の側壁部11と前記円筒状水管群4
を形成する蒸発管3との間に、前記外周流路6が形成さ
れる。前記外周流路6に臨む蒸発管3のうちで、前記出
口部O近傍の蒸発管3は、隣接するもの同士を密接させ
て配置する。こうして密接配置した蒸発管3の上下全長
に亘って、図2に示すように、前記円筒状水管群4の外
周を形成する外面に、吸熱フィン14を熱的に接続して
取り付けて、前記接触伝熱部9を構成する。つまり、熱
源ガスは、蒸気発生器の下方から前記円筒状水管群4の
内側に導入され、前記蒸発管3の間に形成された径方向
流路5から前記円筒状水管群4の外側に流出し、前記側
壁部11と前記円筒状水管群4との間を周方向に流れ
て、前記出口部Oから流出するのである。因みに、前記
径方向流路5は狭い蒸発管3の間隙を通じているから伝
熱効率はよく、熱源ガスの温度は十分に低下する。そこ
で、前記蒸発管3の温度と前記熱源ガスの温度との差が
小さくなるから、前記出口部O近傍の外周流路6に臨む
前記蒸発管3の外面に前記接触伝熱部9を形成して、前
記吸熱フィン14による熱吸収を図り、全体としての伝
熱効率をさらに向上させているのである。
As shown in the figure, the cylindrical water pipe group 4 is formed in a single layer, and the heat source is located at a gap between the evaporating pipes 3 in a circumferential area of the cylindrical water pipe group 4 except for the vicinity of the outlet O. A radial flow path 5 for gas is formed, and the cylindrical side wall portion 11 and the cylindrical water pipe group 4 are provided on both sides from the radial flow path 5.
Is formed between the evaporating tube 3 and the evaporating tube 3. Among the evaporating pipes 3 facing the outer peripheral flow path 6, the evaporating pipes 3 near the outlet O are arranged such that adjacent ones are in close contact with each other. As shown in FIG. 2, heat absorbing fins 14 are thermally connected to and attached to the outer surface forming the outer periphery of the cylindrical water tube group 4 over the entire length of the evaporating tubes 3 closely arranged in this manner, as shown in FIG. The heat transfer section 9 is configured. That is, the heat source gas is introduced into the cylindrical water pipe group 4 from below the steam generator, and flows out of the cylindrical water pipe group 4 from the radial flow path 5 formed between the evaporation pipes 3. Then, it flows between the side wall portion 11 and the cylindrical water tube group 4 in the circumferential direction, and flows out from the outlet portion O. Incidentally, since the radial flow path 5 passes through the narrow gap between the evaporating tubes 3, the heat transfer efficiency is good, and the temperature of the heat source gas is sufficiently lowered. Therefore, since the difference between the temperature of the evaporator tube 3 and the temperature of the heat source gas becomes smaller, the contact heat transfer portion 9 is formed on the outer surface of the evaporator tube 3 facing the outer peripheral flow path 6 near the outlet portion O. Thus, heat absorption by the heat absorbing fins 14 is achieved, and the overall heat transfer efficiency is further improved.

【0021】この蒸気発生器においては、熱源ガスを約
1000℃で前記円筒状水管群4の内部空間に導入した
場合に、前記外周流路6に流出する熱源ガスの保有熱は
この径方向流路5で約36%前記蒸発管3に伝達され、
その温度は300℃以下にまで低下する。そこで、前記
外周流路6における熱源ガスの熱回収が困難になるの
で、前記接触伝熱部9で熱回収を図るのである。この接
触伝熱部9に設ける吸熱フィン14は、蒸発管3に夫々
溶接して取り付ける。尚、前記蒸発管3の間隙は、前記
径方向流路5の合計流路断面積が排気路のそれより小さ
くなるように設定し、前記外周流路6における流路断面
積は、排気路のそれよりも大きくなるようにする。従っ
て、この蒸気発生器は熱効率が極めて良好でありなが
ら、前記半径方向流路5が極めて短かいこともあり、そ
の流路抵抗は低くなる。
In this steam generator, when the heat source gas is introduced into the inner space of the cylindrical water pipe group 4 at about 1000 ° C., the heat retained by the heat source gas flowing out to the outer peripheral flow path 6 is converted into the radial flow. About 36% is transmitted to the evaporating tube 3 by a passage 5,
Its temperature drops below 300 ° C. Then, since it becomes difficult to recover the heat of the heat source gas in the outer peripheral flow path 6, the contact heat transfer section 9 recovers the heat. The heat absorbing fins 14 provided in the contact heat transfer section 9 are respectively attached to the evaporating tubes 3 by welding. The gap between the evaporating pipes 3 is set so that the total cross-sectional area of the radial flow path 5 is smaller than that of the exhaust path. Make it bigger. Therefore, the steam generator has extremely good thermal efficiency, and the radial flow path 5 may be extremely short, so that the flow resistance is low.

【0022】〔第二の実施の形態〕[Second Embodiment]

【0023】竪型水管ボイラは、図3及び図4に示すよ
うに、ボイラ本体10の上部及び下部に、蒸気ドラムと
して機能する上部ヘッダ1と、給水ドラムとして機能す
る下部ヘッダ2とを設け、上端部を前記上部ヘッダ1に
接続し、下端部を前記下部ヘッダ2に接続して、縦方向
に設けた複数の蒸発管3を、上下方向に形成される円筒
状の側壁部11に沿って配置すると共に、前記配列され
た蒸発管3の内側空間を燃焼室8として、前記燃焼室8
内に向けて火炎を形成する燃焼器7を配置する構成を基
本構成とする。そして、前記上部ヘッダ1を環状に形成
して、前記燃焼器7を前記上部ヘッダ1の内側空間の天
井部12に下方に向けて火炎を形成するように配置し、
前記側壁部11の一側方に前記燃焼器7で生成する燃焼
ガスを排出する排ガス出口Eを設ける。
As shown in FIGS. 3 and 4, the vertical water tube boiler is provided with an upper header 1 functioning as a steam drum and a lower header 2 functioning as a water supply drum at the upper and lower portions of a boiler main body 10. The upper end is connected to the upper header 1, the lower end is connected to the lower header 2, and a plurality of evaporating tubes 3 provided in a vertical direction are arranged along a cylindrical side wall 11 formed in a vertical direction. At the same time, the internal space of the evaporating pipes 3 arranged as the combustion chamber 8
The basic configuration is a configuration in which a combustor 7 that forms a flame inward is arranged. Then, the upper header 1 is formed in an annular shape, and the combustor 7 is arranged so as to form a flame downward on the ceiling portion 12 of the inner space of the upper header 1,
An exhaust gas outlet E for discharging the combustion gas generated in the combustor 7 is provided on one side of the side wall 11.

【0024】前記蒸発管3は、前記側壁部11とほぼ同
心の円筒面に沿って配列して、単一の円筒状水管群4を
形成する。この円筒状水管群4を形成する蒸発管3は、
狭い間隔で配列し、前記排ガス出口E近傍の蒸発管3の
み、隣接するもの同士を密接させて配置する。つまり、
前記蒸発管3の間の狭い間隙を、前記燃焼器7で生成す
る燃焼ガスを前記側壁部11に向けて外向きに導く径方
向流路5として形成すると共に、前記円筒状水管群4と
前記側壁部11との間に、燃焼ガスを周方向に導く外周
流路6を形成する。この外周流路6に臨む前記排ガス出
口E近傍の蒸発管3の外面に、前記燃焼ガスとの接触伝
熱を促進する吸熱フィン14を設けて、前記側壁部11
に対向する蒸発管3の外面を接触伝熱部9として構成す
る。前記燃焼器7で前記円筒状水管群4の内側空間で形
成する燃焼室8で生成する燃焼ガスは、前記径方向流路
5を経て前記円筒状水管群4の外側に流出し、この間に
大部分の熱交換を終え、前記円筒状水管群4と前記円筒
状の側壁部11との間の外周流路6を経て前記排ガス出
口Eに至るのである。
The evaporating tubes 3 are arranged along a cylindrical surface substantially concentric with the side wall portion 11 to form a single cylindrical water tube group 4. The evaporating tubes 3 forming the cylindrical water tube group 4 are:
They are arranged at a narrow interval, and only the evaporating pipes 3 near the exhaust gas outlet E are arranged so that adjacent ones are in close contact with each other. That is,
A narrow gap between the evaporating tubes 3 is formed as a radial flow path 5 for guiding the combustion gas generated in the combustor 7 outward toward the side wall portion 11, and the cylindrical water pipe group 4 and the An outer peripheral passage 6 for guiding the combustion gas in the circumferential direction is formed between the outer peripheral passage 6 and the side wall 11. On the outer surface of the evaporating pipe 3 near the exhaust gas outlet E facing the outer peripheral flow path 6, heat absorbing fins 14 for promoting heat transfer in contact with the combustion gas are provided.
The outer surface of the evaporating tube 3 opposed to is formed as a contact heat transfer section 9. Combustion gas generated in the combustion chamber 8 formed in the inner space of the cylindrical water pipe group 4 in the combustor 7 flows out of the cylindrical water pipe group 4 through the radial flow path 5, and a large amount of gas flows during this time. After the heat exchange of the portion is completed, the heat reaches the exhaust gas outlet E via the outer peripheral flow path 6 between the cylindrical water pipe group 4 and the cylindrical side wall portion 11.

【0025】前記燃焼室8では、前記燃焼器7で生成す
る燃焼ガスの温度は約1000℃に維持され、その保有
熱の内の約47%を輻射伝熱で前記円筒状水管群4を形
成する蒸発管3に伝達する。そして、前記燃焼ガスは、
距離が極めて短いが上述の通り伝熱効率がよい前記径方
向流路5でその保有熱の内の約36%を蒸発管3に伝達
し、その温度が約1000℃から約350℃に低下する
のである。そこで、前記排ガス出口E近傍の外周流路6
に臨む前記蒸発管3の外面を前記接触伝熱部9として構
成し、前記吸熱フィン14により、前記温度の低下した
燃焼ガスからの熱回収を図り、全体としての伝熱効率を
向上させているのである。ここで残余の保有熱の内の約
7%を燃焼ガスから吸収し、前記排ガス出口Eに至る燃
焼ガスの温度は約280℃となる。
In the combustion chamber 8, the temperature of the combustion gas generated in the combustor 7 is maintained at about 1000 ° C., and about 47% of the retained heat is formed by the radiant heat to form the cylindrical water tube group 4. To the evaporating tube 3. And the combustion gas is
As described above, about 36% of the retained heat is transmitted to the evaporating tube 3 in the radial flow path 5 which has a very short distance but has a high heat transfer efficiency as described above, and the temperature decreases from about 1000 ° C. to about 350 ° C. is there. Therefore, the outer peripheral flow path 6 near the exhaust gas outlet E
The outer surface of the evaporating tube 3 facing the air is formed as the contact heat transfer section 9, and the heat absorbing fins 14 recover heat from the combustion gas whose temperature has decreased, thereby improving the overall heat transfer efficiency. is there. Here, about 7% of the remaining heat is absorbed from the combustion gas, and the temperature of the combustion gas reaching the exhaust gas outlet E is about 280 ° C.

【0026】前記吸熱フィン14は、蒸発管3に夫々溶
接して取り付ける。上述のように、前記側壁部11に至
る燃焼ガスの温度が低いから、前記側壁部11は耐火物
を設けない鉄皮で形成することができる。さらに、前記
径方向流路5を構成する前記蒸発管3の間隙は、前記径
方向流路5の合計流路断面積は、先に第一の実施の形態
で説明したと同様に設定でき、また、前記外周流路6の
流路断面積は、下流側流路の流路断面積よりも大きくな
るように設定することができ、前記径方向流路5、前記
外周流路6共に、流路抵抗を抑えることができて、生成
する燃焼ガスの背圧を低くできるから、前記燃焼器7を
安価なもので済ますことができる。その上、前記蒸発管
3は、単一の円筒状水管群4を形成するから、前記上部
ヘッダ1と前記下部ヘッダ2との間に取り付けるのに、
その順序を制約されない。例えば、本発明の主たる対象
とする小型の竪型水管ボイラにおいて、前記円筒状水管
群4を二重にしてあれば、少なくともその一方の円筒状
水管群4を先に組み立てなければならないのである。従
って、構造が簡単であり、製造コストを低減でき、しか
も性能の高い竪型水管ボイラを構成することができる。
The heat absorbing fins 14 are attached to the evaporating tubes 3 by welding. As described above, since the temperature of the combustion gas reaching the side wall portion 11 is low, the side wall portion 11 can be formed of a steel shell provided with no refractory. Further, the gap between the evaporating tubes 3 constituting the radial flow path 5 can be set in the same manner as described in the first embodiment, and the total flow path cross-sectional area of the radial flow path 5 can be set, The cross-sectional area of the outer peripheral flow path 6 can be set to be larger than the cross-sectional area of the downstream flow path. Since the road resistance can be suppressed and the back pressure of the generated combustion gas can be reduced, the combustor 7 can be inexpensive. In addition, since the evaporating tubes 3 form a single cylindrical water tube group 4, the evaporating tubes 3 are mounted between the upper header 1 and the lower header 2.
The order is not restricted. For example, in a small vertical water tube boiler that is a main object of the present invention, if the cylindrical water tube group 4 is doubled, at least one of the cylindrical water tube groups 4 must be assembled first. Therefore, a vertical water tube boiler having a simple structure, a reduced production cost, and high performance can be configured.

【0027】〔別実施形態〕上記実施の形態において示
さなかった本発明に係る蒸気発生器及び竪型水管ボイラ
の他の実施の形態について以下に説明する。
[Other Embodiments] Other embodiments of the steam generator and the vertical water tube boiler according to the present invention not shown in the above embodiment will be described below.

【0028】〈1〉 上記第一の実施の形態に於いて
は、下部ヘッダ2を環状に形成して、その下部ヘッダ2
の内側の底部13に、熱源ガスの導入部Iを開口させた
例について説明したが、前記導入部Iは、上部ヘッダ1
を環状に形成して、その上部ヘッダ1の内側の天井部1
2に開口させてあってもよい。
<1> In the first embodiment, the lower header 2 is formed in an annular shape, and the lower header 2
The example in which the heat source gas introduction portion I is opened in the bottom portion 13 inside the above has been described.
Is formed in an annular shape, and a ceiling portion 1 inside the upper header 1 is formed.
2 may be opened.

【0029】〈2〉 上記第一の実施の形態に於いて
は、下部ヘッダ2の内側の底部13に導入部Iを開口
し、側壁部11の一側方に出口部Oを開口して、円筒状
水管群4の内側から外方に向けて熱源ガスが通流する例
について説明したが、例えば図5に示すように、前記出
口部Oを、上部ヘッダ1の上方の天井部12に開口させ
てあってもよい。また、導入部Iと出口部Oとを上下逆
に配置してあってもよい。要は、径方向流路5を、円筒
状水管群4の内側から外方に向けて熱源ガスが通流する
経路としてあればよい。
<2> In the first embodiment, the introduction portion I is opened in the bottom portion 13 inside the lower header 2, and the outlet portion O is opened on one side of the side wall portion 11. The example in which the heat source gas flows outward from the inside of the cylindrical water tube group 4 has been described. For example, as shown in FIG. 5, the outlet O is opened to the ceiling 12 above the upper header 1. You may let me. Further, the introduction section I and the exit section O may be arranged upside down. In short, the radial flow path 5 may be a path through which the heat source gas flows from the inside of the cylindrical water pipe group 4 to the outside.

【0030】〈3〉 上記第一の実施の形態に於いて
は、外周流路6に臨む蒸発管3のうちで、出口部O近傍
の蒸発管3は、隣接するもの同士を密接配置する例につ
いて図1を用いて説明したが、密接配置する領域を、前
記出口部Oの反対側に向けて拡張してもよい。
<3> In the first embodiment, among the evaporating pipes 3 facing the outer peripheral flow path 6, the evaporating pipes 3 near the outlet O are closely arranged. Has been described with reference to FIG. 1, the closely arranged region may be expanded toward the opposite side of the outlet portion O.

【0031】〈4〉 上記第一の実施の形態に於いて
は、円筒状水管群4の外周流路6に臨む蒸発管3の外面
を吸熱フィン14を設けた接触伝熱部9として構成した
例について説明したが、前記吸熱フィン14は、さらに
広範囲に亘って設けてもよく、全ての前記蒸発管3の側
壁部11に対向する側の外面に設けて前記円筒状水管群
4の全周に亘って前記蒸発管3の外面を接触伝熱部9と
して構成してあってもよい。
<4> In the first embodiment, the outer surface of the evaporating pipe 3 facing the outer peripheral flow path 6 of the cylindrical water pipe group 4 is configured as the contact heat transfer section 9 provided with the heat absorbing fins 14. Although the example has been described, the heat absorbing fins 14 may be provided over a wider range, and may be provided on the outer surface of all the evaporating tubes 3 on the side facing the side wall portion 11 so as to cover the entire circumference of the cylindrical water tube group 4. The outer surface of the evaporating tube 3 may be configured as the contact heat transfer section 9 over the range.

【0032】〈5〉 上記第二の実施の形態及び第三の
実施の形態に於いては、燃焼器7を上部ヘッダ1の内側
空間の天井部12に下方に向けて火炎を形成するように
配置した例について説明したが、前記燃焼器7を環状に
形成した下部ヘッダ2の内側の底部13に、上方に向け
て火炎を形成するように設けてあってもよい。
<5> In the second and third embodiments, the flame is formed so that the combustor 7 is directed downward to the ceiling 12 in the inner space of the upper header 1. Although the arrangement example has been described, the combustor 7 may be provided on the bottom 13 inside the lower header 2 having an annular shape so as to form a flame upward.

【0033】〈6〉 上記第二の実施の形態に於いて
は、単一の円筒状水管群4を設けた例について説明した
が、例えば図6及び図7に示すように、上記第二の実施
の形態における円筒状水管群4の外側に、前記側壁部1
1に沿って蒸発管3を配置し、前記排ガス出口Eの部位
に蒸発管を配置しない断面C字状に形成した切り欠き円
筒状の円筒状水管壁4Aを設けてもよい。この場合、前
記円筒状水管壁4Aに配置する蒸発管3は、隣接するも
の同士の間をフィンプレートPで連結しておく。そし
て、前記内側円筒状水管群4の外側で、前記円筒状水管
壁4Aとの間に、前記燃焼ガスを前記排ガス出口Eに向
けて周方向に導く外周流路6を形成する。この外周流路
6に臨む前記円筒状水管群4及び前記円筒状水管壁4A
の蒸発管3夫々の外面に熱的に接続して吸熱フィン14
を設けて、前記外周流路6に臨む前記蒸発管3の外面を
接触伝熱部9として構成する。
<6> In the second embodiment, an example in which a single cylindrical water pipe group 4 is provided has been described. For example, as shown in FIGS. The side wall portion 1 is provided outside the cylindrical water tube group 4 in the embodiment.
The exhaust pipe 3 may be disposed along the exhaust pipe E, and a cut-out cylindrical water pipe wall 4A formed in a C-shaped cross section without the evaporative pipe may be provided at the exhaust gas outlet E. In this case, the evaporating pipes 3 arranged on the cylindrical water pipe wall 4A are connected to each other with a fin plate P between adjacent ones. Then, an outer peripheral flow path 6 that guides the combustion gas in the circumferential direction toward the exhaust gas outlet E is formed outside the inner cylindrical water pipe group 4 and between the cylindrical water pipe wall 4A. The cylindrical water pipe group 4 and the cylindrical water pipe wall 4A facing the outer peripheral flow path 6
Heat absorbing fins 14 which are thermally connected to the outer surfaces of
And the outer surface of the evaporating tube 3 facing the outer peripheral flow path 6 is configured as a contact heat transfer section 9.

【0034】この構成により、前記円筒状水管群4にお
ける径方向流路5の伝熱効率の高いところを利用しなが
ら、前記径方向流路5を通過した燃焼ガスの温度が低下
していても、その燃焼ガスを前記円筒状水管壁4Aで受
け止め、前記円筒状水管壁4Aと前記円筒状水管群4と
の間に形成した外周流路6に接触伝熱部9を構成してあ
るから、総合的な熱回収効率を十分に高くとることがで
きる。また、側壁部11を前記円筒状水管壁4Aで形成
することで、外壁温度をさらに低くできる。従って、熱
効率も向上できる。
With this configuration, while utilizing the high heat transfer efficiency of the radial flow path 5 in the cylindrical water pipe group 4, even if the temperature of the combustion gas passing through the radial flow path 5 is reduced, The combustion gas is received by the cylindrical water pipe wall 4A, and the contact heat transfer portion 9 is formed in the outer peripheral flow path 6 formed between the cylindrical water pipe wall 4A and the cylindrical water pipe group 4. Thus, the overall heat recovery efficiency can be made sufficiently high. Further, by forming the side wall portion 11 with the cylindrical water tube wall 4A, the outer wall temperature can be further reduced. Therefore, the thermal efficiency can be improved.

【0035】〈7〉 上記第二の実施の形態に於いて
は、排ガス出口Eを側壁部11の一側方に設けた例につ
いて説明したが、前記排ガス出口Eは、下部ヘッダ2の
下方に開口させてあってもよい。また、燃焼器7を底部
13に設けて、前記排ガス出口Eを上部ヘッダ1の上方
に開口させてあってもよい。
<7> In the second embodiment, the example in which the exhaust gas outlet E is provided on one side of the side wall portion 11 has been described, but the exhaust gas outlet E is provided below the lower header 2. It may be opened. Further, the combustor 7 may be provided at the bottom 13, and the exhaust gas outlet E may be opened above the upper header 1.

【0036】〈8〉 以上に説明した接触伝熱部9は、
隣接するもの同士を密接配置した蒸発管3には設けてあ
ることが望ましく、外周流路6の流れの方向を周方向に
してある場合には、前記外周流路6に臨む蒸発管3夫々
の外面全てに設けてあってもよい。
<8> The contact heat transfer section 9 described above
It is desirable to provide the evaporating pipes 3 in which adjacent ones are closely arranged. When the direction of the flow of the outer peripheral flow path 6 is set to the circumferential direction, each of the evaporating pipes 3 facing the outer peripheral flow path 6 is provided. It may be provided on all outer surfaces.

【0037】〈9〉上記各実施の形態に於いては、上部
ヘッダ1、下部ヘッダ2共に環状に形成してある例につ
いて図に示して説明したが、このヘッダの形状は任意で
あり、上下何れかに導入部I或いは出口部Oを設ける場
合を除き、蒸発管3の配置に応じて任意の形状を選択で
きる。
<9> In each of the above-described embodiments, an example in which both the upper header 1 and the lower header 2 are formed in a ring shape has been described with reference to the drawings, but the shape of the header is arbitrary. An arbitrary shape can be selected in accordance with the arrangement of the evaporating tubes 3, except in the case where the introduction part I or the outlet part O is provided in any of them.

【0038】[0038]

【発明の効果】以上説明したように、本発明によって、
コンパクトな構造を維持しながら、製造コストを削減
し、且つ、伝熱効率を向上できた。
As described above, according to the present invention,
The manufacturing cost was reduced and the heat transfer efficiency was improved while maintaining a compact structure.

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

【図1】本発明に係る蒸気発生器の一例につき構成を説
明する平断面図
FIG. 1 is a cross-sectional plan view illustrating a configuration of an example of a steam generator according to the present invention.

【図2】図1に示した蒸気発生器の構成を説明する縦断
面図
FIG. 2 is a longitudinal sectional view illustrating the configuration of the steam generator shown in FIG.

【図3】本発明に係る竪型水管ボイラの一例につき構成
を説明する平断面図
FIG. 3 is a cross-sectional plan view illustrating a configuration of an example of a vertical water tube boiler according to the present invention.

【図4】図3に示した竪型水管ボイラの構成を説明する
縦断面図
FIG. 4 is a longitudinal sectional view illustrating the configuration of the vertical water tube boiler shown in FIG.

【図5】本発明に係る蒸発器の他の例につき構成を説明
する縦断面図
FIG. 5 is a longitudinal sectional view illustrating the configuration of another example of the evaporator according to the present invention.

【図6】本発明に係る竪型水管ボイラの他の例につき構
成を説明する平断面図
FIG. 6 is a cross-sectional plan view illustrating the configuration of another example of the vertical water tube boiler according to the present invention.

【図7】図6に示した竪型水管ボイラの構成を説明する
縦断面図
FIG. 7 is a longitudinal sectional view illustrating the configuration of the vertical water tube boiler shown in FIG.

【図8】従来の竪型水管ボイラの一例を示す平断面図。FIG. 8 is a plan sectional view showing an example of a conventional vertical water tube boiler.

【図9】従来の竪型水管ボイラの他の例を示す平断面
図。
FIG. 9 is a plan sectional view showing another example of a conventional vertical water tube boiler.

【符号の説明】[Explanation of symbols]

1 上部ヘッダ 2 下部ヘッダ 3 蒸発管 4 円筒状水管群 5 径方向流路 6 外周流路 7 燃焼器 8 燃焼室 9 接触伝熱部 11 側壁部 12 天井部 E 排ガス出口 O 出口部 DESCRIPTION OF SYMBOLS 1 Upper header 2 Lower header 3 Evaporation pipe 4 Cylindrical water pipe group 5 Radial flow path 6 Outer flow path 7 Combustor 8 Combustion chamber 9 Contact heat transfer part 11 Side wall part 12 Ceiling part E Exhaust gas outlet O Exit part

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 上下に上部ヘッダと下部ヘッダとを設
け、上端部を前記上部ヘッダに接続し、下端部を前記下
部ヘッダに接続して、縦方向に設けた複数の蒸発管を、
上下方向に形成される円筒状の側壁部に沿って配置して
ある蒸気発生器であって、 前記蒸発管を、前記側壁部に沿った円筒面に沿って狭い
間隙で配列して円筒状水管群を形成し、その円筒状水管
群の隣接する蒸発管同士の間隙を熱源ガスを外方に向け
て通流する径方向流路として形成してある蒸気発生器。
An upper header and a lower header are provided at the top and bottom, an upper end is connected to the upper header, and a lower end is connected to the lower header.
A steam generator arranged along a cylindrical side wall formed in a vertical direction, wherein the evaporating pipes are arranged with a narrow gap along a cylindrical surface along the side wall, and a cylindrical water pipe is provided. A steam generator in which a group is formed and a gap between adjacent evaporating tubes of the cylindrical water tube group is formed as a radial flow path through which a heat source gas flows outward.
【請求項2】 前記円筒状水管群に沿って前記側壁部と
の間で前記熱源ガスを前記円筒状水管群の外周に沿って
出口部に導く外周流路を形成し、その外周流路に臨む前
記蒸発管の外面を、前記熱源ガスとの接触伝熱を促進す
る接触伝熱部として構成してある請求項1記載の蒸気発
生器。
2. An outer peripheral flow path is formed between the side walls along the cylindrical water pipe group to guide the heat source gas to an outlet along the outer circumference of the cylindrical water pipe group. The steam generator according to claim 1, wherein an outer surface of the facing evaporating tube is configured as a contact heat transfer unit that promotes contact heat transfer with the heat source gas.
【請求項3】 上下に上部ヘッダと下部ヘッダとを設
け、上端部を前記上部ヘッダに接続し、下端部を前記下
部ヘッダに接続して、縦方向に設けた複数の蒸発管を、
上下方向に形成される円筒状の側壁部に沿って配置する
と共に、前記配列された蒸発管の内側空間を燃焼室に構
成して、前記燃焼室内に向けて火炎を形成する燃焼器を
配置してある竪型水管ボイラであって、 前記蒸発管を、前記側壁部に沿う単一の円筒面に沿って
隣接するもの同士の間隙を狭く配列した円筒状水管群を
形成し、前記燃焼器を天井部に配置して下方に向けて火
炎を形成するように構成し、前記側壁部の一側方に前記
燃焼器で生成する燃焼ガスを排出する排ガス出口を設
け、前記排ガス出口近傍の蒸発管は密接配置すると共
に、その他の部位に配置する蒸発管の間隙を、前記燃焼
ガスが前記側壁部に向かう外向きの径方向流路として形
成してある竪型水管ボイラ。
3. An upper header and a lower header are provided at the top and bottom, an upper end is connected to the upper header, and a lower end is connected to the lower header.
Along with the cylindrical side wall formed in the vertical direction, a combustor that forms a flame toward the combustion chamber by forming a space inside the arranged evaporator tubes as a combustion chamber is disposed. A vertical water tube boiler, wherein the evaporating tubes are formed into a group of cylindrical water tubes in which a gap between adjacent ones of the evaporating tubes is narrowed along a single cylindrical surface along the side wall portion. An exhaust gas outlet for discharging combustion gas generated in the combustor is provided on one side of the side wall so as to be arranged on the ceiling to form a flame downward, and an evaporating pipe near the exhaust gas outlet is provided. Is a vertical water tube boiler which is closely arranged and has a gap between evaporating tubes arranged at other portions as an outward radial flow path for the combustion gas toward the side wall portion.
【請求項4】 前記円筒状水管群と前記側壁部との間
に、前記径方向流路から流出した燃焼ガスを、前記排ガ
ス出口に向けて周方向に導く外周流路を形成し、前記外
周流路に臨む蒸発管の外面を、前記燃焼ガスとの接触伝
熱を促進する接触伝熱部として構成してある請求項3記
載の竪型水管ボイラ。
4. An outer peripheral flow path is formed between the cylindrical water pipe group and the side wall to guide a combustion gas flowing out of the radial flow path in a circumferential direction toward the exhaust gas outlet. 4. The vertical water tube boiler according to claim 3, wherein an outer surface of the evaporator tube facing the flow path is configured as a contact heat transfer unit for promoting contact heat transfer with the combustion gas.
JP2000165596A 2000-06-02 2000-06-02 Steam generator and vertical water tube boiler Pending JP2001349502A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000165596A JP2001349502A (en) 2000-06-02 2000-06-02 Steam generator and vertical water tube boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000165596A JP2001349502A (en) 2000-06-02 2000-06-02 Steam generator and vertical water tube boiler

Publications (1)

Publication Number Publication Date
JP2001349502A true JP2001349502A (en) 2001-12-21

Family

ID=18669045

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000165596A Pending JP2001349502A (en) 2000-06-02 2000-06-02 Steam generator and vertical water tube boiler

Country Status (1)

Country Link
JP (1) JP2001349502A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102606236A (en) * 2012-03-22 2012-07-25 深圳市炬能生物质气化科技有限公司 Garbage disposal waste heat power generation system with internal steam pipe

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102606236A (en) * 2012-03-22 2012-07-25 深圳市炬能生物质气化科技有限公司 Garbage disposal waste heat power generation system with internal steam pipe

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