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JPH0571602U - Boiler structure - Google Patents

Boiler structure

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Publication number
JPH0571602U
JPH0571602U JP1745992U JP1745992U JPH0571602U JP H0571602 U JPH0571602 U JP H0571602U JP 1745992 U JP1745992 U JP 1745992U JP 1745992 U JP1745992 U JP 1745992U JP H0571602 U JPH0571602 U JP H0571602U
Authority
JP
Japan
Prior art keywords
boiler
pressure vessel
vertical cylindrical
fluidized bed
cylindrical pressure
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
JP1745992U
Other languages
Japanese (ja)
Inventor
忍 中村
佳満 積田
Original Assignee
石川島播磨重工業株式会社
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 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP1745992U priority Critical patent/JPH0571602U/en
Publication of JPH0571602U publication Critical patent/JPH0571602U/en
Pending legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Abstract

(57)【要約】 【目的】 垂直円筒形圧力容器にに対するボイラの収納
効率を高められて垂直円筒形圧力容器の小型化を図り得
るボイラ構造を提供する。 【構成】 菱形のボイラブロック4を3個組合わせて、
上方から見て6個の角を有する六角形状に流動層ボイラ
2炉壁の外壁3を形成し、流動層ボイラ2を垂直円筒形
圧力容器5に同軸方向に収納する。従って流動層ボイラ
2の垂直円筒形圧力容器5への収納効率を高められて、
該垂直円筒形圧力容器5の小型化を図り得る。
(57) [Summary] [PROBLEMS] To provide a boiler structure capable of miniaturizing a vertical cylindrical pressure vessel by increasing the storage efficiency of the boiler in the vertical cylindrical pressure vessel. [Composition] Combining three diamond-shaped boiler blocks 4
An outer wall 3 of a furnace wall of a fluidized bed boiler 2 is formed in a hexagonal shape having six corners when viewed from above, and the fluidized bed boiler 2 is housed in a vertical cylindrical pressure vessel 5 coaxially. Therefore, the storage efficiency of the fluidized bed boiler 2 in the vertical cylindrical pressure vessel 5 can be increased,
The vertical cylindrical pressure vessel 5 can be miniaturized.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は、石炭利用火力発電において、環境保全と経済性の両立をめざして開 発されている加圧流動層複合発電及び石炭ガス化複合発電システムに用いられる ボイラを対称とするもので、加圧操業ボイラに対し圧力バランスをとり保護する ためにボイラを収納する垂直円筒形圧力容器に対する、ボイラの占める割合を大 きくして、即ち収納効率を高めて垂直円筒形圧力容器の径を小さくしボイラ設備 の小型化を図ってスペースの有効利用を図り得るボイラ構造に関するものである 。 In the present invention, in the coal-fired thermal power generation, the boiler used for the pressurized fluidized bed combined cycle power generation and the coal gasification combined cycle power generation system, which has been developed with the aim of achieving both environmental protection and economic efficiency, is symmetrical. In order to balance and protect the pressure operation boiler, the ratio of the boiler to the vertical cylindrical pressure vessel that stores the boiler is increased, that is, the storage efficiency is increased and the diameter of the vertical cylindrical pressure vessel is reduced to reduce the boiler. The present invention relates to a boiler structure that can reduce the size of equipment and make effective use of space.

【0002】[0002]

【従来の技術】[Prior Art]

現在、石炭専焼火力発電において、環境保全と経済性の両立をめざして開発さ れている加圧流動層複合発電及び石炭ガス化複合発電システムが、熱効率が高く 且つ環境汚染物質を発生しにくく、最適であるとして種々検討されている。 Currently, in the coal-fired thermal power generation, the pressurized fluidized bed combined cycle power generation and coal gasification combined cycle power generation system, which have been developed with the aim of achieving both environmental protection and economic efficiency, have high thermal efficiency and are less likely to generate environmental pollutants. Various studies have been conducted to find that it is optimal.

【0003】 加圧流動層ボイラは、加圧流動層複合発電に利用されるボイラであり、流動層 ボイラを圧力容器に収納して加圧条件下で運転するようにしたものであり、流動 層ボイラで発生した蒸気を蒸気タービンに導いて発電することに加え、流動層ボ イラで発生した排ガスを利用しガスタービンを回して発電を行ったり、コンプレ ッサを駆動したりすることができるので、高い熱効率が得られると共に、燃焼温 度が低く且つ排ガスの内部滞留時間が長いので、燃料と共に脱硫剤を供給するこ とにより、イオウ酸化物及び窒素酸化物の発生量の低減化、並びに高い熱効率に より、設備の小型化、等を図ることができるものであると期待され、検討されて いるものである。又、石炭ガス化複合発電に利用されるものとしては粗ガスクー ラがあり、粗ガスクーラは、加圧下でガスとの対流伝熱による熱交換を行なうボ イラである。The pressurized fluidized bed boiler is a boiler used in the pressurized fluidized bed combined cycle power generation, in which the fluidized bed boiler is housed in a pressure vessel and operated under pressurized conditions. In addition to guiding the steam generated in the boiler to a steam turbine to generate electricity, the exhaust gas generated in the fluidized bed boiler can be used to rotate the gas turbine to generate electricity and drive the compressor. In addition to high thermal efficiency, low combustion temperature and long internal residence time of exhaust gas, supply of desulfurizing agent together with fuel reduces the amount of sulfur oxides and nitrogen oxides generated and increases It is expected and considered that the equipment can be downsized due to its thermal efficiency. Also, there is a crude gas cooler that is used for combined coal gasification combined cycle power generation, and the crude gas cooler is a boiler that performs heat exchange by convective heat transfer with gas under pressure.

【0004】 これらのうち、現在、検討が進められている加圧流動層ボイラを例として図4 及び図5を参照しつつ説明する。Of these, a pressurized fluidized bed boiler currently under study will be described as an example with reference to FIGS. 4 and 5.

【0005】 図中11は加圧流動層ボイラであり、該加圧流動層ボイラ11は、垂直円筒形 圧力容器12と、上方から見て四角形状のボイラブロック14を適数(図では1 個)備えていて前記垂直円筒形圧力容器12に収納されて加圧燃焼を行い得るよ うになっている流動層ボイラ13と、該流動層ボイラ13からダクトを経て排出 されたボイラ排ガス中の灰を除去する集塵器(図示せず)とを備えている。図中 15は各ボイラブロック14に備えられた管寄せである。Reference numeral 11 in the figure is a pressurized fluidized bed boiler, and the pressurized fluidized bed boiler 11 has a vertical cylindrical pressure vessel 12 and a proper number of square-shaped boiler blocks 14 when viewed from above (one in the figure). ), Which is housed in the vertical cylindrical pressure vessel 12 and is capable of performing pressure combustion, and ash in the boiler exhaust gas discharged from the fluidized bed boiler 13 through a duct. And a dust collector (not shown) for removal. In the figure, reference numeral 15 is a header provided in each boiler block 14.

【0006】[0006]

【考案が解決しようとする課題】[Problems to be solved by the device]

しかしながら、上述の如く垂直円筒形圧力容器12に流動層ボイラ13を収納 した加圧流動層ボイラ11にあっては、流動層ボイラ13が上方から見て四角形 状であるので、垂直円筒形圧力容器12に対する収納効率が悪く、該垂直円筒形 圧力容器12は流動層ボイラ13の大きさに比し大型にならざるをえず、従って 垂直円筒形圧力容器12の大型化に伴いボイラ設備自体も大型になってスペース の有効利用の面から見て不具合であった。 However, in the pressurized fluidized bed boiler 11 in which the fluidized bed boiler 13 is housed in the vertical cylindrical pressure vessel 12 as described above, since the fluidized bed boiler 13 has a rectangular shape when viewed from above, the vertical cylindrical pressure vessel The vertical cylindrical pressure vessel 12 is inevitably large in size as compared with the size of the fluidized bed boiler 13 because the storage efficiency of the vertical cylindrical pressure vessel 12 is large. It was a problem from the viewpoint of effective use of space.

【0007】 本考案は上述の実情に鑑み、垂直円筒形圧力容器に対するボイラの収納効率を 高くし、垂直円筒形圧力容器の小型化、ひいてはボイラ設備自体の小型化も図り 得られ、スペースの有効利用をなし得るボイラ構造を提供することを目的として なしたものである。In view of the above situation, the present invention can improve the storage efficiency of the boiler in the vertical cylindrical pressure vessel, downsize the vertical cylindrical pressure vessel, and in turn, downsize the boiler equipment itself, and save space. The purpose is to provide a boiler structure that can be used.

【0008】[0008]

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

本考案は、垂直円筒形圧力容器に収納するボイラ炉壁の外壁を、上方から見て 5個以上の角を有する多角形状に形成し、前記ボイラ炉壁内にループ管を収納し たことを特徴とするボイラ構造、にかかるものである。 According to the present invention, the outer wall of the boiler furnace wall to be housed in the vertical cylindrical pressure vessel is formed in a polygonal shape having five or more corners when viewed from above, and the loop tube is housed in the boiler furnace wall. It relates to a characteristic boiler structure.

【0009】[0009]

【作用】[Action]

垂直円筒形圧力容器に収納するボイラ炉壁の外壁を、上方から見て5個以上の 角を有する多角形状に形成したことにより、垂直円筒形圧力容器に対するボイラ の占める割合を大きくできて垂直円筒形圧力容器の径を小さくでき、垂直円筒形 圧力容器の小型化を図り得る。 By forming the outer wall of the boiler furnace wall to be housed in the vertical cylindrical pressure vessel into a polygonal shape with five or more corners when viewed from above, the ratio of the boiler to the vertical cylindrical pressure vessel can be increased and the vertical cylinder The diameter of the pressure vessel can be reduced, and the vertical cylindrical pressure vessel can be miniaturized.

【0010】[0010]

【実施例】【Example】

以下、図1及び図2に基づき本考案の実施例を、加圧流動層ボイラを例にとり 説明する。 Hereinafter, an embodiment of the present invention will be described with reference to FIGS. 1 and 2 by taking a pressurized fluidized bed boiler as an example.

【0011】 加圧流動層ボイラ1において、流動層ボイラ2炉壁の外壁3を上方から見て6 個の角を有する六角形状になるように菱形のボイラブロック4を三個組合わせて 構成し、斯かる流動層ボイラ2を同軸状に垂直円筒形圧力容器5に収納する。図 中6は水平ループ管、7は各ボイラブロック4に備えられた管寄せ、8は各ボイ ラブロック4を仕切る仕切壁である。In the pressurized fluidized bed boiler 1, three diamond-shaped boiler blocks 4 are combined so that the outer wall 3 of the furnace wall of the fluidized bed boiler 2 has a hexagonal shape with six corners when viewed from above. The fluidized bed boiler 2 is housed coaxially in the vertical cylindrical pressure vessel 5. In the figure, 6 is a horizontal loop pipe, 7 is a pipe holder provided in each boiler block 4, and 8 is a partition wall for partitioning each boiler block 4.

【0012】 具体的に図3(A)(B)に基づき前記の如く構成した流動層ボイラ2の垂直 円筒形圧力容器5に対する占有面積を従来の場合と比較して述べる。説明上、垂 直円筒形圧力容器5に流動層ボイラ2炉壁の外壁3が、又垂直円筒形圧力容器1 2に流動層ボイラ13炉壁の外壁が内接しているものとし、更に該流動層ボイラ 13炉壁の外壁を正方形であると仮定して述べる。The occupying area of the fluidized bed boiler 2 configured as described above with respect to the vertical cylindrical pressure vessel 5 will be specifically described based on FIGS. 3A and 3B in comparison with the conventional case. For the sake of explanation, it is assumed that the vertical cylindrical pressure vessel 5 is inscribed with the outer wall 3 of the furnace wall of the fluidized bed boiler 2, and the vertical cylindrical pressure vessel 12 is inscribed with the outer wall of the furnace wall of the fluidized bed boiler 13. The description will be made assuming that the outer wall of the single-layer boiler 13 furnace wall is a square.

【0013】 垂直円筒形圧力容器5,12の半径を夫々Rとすると、流動層ボイラ2の軸心 から角までの寸法もRに、又従来の流動層ボイラ13の軸心から角までの寸法も Rになり、従って垂直円筒形圧力容器5に対する流動層ボイラ2の占有面積(図 3(A)の斜線部)は(3/2)31/22(≒2.6R2)となり、又垂直円筒 形圧力容器12に対する流動層ボイラ13の占有面積(図3(B)の斜線部)は 2R2となり、明らかに本考案における垂直円筒形圧力容器5に対する流動層ボ イラ2の占有面積が、従来の上方から見て四角形状の流動層ボイラ13の場合に 比し0.6R2増加していることがわかる。When the radii of the vertical cylindrical pressure vessels 5 and 12 are R, the dimension from the axis of the fluidized bed boiler 2 to the corner is also R, and the dimension from the axis of the conventional fluidized bed boiler 13 to the corner. Also becomes R, and therefore the occupied area of the fluidized bed boiler 2 with respect to the vertical cylindrical pressure vessel 5 (hatched portion in FIG. 3 (A)) is (3/2) 3 1/2 R 2 (≈2.6 R 2 ). Also, the occupied area of the fluidized bed boiler 13 for the vertical cylindrical pressure vessel 12 (the hatched portion in FIG. 3 (B)) is 2R 2 , which clearly indicates the occupied area of the fluidized bed boiler 2 for the vertical cylindrical pressure vessel 5 in the present invention. It can be seen that the area is increased by 0.6R 2 as compared with the case of the conventional fluidized bed boiler 13 having a rectangular shape when viewed from above.

【0014】 従って垂直円筒形圧力容器5に対する流動層ボイラ2の占有面積を大きくでき て、該流動層ボイラ2の大きさに比し垂直円筒形圧力容器5の径を小さくでき小 型化を図り得られ、ボイラ設備の小型化も図り得ると共に、流動層ボイラ2炉壁 の外壁3が上方から見て6個の角を有する六角形になっているので、水平ループ 管5の長手方向長さを等しくできて各ボイラブロック4における熱交換の一様化 を図り得られ、しかも管寄せ7を対称的に配置することができて垂直円筒形圧力 容器5内における圧力バランス上好都合である。Therefore, the occupied area of the fluidized bed boiler 2 with respect to the vertical cylindrical pressure vessel 5 can be increased, and the diameter of the vertical cylindrical pressure vessel 5 can be made smaller than the size of the fluidized bed boiler 2 to achieve downsizing. As a result, the size of the boiler equipment can be reduced, and the outer wall 3 of the fluidized-bed boiler 2 furnace wall is hexagonal with 6 corners when viewed from above. Can be equalized to achieve uniform heat exchange in each boiler block 4, and the headers 7 can be symmetrically arranged, which is convenient for pressure balance in the vertical cylindrical pressure vessel 5.

【0015】 尚、本考案は図示し説明せる実施例にのみ限定されることなく、例えば仕切壁 8,8a,8bを単に省きボイラブロック4,4a,4b相互間を自由空間とし て熱流移動を行い得るようにすること、加圧流動層ボイラ以外の加圧下の熱交換 器に適用すること等は任意であり、その他、本考案の要旨を逸脱しない限り種々 の変更を加え得ることは勿論である。It should be noted that the present invention is not limited to the illustrated and described embodiments, and for example, the partition walls 8, 8a, 8b are simply omitted and the heat flow movement is performed by using the boiler blocks 4, 4a, 4b as free spaces. It is optional to make it possible to apply it, to apply it to a heat exchanger under pressure other than the pressurized fluidized bed boiler, and various modifications can be made without departing from the gist of the present invention. is there.

【0016】[0016]

【考案の効果】[Effect of the device]

以上述べたように本考案のボイラ構造によれば、垂直円筒形圧力容器に対する ボイラの収納効率を大きくできるので、垂直円筒形圧力容器の小型化を図り得ら れ、ボイラ設備の小型化も図り得られてスペースの有効利用をなし得る、等種々 の優れた効果を奏し得る。 As described above, according to the boiler structure of the present invention, the storage efficiency of the boiler in the vertical cylindrical pressure vessel can be increased, so that the vertical cylindrical pressure vessel can be downsized and the boiler equipment can be downsized. Various excellent effects such as the obtained space can be effectively used can be obtained.

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

【図1】本考案のボイラ構造を示す概略平面図にして図
2のIーI方向矢視図である。
FIG. 1 is a schematic plan view showing a boiler structure of the present invention and is a view taken in the direction of arrows II in FIG.

【図2】図1の概略側面図である。FIG. 2 is a schematic side view of FIG.

【図3】垂直円筒形圧力容器に対するボイラの占有状態
を説明するための図であって、(A)は本考案のボイラ
構造における垂直円筒形圧力容器に対するボイラの占有
状態を示す図、(B)は従来のボイラにおける垂直円筒
形圧力容器に対するボイラの占有状態を示す図である。
3A and 3B are views for explaining the occupancy state of the boiler with respect to the vertical cylindrical pressure vessel, FIG. 3A is a diagram showing the occupancy state of the boiler with respect to the vertical cylindrical pressure vessel in the boiler structure of the present invention; [Fig. 4] is a diagram showing a state in which a boiler is occupied by a vertical cylindrical pressure vessel in a conventional boiler.

【図4】現在開発されている加圧流動層ボイラを示す概
略平面図にして図5のIVーIV方向矢視図である。
4 is a schematic plan view showing a currently developed pressurized fluidized bed boiler, which is a view taken in the direction of arrows IV-IV in FIG.

【図5】図4の概略側面図である。5 is a schematic side view of FIG.

【符号の説明】[Explanation of symbols]

1 加圧流動層ボイラ 2,2a,2b 流動層ボイラ 3,3a,3b 外壁 4,4a,4b ボイラブロック 5 垂直円筒形圧力容器 6,6a,6b 水平ループ管 7,7a,7b 管寄せ 8,8a,8b 仕切壁 1 Pressurized fluidized bed boiler 2,2a, 2b Fluidized bed boiler 3,3a, 3b Outer wall 4,4a, 4b Boiler block 5 Vertical cylindrical pressure vessel 6,6a, 6b Horizontal loop pipe 7,7a, 7b Pipe shifter 8, 8a, 8b partition wall

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 垂直円筒形圧力容器に収納するボイラ炉
壁の外壁を、上方から見て5個以上の角を有する多角形
状に形成し、前記ボイラ炉壁内にループ管を収納したこ
とを特徴とするボイラ構造。
1. An outer wall of a boiler furnace wall housed in a vertical cylindrical pressure vessel is formed into a polygonal shape having five or more corners when viewed from above, and a loop pipe is housed in the boiler furnace wall. Characteristic boiler structure.
JP1745992U 1992-02-25 1992-02-25 Boiler structure Pending JPH0571602U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1745992U JPH0571602U (en) 1992-02-25 1992-02-25 Boiler structure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1745992U JPH0571602U (en) 1992-02-25 1992-02-25 Boiler structure

Publications (1)

Publication Number Publication Date
JPH0571602U true JPH0571602U (en) 1993-09-28

Family

ID=11944608

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1745992U Pending JPH0571602U (en) 1992-02-25 1992-02-25 Boiler structure

Country Status (1)

Country Link
JP (1) JPH0571602U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006214712A (en) * 2005-01-07 2006-08-17 Mitsubishi Heavy Ind Ltd Pressurized hot gas cooler
US7803216B2 (en) 2005-12-28 2010-09-28 Mitsubishi Heavy Industries, Ltd. Pressurized high-temperature gas cooler

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006214712A (en) * 2005-01-07 2006-08-17 Mitsubishi Heavy Ind Ltd Pressurized hot gas cooler
JP4599291B2 (en) * 2005-01-07 2010-12-15 三菱重工業株式会社 Pressurized high temperature gas cooler
US7803216B2 (en) 2005-12-28 2010-09-28 Mitsubishi Heavy Industries, Ltd. Pressurized high-temperature gas cooler

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