JPH06349513A - Cylindrical fuel cell module - Google Patents

Cylindrical fuel cell module

Info

Publication number
JPH06349513A
JPH06349513A JP5134681A JP13468193A JPH06349513A JP H06349513 A JPH06349513 A JP H06349513A JP 5134681 A JP5134681 A JP 5134681A JP 13468193 A JP13468193 A JP 13468193A JP H06349513 A JPH06349513 A JP H06349513A
Authority
JP
Japan
Prior art keywords
air
chamber
reaction chamber
air supply
exhaust
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.)
Withdrawn
Application number
JP5134681A
Other languages
Japanese (ja)
Inventor
Katsumi Nagata
勝巳 永田
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP5134681A priority Critical patent/JPH06349513A/en
Publication of JPH06349513A publication Critical patent/JPH06349513A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Abstract

PURPOSE:To improve a utilization factor of air by connecting an air preheating chamber and an air supply tube via an air supply header to perform heat exchange in the air preheating chamber after generation. CONSTITUTION:Plural cell tubes 12 are arranged upward and downward inside a reaction chamber 11, an air exhaust chamber 14 is provided at the lower part thereof and an air preheating chamber 15 is provided at the lower part of the exhaust chamber 14. The preheating chamber 15 to which an air tube 16 to supply air and an air tube 17 to exhaust air are connected is arranged in the reaction chamber 11 along the longitudinal direction of the tubes 12. Air is supplied from the air chamber 16 to the air preheating chamber 15, passed through an air supply tube 18 and an air supply header 19 and led to the upper part of the reaction chamber 11. After used for generation while lowering, air is passed through a ceramics foamer 13 and the air exhaust chamber 14, heat-exchanged in the preheating chamber 15 and exhausted outside. As the quantity of heat in the reaction chamber 11 is used to preheat air, extra one is effectively removed, an air flow rate is decreased accordingly and a utilization factor of air is improved.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、固体電解質型燃料電
池(以下、SOFCと呼ぶ)を有した円筒型燃料電池モ
ジュールに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cylindrical fuel cell module having a solid oxide fuel cell (hereinafter referred to as SOFC).

【0002】[0002]

【従来の技術】図3は、円筒型燃料電池モジュールを示
す。図中の符番1は、内部に複数のセルチューブ2を上
下方向に配置した反応室である。この反応室1の底部に
は、セラミックス発泡体3が配置されている。前記反応
室1の下部には、空気予熱器4を備えた空気予熱室5が
設けられている。前記反応室1及び空気予熱室5には、
前記空気予熱器4に接続した空気排出管6が設けられて
いる。この空気排出管6の上端は開口されており、その
上端は前記反応室1の内壁近くまで延出している。前記
空気予熱器4には、空気を供給する空気管7,空気を排
出する排空気管8が接続されている。
2. Description of the Related Art FIG. 3 shows a cylindrical fuel cell module. Reference numeral 1 in the figure is a reaction chamber in which a plurality of cell tubes 2 are vertically arranged. A ceramic foam 3 is arranged at the bottom of the reaction chamber 1. An air preheating chamber 5 having an air preheater 4 is provided below the reaction chamber 1. In the reaction chamber 1 and the air preheating chamber 5,
An air discharge pipe 6 connected to the air preheater 4 is provided. An upper end of the air discharge pipe 6 is opened, and the upper end thereof extends close to the inner wall of the reaction chamber 1. An air pipe 7 for supplying air and an exhaust air pipe 8 for discharging air are connected to the air preheater 4.

【0003】こうした構成の円筒型燃料電池モジュール
の作用は、次の通りである。空気は、系外よりまず空気
予熱器4に供給された後、〜約700℃に予熱され、セ
ラミックス発泡体3を通って反応室2内へ導かれ、セル
チューブ2を上昇していく。そこで、発電反応のために
消費され、残りの排空気は空気排出管6を通り、空気予
熱器4で導入されてくる空気と熱交換をした後、系外へ
排出される。
The operation of the cylindrical fuel cell module having such a structure is as follows. The air is first supplied to the air preheater 4 from the outside of the system, then preheated to about 700 ° C., introduced into the reaction chamber 2 through the ceramic foam 3, and rises in the cell tube 2. Then, the remaining exhaust air consumed for the power generation reaction passes through the air exhaust pipe 6, exchanges heat with the air introduced in the air preheater 4, and is then exhausted to the outside of the system.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、従来の
円筒型燃料電池モジュールによれば、次に述べる問題点
を有する。即ち、SOFCの場合、反応室内温度を一定
に保つためには反応室内の余分な熱量を排空気として系
外に排出する必要がある。従って、反応室内の熱量を効
果的に除去しない限り、空気流量を一定流量以下には絞
れない(空気利用率が上げられない)ことになる。この
傾向は、第容量化が進む程顕著になる。また、空気排出
管6が1本だけなので、反応室上部付近において空気流
れのアンバランスが生じやすい。
However, the conventional cylindrical fuel cell module has the following problems. That is, in the case of SOFC, in order to keep the temperature in the reaction chamber constant, it is necessary to discharge the excess heat amount in the reaction chamber as exhaust air to the outside of the system. Therefore, unless the amount of heat in the reaction chamber is effectively removed, the air flow rate cannot be reduced below a certain flow rate (the air utilization rate cannot be increased). This tendency becomes more remarkable as the capacity becomes higher. Further, since there is only one air discharge pipe 6, an air flow is likely to be unbalanced near the upper portion of the reaction chamber.

【0005】この発明はこうした事情を考慮してなされ
たもので、反応室内の熱量を空気の予熱に用いることに
より余分な熱量を有効に取り除き、その分空気流量を減
少して空気利用率を向上するとともに、反応室内におけ
る空気流れのアンバランスを緩和でき、更に空気予熱器
の伝熱面積を減少してコンパクト化可能な円筒型燃料電
池モジュールを提供することを目的とする。
The present invention has been made in consideration of such circumstances, and the excess heat amount is effectively removed by using the heat amount in the reaction chamber for preheating the air, and the air flow rate is reduced by that amount to improve the air utilization rate. In addition, it is an object of the present invention to provide a cylindrical fuel cell module that can alleviate the imbalance of the air flow in the reaction chamber and further reduce the heat transfer area of the air preheater to make it compact.

【0006】[0006]

【課題を解決するための手段】この発明は、内部に複数
のセルチューブを上下方向に配置した反応室と、この反
応室の下部に設けられた空気排出室と、この空気排出室
の下部に設けられ,空気を供給する空気管及び空気を排
出する排空気管が夫々接続した空気予熱器と、前記反応
室内に前記セルチューブの長手方向に沿って配置され、
開口された上端部が反応室の上部内壁付近まで延出する
複数の空気供給管と、前記空気予熱器と空気供給管とを
接続する空気供給ヘッダーとを具備することを特徴とす
る円筒型燃料電池モジュールである。
According to the present invention, a reaction chamber having a plurality of cell tubes vertically arranged therein, an air discharge chamber provided in the lower part of the reaction chamber, and a lower part of the air discharge chamber are provided. An air preheater, which is provided with an air pipe for supplying air and an exhaust air pipe for discharging air, respectively, and is arranged along the longitudinal direction of the cell tube in the reaction chamber,
A cylindrical fuel characterized by comprising a plurality of air supply pipes whose opened upper ends extend to the vicinity of the upper inner wall of the reaction chamber, and an air supply header which connects the air preheater and the air supply pipes. It is a battery module.

【0007】この発明においては、熱の輻射効果を促進
するため前記空気供給管を耐熱ガラス製で作ったり、ま
た耐熱ガラス製の空気供給管の内部にセラミックス発泡
体を充填することが考えられる。
In the present invention, it is considered that the air supply pipe is made of heat-resistant glass or the inside of the air supply pipe made of heat-resistant glass is filled with a ceramic foam in order to promote the heat radiation effect.

【0008】[0008]

【作用】この発明において、空気は空気予熱器に供給さ
れ、空気供給ヘッダー及び夫々の空気供給管を通り、反
応室上部に導入され、セルチューブで発電に用いられた
後、下方のセラミック発泡体を通り空気排出室より空気
予熱器で熱交換を行なった後、系外へ排出される。
In the present invention, air is supplied to the air preheater, introduced into the upper part of the reaction chamber through the air supply header and the respective air supply pipes, and is used for power generation in the cell tube, and then the ceramic foam below. After passing through the air exhaust chamber to exchange heat with the air preheater, the air is discharged to the outside of the system.

【0009】[0009]

【実施例】以下、この発明の一実施例に係る円筒型燃料
電池モジュールを図1を参照して説明する。なお、モジ
ュール全体は断熱材(図示せず)により被われて、内部
は一定高温を保つようになっている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A cylindrical fuel cell module according to an embodiment of the present invention will be described below with reference to FIG. In addition, the entire module is covered with a heat insulating material (not shown) so that a constant high temperature is maintained inside.

【0010】図中の符番11は、内部に上側の管板(図示
せず)に取付けられた有底の複数のセルチューブ12を上
下方向に配置した反応室である。この反応室11の底部に
は、セラミックス発泡体13が配置されている。前記反応
室11の下部には、空気排出室14が設けられている。ここ
で、空気排出室14は、後記排空気管の流路と接続されて
いる。この空気排出室14の下部には、流路が交差した空
気予熱器15が設けられている。この空気予熱器15には、
空気を供給する空気管16及び空気を排出する排空気管17
が夫々接続されている。前記反応室11内には、複数の空
気供給管18が前記セルチューブの長手方向に沿って配置
されている。ここで、空気供給管18の両端は開口されて
おり、上端部は反応室11の上部内壁付近まで延出し、下
端部はセラミックス発泡体13まで延出している。また、
前記空気供給管18としては、熱の輻射効果を促進するた
めに図2(A)のように耐熱ガラス製の空気供給管21を
用いたり、あるいは図2(B)のように内部にセラミッ
クス発泡体22を充填した耐熱ガラス製の空気供給管21を
用いることができる。前記空気排出室14内には、前記空
気予熱器15と空気供給管18を接続する空気供給ヘッダー
19が設けられている。ここで、この空気供給ヘッダー19
は前記排空気管17の流路と接続し、前記セラミックス発
泡体13まで延出している。
Reference numeral 11 in the drawing is a reaction chamber in which a plurality of bottomed cell tubes 12 mounted inside an upper tube sheet (not shown) are vertically arranged. At the bottom of the reaction chamber 11, a ceramic foam 13 is arranged. An air exhaust chamber 14 is provided below the reaction chamber 11. Here, the air exhaust chamber 14 is connected to a flow path of an exhaust air pipe described later. Below the air discharge chamber 14, an air preheater 15 whose flow paths intersect is provided. In this air preheater 15,
Air pipe 16 for supplying air and exhaust air pipe 17 for discharging air
Are connected to each other. In the reaction chamber 11, a plurality of air supply pipes 18 are arranged along the longitudinal direction of the cell tube. Here, both ends of the air supply pipe 18 are opened, the upper end extends to the vicinity of the upper inner wall of the reaction chamber 11, and the lower end extends to the ceramic foam 13. Also,
As the air supply pipe 18, an air supply pipe 21 made of heat-resistant glass is used as shown in FIG. 2 (A) in order to promote a heat radiation effect, or a ceramic foam is provided inside as shown in FIG. 2 (B). An air supply tube 21 made of heat resistant glass and filled with the body 22 can be used. An air supply header that connects the air preheater 15 and the air supply pipe 18 in the air discharge chamber 14.
19 are provided. Where this air supply header 19
Is connected to the flow path of the exhaust air pipe 17 and extends to the ceramic foam 13.

【0011】次に、こうした構成の円筒型燃料電池モジ
ュールの作用について説明する。即ち、空気は空気管16
より空気予熱器15に供給され、空気供給ヘッダー19及び
空気供給管18を通り、反応室11内の上部へ導かれる。そ
して、下降しつつ発電に用いられた後、セラミックス発
泡体13,空気排出室14を通り、空気予熱器15で熱交換を
行った後、系外へ排出される。
Next, the operation of the cylindrical fuel cell module having such a structure will be described. That is, the air is the air pipe 16
It is further supplied to the air preheater 15, passes through the air supply header 19 and the air supply pipe 18, and is guided to the upper part in the reaction chamber 11. Then, after being used for power generation while descending, it passes through the ceramic foam 13, the air discharge chamber 14, undergoes heat exchange with the air preheater 15, and is then discharged to the outside of the system.

【0012】このように、上記実施例に係る円筒型モジ
ュールは、上側の管板(図示せず)に取付けられた有底
の複数のセルチューブ12を上下方向に配置した反応室
と、この反応室11の底部に配置されたセラミックス発泡
体13と、前記反応室11の下部に設けられ,空気管16の流
路と接続された空気排出室14と、この空気排出室14の下
部に設けられた空気予熱器15と、この空気予熱器15に接
続された空気管16及び排空気管17と、前記反応室11内に
前記セルチューブの長手方向に沿って配置された複数の
空気供給管18と、前記空気排出室14内に設けられ,前記
空気予熱器15と空気供給管18を接続する空気供給ヘッダ
ー19とを具備した構成になっている。従って、次のよう
な効果を有する。
As described above, the cylindrical module according to the above embodiment has a reaction chamber in which a plurality of bottomed cell tubes 12 attached to an upper tube sheet (not shown) are vertically arranged, and a reaction chamber A ceramic foam body 13 arranged at the bottom of the chamber 11, an air discharge chamber 14 provided in the lower part of the reaction chamber 11 and connected to the flow path of the air pipe 16, and a lower part of the air discharge chamber 14 are provided. Air preheater 15, an air pipe 16 and an exhaust air pipe 17 connected to the air preheater 15, and a plurality of air supply pipes 18 arranged in the reaction chamber 11 along the longitudinal direction of the cell tube. And an air supply header 19 which is provided in the air discharge chamber 14 and connects the air preheater 15 and the air supply pipe 18. Therefore, it has the following effects.

【0013】(1) 反応室11内の熱量を空気の予熱に用い
ることにより、余分な熱量を有効に取り除くことができ
る。その分、空気流量を減少できるので空気利用率が向
上する。その結果、空気供給のための補機動力が減少す
るために全体のシステム効率が向上する。 (2) 空気供給管18を複数本とすることにより、反応室11
内における空気流れのアンバランスを緩和できる。 (3) 空気供給管18内で空気予熱をする分、空気予熱器出
口温度を下げることができるので、空気予熱器15の伝熱
面積が減少し、コンパクト化が可能となる。
(1) By using the heat quantity in the reaction chamber 11 for preheating the air, the excess heat quantity can be effectively removed. As a result, the air flow rate can be reduced and the air utilization rate is improved. As a result, overall system efficiency is improved due to reduced auxiliary power for air supply. (2) By using a plurality of air supply pipes 18, the reaction chamber 11
The imbalance of the air flow inside can be eased. (3) Since the temperature of the air preheater outlet can be lowered by the amount of air preheating in the air supply pipe 18, the heat transfer area of the air preheater 15 is reduced, and the size can be reduced.

【0014】[0014]

【発明の効果】以上詳述したようにこの発明によれば、
反応室内の熱量を空気の予熱に用いることにより余分な
熱量を有効に取り除き、その分空気流量を減少して空気
利用率を向上するとともに、反応室内における空気流れ
のアンバランスを緩和でき、更に空気予熱器の伝熱面積
を減少してコンパクト化可能な円筒型燃料電池モジュー
ルを提供できる。
As described above in detail, according to the present invention,
By using the amount of heat in the reaction chamber to preheat the air, the excess amount of heat is effectively removed, the air flow rate is reduced by that amount, and the air utilization rate is improved, and the imbalance of the air flow in the reaction chamber can be mitigated. It is possible to provide a cylindrical fuel cell module that can be made compact by reducing the heat transfer area of the preheater.

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

【図1】この発明の一実施例に係る円筒型燃料電池モジ
ュールの説明図。
FIG. 1 is an explanatory diagram of a cylindrical fuel cell module according to an embodiment of the present invention.

【図2】図1の円筒型燃料電池モジュールに使用される
空気供給管とは異なる空気供給管の説明図であり、図2
(A)は耐熱ガラス製の空気供給管、図2(B)は内部
にセラミック発泡体を充填した耐熱ガラス製の空気供給
管の説明図。
2 is an explanatory view of an air supply pipe different from the air supply pipe used in the cylindrical fuel cell module of FIG.
(A) is an air supply pipe made of heat-resistant glass, and FIG. 2 (B) is an explanatory view of an air supply pipe made of heat-resistant glass having a ceramic foam filled therein.

【図3】従来の円筒型燃料電池モジュールの説明図。FIG. 3 is an explanatory view of a conventional cylindrical fuel cell module.

【符号の説明】[Explanation of symbols]

11…反応室、 12…セルチューブ、 13,22…
セラミック発泡体、14…空気排出室、 15…空気予熱
器、 16…空気管、17…排空気管、 18,21…
空気供給管、 19…空気供給ヘッダー。
11 ... Reaction chamber, 12 ... Cell tube, 13, 22 ...
Ceramic foam, 14 ... Air exhaust chamber, 15 ... Air preheater, 16 ... Air pipe, 17 ... Exhaust air pipe, 18, 21 ...
Air supply pipe, 19… Air supply header.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 内部に複数のセルチューブを上下方向に
配置した反応室と、この反応室の下部に設けられた空気
排出室と、この空気排出室の下部に設けられ,空気を供
給する空気管及び空気を排出する排空気管が夫々接続し
た空気予熱器と、前記反応室内に前記セルチューブの長
手方向に沿って配置され、開口された上端部が反応室の
上部内壁付近まで延出する複数の空気供給管と、前記空
気予熱器と空気供給管とを接続する空気供給ヘッダーと
を具備することを特徴とする円筒型燃料電池モジュー
ル。
1. A reaction chamber in which a plurality of cell tubes are vertically arranged, an air exhaust chamber provided in a lower portion of the reaction chamber, and an air supply air provided in a lower portion of the air exhaust chamber for supplying air. A pipe and an exhaust air pipe for exhausting air are respectively connected to the air preheater, and are arranged along the longitudinal direction of the cell tube in the reaction chamber, and the opened upper end extends to near the upper inner wall of the reaction chamber. A cylindrical fuel cell module comprising: a plurality of air supply pipes; and an air supply header that connects the air preheater and the air supply pipes.
【請求項2】 前記空気供給管を耐熱ガラス材とし、内
部にセラミックス発泡体を充填した請求項1記載の円筒
型燃料電池モジュール。
2. The cylindrical fuel cell module according to claim 1, wherein the air supply pipe is made of a heat-resistant glass material, and a ceramic foam is filled inside.
JP5134681A 1993-06-04 1993-06-04 Cylindrical fuel cell module Withdrawn JPH06349513A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5134681A JPH06349513A (en) 1993-06-04 1993-06-04 Cylindrical fuel cell module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5134681A JPH06349513A (en) 1993-06-04 1993-06-04 Cylindrical fuel cell module

Publications (1)

Publication Number Publication Date
JPH06349513A true JPH06349513A (en) 1994-12-22

Family

ID=15134088

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5134681A Withdrawn JPH06349513A (en) 1993-06-04 1993-06-04 Cylindrical fuel cell module

Country Status (1)

Country Link
JP (1) JPH06349513A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002280050A (en) * 2001-03-21 2002-09-27 Toto Ltd Fuel cell power generating device
JP2004119239A (en) * 2002-09-27 2004-04-15 Mitsubishi Heavy Ind Ltd Fuel cell-gas turbine power generation equipment and combined cycle power generation equipment
JP2007317544A (en) * 2006-05-26 2007-12-06 Nippon Oil Corp Solid oxide fuel cell system
JP2009238651A (en) * 2008-03-28 2009-10-15 Toho Gas Co Ltd Gas supply-exhaust manifold and solid oxide fuel cell bundle

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002280050A (en) * 2001-03-21 2002-09-27 Toto Ltd Fuel cell power generating device
JP2004119239A (en) * 2002-09-27 2004-04-15 Mitsubishi Heavy Ind Ltd Fuel cell-gas turbine power generation equipment and combined cycle power generation equipment
JP2007317544A (en) * 2006-05-26 2007-12-06 Nippon Oil Corp Solid oxide fuel cell system
JP2009238651A (en) * 2008-03-28 2009-10-15 Toho Gas Co Ltd Gas supply-exhaust manifold and solid oxide fuel cell bundle

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