JP2008300304A - Fuel cell power generation system - Google Patents

Fuel cell power generation system Download PDF

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JP2008300304A
JP2008300304A JP2007147592A JP2007147592A JP2008300304A JP 2008300304 A JP2008300304 A JP 2008300304A JP 2007147592 A JP2007147592 A JP 2007147592A JP 2007147592 A JP2007147592 A JP 2007147592A JP 2008300304 A JP2008300304 A JP 2008300304A
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fuel cell
cooling water
power generation
cell body
generation system
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Takayuki Shinohara
隆之 篠原
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Toshiba Corp
Toshiba Energy Systems and Solutions Corp
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Toshiba Corp
Toshiba Fuel Cell Power Systems Corp
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    • 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

<P>PROBLEM TO BE SOLVED: To provide a fuel cell power generation system in which an amount of moisture in offgas exhausted from a fuel cell body flowing into a reformer burner is reduced in a simple and economical composition. <P>SOLUTION: The fuel cell power generation system has a fuel treatment unit 2, a fuel cell body, an offgas supplying passage 8 for guiding the offgas exhausted from an anode directly to a reformer burner 3 on an upward slope, and a cooling water flowing passage 7 which circulates a cooling water from outside of the fuel cell body 1 to the inside of the fuel cell body 1. The fuel cell body 1 includes an anode separator made of a porous material, and a condensed water generated in the offgas supplying passage 8 is made to flow into the cooling water flowing passage 7 through the anode separator. The cooling water flowing passage 7 has a tank 4 for storing the cooling water to be supplied to the fuel cell body 1 and a cooling water pump 6 for sucking and sending the cooling water coming through the anode separator to the tank 4. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

この発明は、燃料電池発電システムに関し、特に、改質器バーナを有する燃料処理装置を備えた燃料電池発電システムに関する。   The present invention relates to a fuel cell power generation system, and more particularly to a fuel cell power generation system including a fuel processing device having a reformer burner.

外部から供給される都市ガスやLPG(液化天然ガス)に代表される炭化水素系燃料を水素リッチなガスに改質させる燃料処理装置、および、燃料処理装置で得られた水素リッチなガスと酸素とを反応させ直流電力を作る燃料電池本体を含む燃料電池発電システムが知られている。このシステムにおいて、燃料電池本体のアノード極からは燃料電池本体内部で消費されなかった残余の燃料ガス(オフガス)が排出される。そのオフガスは、燃料処理装置内にある改質器の反応熱供給用の熱供給手段として備えられている改質器バーナに供給され、外部から供給される空気とにより燃焼が行われる。   A fuel processing device for reforming a hydrocarbon-based fuel represented by city gas or LPG (liquefied natural gas) supplied from the outside into a hydrogen-rich gas, and a hydrogen-rich gas and oxygen obtained by the fuel processing device There is known a fuel cell power generation system including a fuel cell main body that generates a DC power by reacting with. In this system, the remaining fuel gas (off gas) that has not been consumed inside the fuel cell body is discharged from the anode electrode of the fuel cell body. The off gas is supplied to a reformer burner provided as heat supply means for supplying reaction heat of the reformer in the fuel processing apparatus, and is combusted by air supplied from the outside.

当該オフガスは燃料電池本体の電気化学反応により生成される水を主とした水分を含んでいるが、その水分が改質器バーナでの燃焼性を悪化させる要因となる。そのため、燃料電池本体のアノード極と改質器バーナの間に水分を除去するための装置、および、除去された水分(凝縮水)を水分除去装置から排出するための装置が必要となっていた(特許文献1および特許文献2参照)。
特許第2656262号公報 特開2006−147264号公報
The off gas contains water mainly composed of water generated by the electrochemical reaction of the fuel cell body, and the water becomes a factor that deteriorates the combustibility in the reformer burner. Therefore, a device for removing moisture between the anode electrode of the fuel cell main body and the reformer burner and a device for discharging the removed moisture (condensed water) from the moisture removing device are required. (See Patent Document 1 and Patent Document 2).
Japanese Patent No. 2656262 JP 2006-147264 A

従来の燃料電池発電システムにおいては、システムの簡素化、コンパクト化およびコストダウン実現のためにつぎのような課題があった。すなわち、従来の燃料電池発電システムにおいては、アノード極から排出されるオフガスは燃料電池本体から下り勾配でアノード極−凝縮水タンク配管により凝縮水タンクに供給される。凝縮水タンクは熱交換部を備え、オフガス中に含まれる水分を凝縮させる。凝縮水は水分除去装置によりタンクに排出される。水分を除去されたオフガスは凝縮水タンクから上り勾配で凝縮水タンク−改質器バーナ配管により改質器バーナに供給される。また、前記熱交換部に冷媒を供給する手段として冷媒ポンプと冷媒供給路が備えられる。   The conventional fuel cell power generation system has the following problems in order to simplify the system, make it compact, and realize cost reduction. That is, in the conventional fuel cell power generation system, the off-gas discharged from the anode electrode is supplied to the condensed water tank through the anode electrode-condensed water tank pipe in a descending gradient from the fuel cell body. The condensed water tank is provided with a heat exchanging unit and condenses moisture contained in the offgas. Condensed water is discharged into the tank by a moisture removing device. The off gas from which moisture has been removed is supplied to the reformer burner from the condensate water tank in an ascending gradient through a condensate water tank-reformer burner pipe. In addition, a refrigerant pump and a refrigerant supply path are provided as means for supplying the refrigerant to the heat exchange unit.

このような構成のシステムにおいては付帯機器が多く、また、熱交換部の冷媒供給量の制御などシステムが煩雑となってしまう。また、付帯機器の設置スペース確保、配管の勾配確保のためにパッケージのコンパクト化の面でも問題があった。さらに、部品点数が多い中で、オフガス流通路については可燃ガスに対する規制のためにステンレス鋼製としなければならず、コストアップの要因となっている。   In the system having such a configuration, there are many auxiliary devices, and the system becomes complicated, such as control of the amount of refrigerant supplied to the heat exchange unit. In addition, there was a problem in terms of downsizing the package in order to secure the installation space for the incidental equipment and the slope of the piping. Furthermore, with a large number of parts, the off-gas flow passage must be made of stainless steel due to restrictions on combustible gas, which increases costs.

本発明は上記課題を解決するものであって、燃料電池本体から排出されるオフガス中の水分が改質器バーナに流入する量を低減するための簡素で安価な構成を提供することを目的とする。   The present invention solves the above-described problem, and an object thereof is to provide a simple and inexpensive configuration for reducing the amount of moisture in the off-gas discharged from the fuel cell main body flowing into the reformer burner. To do.

上記目的を達成するために、本発明に係る燃料電池発電システムは、改質器バーナを有して炭化水素系燃料を水素リッチなガスに改質させる燃料処理装置と、アノード極およびカソード極を有し、酸素と前記燃料処理装置で得られた水素リッチなガスとを反応させて直流電力を作る燃料電池本体と、前記アノード極から排出されるオフガスを上り勾配で前記改質器バーナに直接導くオフガス供給路と、を有することを特徴とする。   In order to achieve the above object, a fuel cell power generation system according to the present invention comprises a fuel treatment device having a reformer burner for reforming a hydrocarbon-based fuel into a hydrogen-rich gas, an anode electrode and a cathode electrode. A fuel cell main body that generates direct-current power by reacting oxygen and the hydrogen-rich gas obtained in the fuel processing apparatus, and off-gas discharged from the anode electrode directly to the reformer burner in an upward gradient. And an off-gas supply path for guiding.

本発明によれば、燃料電池本体から排出されるオフガス中の水分が改質器バーナに流入する量を、簡素で安価な構成によって低減することができる。   ADVANTAGE OF THE INVENTION According to this invention, the quantity in which the water | moisture content in the off gas discharged | emitted from a fuel cell main body flows in into a reformer burner can be reduced with a simple and cheap structure.

図1および図2を用いて本発明に係る燃料電池発電システムの一実施形態を説明する。図1は本発明に係る燃料電池発電システムの一実施形態の構成を示すブロック系統図であり、図2は図1の燃料電池発電システムにおける燃料電池本体の燃料電池スタックの断面の一部を示す断面図である。   An embodiment of a fuel cell power generation system according to the present invention will be described with reference to FIGS. 1 and 2. FIG. 1 is a block system diagram showing a configuration of an embodiment of a fuel cell power generation system according to the present invention, and FIG. 2 shows a part of a cross section of a fuel cell stack of a fuel cell main body in the fuel cell power generation system of FIG. It is sectional drawing.

燃料電池本体1は、図2に示すような、単位電池21を複数段に積み重ねた燃料電池スタックで構成されている。単位電池21は、膜電極複合体(MEA)28と、これをはさんで配置されるアノードセパレータ25およびカソードセパレータ26とからなる。膜電極複合体28は、中央に配置された固体高分子膜22と、これをはさむアノード触媒層23aおよびカソード触媒層24aとからなり、その内部にアノード極23およびカソード極24が形成されている。   The fuel cell main body 1 is composed of a fuel cell stack in which unit cells 21 are stacked in a plurality of stages as shown in FIG. The unit cell 21 includes a membrane electrode assembly (MEA) 28 and an anode separator 25 and a cathode separator 26 that are disposed therebetween. The membrane electrode assembly 28 includes a solid polymer membrane 22 disposed in the center, and an anode catalyst layer 23a and a cathode catalyst layer 24a sandwiching the membrane, and an anode electrode 23 and a cathode electrode 24 are formed therein. .

アノードセパレータ25のアノード極23に接する部分に燃料ガス流通路23cが形成されている。また、カソードセパレータ26のカソード極24に接する部分に酸化剤ガス流通路24cが形成されている。さらに、カソードセパレータ26のアノードセパレータ25に隣接する部分には電池内冷却水流通路27cが形成されている。アノードセパレータ25およびカソードセパレータ26は多孔質体からできている。   A fuel gas flow passage 23 c is formed in a portion of the anode separator 25 that is in contact with the anode electrode 23. An oxidant gas flow passage 24c is formed in a portion of the cathode separator 26 that is in contact with the cathode electrode 24. Further, an in-battery cooling water flow passage 27 c is formed in a portion of the cathode separator 26 adjacent to the anode separator 25. The anode separator 25 and the cathode separator 26 are made of a porous material.

燃料ガス流通路23cには、燃料処理装置2(図1参照)で処理された水素を含む燃料ガスが供給される。また、酸化剤ガス流通路24cには空気などの酸化剤ガスが供給される。   A fuel gas containing hydrogen processed by the fuel processing device 2 (see FIG. 1) is supplied to the fuel gas flow passage 23c. An oxidant gas such as air is supplied to the oxidant gas flow passage 24c.

また、電池内冷却水流通路27cには、図1に示す冷却水流通路7を通して冷却水が供給され、この冷却水を循環することにより燃料電池本体1の冷却が行なわれる。冷却水流通路7は冷却水ポンプ6およびタンク4を経て循環するように構成されている。ここで、電池内冷却水流通路27cの下流側の冷却水流通路7に冷却水ポンプ6が配置され、電池内冷却水流通路27c内の圧力が負圧に保たれている。   Further, the cooling water flow passage 27c is supplied with cooling water through the cooling water flow passage 7 shown in FIG. 1, and the cooling of the fuel cell main body 1 is performed by circulating this cooling water. The cooling water flow passage 7 is configured to circulate through the cooling water pump 6 and the tank 4. Here, the cooling water pump 6 is disposed in the cooling water flow passage 7 on the downstream side of the in-battery cooling water flow passage 27c, and the pressure in the in-battery cooling water flow passage 27c is maintained at a negative pressure.

アノード極23より排出されるオフガスはアノード極23から、直接上り勾配でオフガス供給路8により改質器バーナ3に供給される。   The off gas discharged from the anode electrode 23 is directly supplied from the anode electrode 23 to the reformer burner 3 through the off gas supply path 8 in an upward gradient.

アノード極23と改質器バーナ3の間で発生した凝縮水は、重力によってオフガス供給路8を逆流してアノード極23に流れ落ちる。アノード極23に流れ込んだ凝縮水は燃料電池本体1内の多孔質材料11を介して負圧状態となっている電池内冷却水流通路27cへ流れ、さらに冷却水流通路7へ流れることにより電池本体1から取り除かれる。   Condensed water generated between the anode 23 and the reformer burner 3 flows backward to the anode 23 through the off-gas supply path 8 due to gravity. The condensed water flowing into the anode electrode 23 flows into the in-battery cooling water flow passage 27c that is in a negative pressure state through the porous material 11 in the fuel cell main body 1, and further flows into the cooling water flow passage 7 to thereby cause the battery main body 1 to flow. Removed from.

具体的には、正圧である燃料ガス流通路23c内の凝縮水が多孔質材料で構成されるアノードセパレータ25を介し燃料ガス流通路23cと隣り合う電池内冷却水流通路27c内へ取り除かれる。   Specifically, the condensed water in the fuel gas flow passage 23c having a positive pressure is removed into the in-battery cooling water flow passage 27c adjacent to the fuel gas flow passage 23c through the anode separator 25 made of a porous material.

上記の構成をとることにより、凝縮水排出のための凝縮水タンクなどの付帯設備を用いることなく、改質器バーナ3での燃焼性を良好に保つことができる。その結果、燃料電池発電システムにおけるシステムの簡素化、コンパクト化およびコストダウンの実現が可能となる。   By adopting the above configuration, the combustibility in the reformer burner 3 can be kept good without using incidental equipment such as a condensed water tank for discharging condensed water. As a result, the system in the fuel cell power generation system can be simplified, downsized, and cost can be reduced.

本発明に係る燃料電池発電システムの一実施形態の構成を示すブロック系統図である。1 is a block system diagram showing a configuration of an embodiment of a fuel cell power generation system according to the present invention. 図1の燃料電池発電システムにおける燃料電池本体の燃料電池スタックの断面の一部を示す断面図である。FIG. 2 is a cross-sectional view showing a part of a cross section of a fuel cell stack of a fuel cell main body in the fuel cell power generation system of FIG. 1.

符号の説明Explanation of symbols

1 ・・・ 燃料電池本体
2 ・・・ 燃料処理装置
3 ・・・ 改質器バーナ
4 ・・・ タンク
6 ・・・ 冷却水ポンプ
7 ・・・ 冷却水流通路
8 ・・・ オフガス供給路
11 ・・・ 多孔質材料
12 ・・・ 凝縮水
21 ・・・ 単位電池
22 ・・・ 固体高分子膜
23 ・・・ アノード極
23a ・・・ アノード触媒層
23c ・・・ 燃料ガス流通路
24 ・・・ カソード極
24a ・・・ カソード触媒層
24c ・・・ 酸化剤ガス流通路
25 ・・・ アノードセパレータ
26 ・・・ カソードセパレータ
27c ・・・ 電池内冷却水流通路
28 ・・・ 膜電極複合体(MEA)
DESCRIPTION OF SYMBOLS 1 ... Fuel cell main body 2 ... Fuel processing apparatus 3 ... Reformer burner 4 ... Tank 6 ... Cooling water pump 7 ... Cooling water flow path 8 ... Off gas supply path 11・ ・ Porous material 12 ・ ・ ・ Condensed water 21 ・ ・ ・ Unit battery 22 ・ ・ ・ Solid polymer membrane 23 ・ ・ ・ Anode electrode 23 a ・ ・ ・ Anode catalyst layer 23 c ・ ・ ・ Fuel gas flow passage 24 ・ ・ ・Cathode electrode 24a ... Cathode catalyst layer 24c ... Oxidant gas flow passage 25 ... Anode separator 26 ... Cathode separator 27c ... In-battery cooling water flow passage 28 ... Membrane electrode assembly (MEA)

Claims (3)

改質器バーナを有して炭化水素系燃料を水素リッチなガスに改質させる燃料処理装置と、
アノード極およびカソード極を有し、酸素と前記燃料処理装置で得られた水素リッチなガスとを反応させて直流電力を作る燃料電池本体と、
前記アノード極から排出されるオフガスを上り勾配で前記改質器バーナに直接導くオフガス供給路と、
を有することを特徴とする燃料電池発電システム。
A fuel processor having a reformer burner for reforming a hydrocarbon-based fuel into a hydrogen-rich gas; and
A fuel cell body having an anode electrode and a cathode electrode, which reacts oxygen with a hydrogen-rich gas obtained by the fuel processing device to produce DC power;
An off-gas supply path for directing off-gas discharged from the anode electrode directly to the reformer burner in an upward gradient;
A fuel cell power generation system comprising:
前記燃料電池本体の外部からの冷却水を前記燃料電池本体内に循環させる冷却水流通路をさらに有し、
前記燃料電池本体は、多孔質材料からなるアノードセパレータを備え、
前記オフガス供給路で発生した凝縮水が前記アノードセパレータを通って前記冷却水流通路に流入するように構成されていること、を特徴とする請求項1に記載の燃料電池発電システム。
A cooling water flow passage for circulating cooling water from the outside of the fuel cell body into the fuel cell body;
The fuel cell body includes an anode separator made of a porous material,
2. The fuel cell power generation system according to claim 1, wherein the condensed water generated in the off-gas supply path is configured to flow into the cooling water flow path through the anode separator.
前記冷却水流通路は、前記燃料電池本体に供給される冷却水を溜めるタンクと、前記アノードセパレータを通った冷却水を吸引して前記タンクに送る冷却水ポンプと、を有すること、を特徴とする請求項2に記載の燃料電池発電システム。   The cooling water flow passage has a tank for storing cooling water supplied to the fuel cell main body, and a cooling water pump that sucks the cooling water that has passed through the anode separator and sends the cooling water to the tank. The fuel cell power generation system according to claim 2.
JP2007147592A 2007-06-04 2007-06-04 Fuel cell power generation system Pending JP2008300304A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011113918A (en) * 2009-11-30 2011-06-09 Toshiba Corp Fuel cell system

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6482464A (en) * 1987-09-25 1989-03-28 Toshiba Corp Power generating facility for fuel cell
JP2003151597A (en) * 2001-11-08 2003-05-23 Nissan Motor Co Ltd Fuel cell system
JP2006236599A (en) * 2005-02-22 2006-09-07 Mitsubishi Materials Corp Water recovery method for fuel cell power generator

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6482464A (en) * 1987-09-25 1989-03-28 Toshiba Corp Power generating facility for fuel cell
JP2003151597A (en) * 2001-11-08 2003-05-23 Nissan Motor Co Ltd Fuel cell system
JP2006236599A (en) * 2005-02-22 2006-09-07 Mitsubishi Materials Corp Water recovery method for fuel cell power generator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011113918A (en) * 2009-11-30 2011-06-09 Toshiba Corp Fuel cell system

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