JPH08321316A - Fuel cell generator - Google Patents

Fuel cell generator

Info

Publication number
JPH08321316A
JPH08321316A JP7126036A JP12603695A JPH08321316A JP H08321316 A JPH08321316 A JP H08321316A JP 7126036 A JP7126036 A JP 7126036A JP 12603695 A JP12603695 A JP 12603695A JP H08321316 A JPH08321316 A JP H08321316A
Authority
JP
Japan
Prior art keywords
gas
fuel
fuel cell
water
power generator
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
JP7126036A
Other languages
Japanese (ja)
Inventor
Shunsuke Oga
俊輔 大賀
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP7126036A priority Critical patent/JPH08321316A/en
Publication of JPH08321316A publication Critical patent/JPH08321316A/en
Pending 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 prevent moisture contained in fuel off gas from condensing in a gas pipe, in mixture condition with fuel gas being supplied anew, aiming at a fuel cell generator of such system that the fuel off gas discharged from the fuel cell is recycled and mixed in fuel gas prior to supply. CONSTITUTION: This is a fuel cell generator which recycles the fuel off gas of a fuel cell 1 and mixes it with the fuel gas supplied through a fuel gas supply circuit 2a by an ejector pump 5 and sends it into the fuel electrode 1a of the fuel cell. A recycle circuit 2b of fuel off gas being piped on the gas outlet side of a fuel cell is provided with a moisture separator 11 which condenses and removes the steam contained in the gas by cooling the off gas by the exchange with cooling water, as a dehumidifying means which removes the moisture (produced water accompanying battery reaction) contained in off gas. And, the flow and pressure of the fuel gas to be supplied to the fuel cell are stabilized by preventing condensed water from staying within the pipe of the mixture gas circuit 2c within an ejector pump during operation.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、燃料電池から排出され
る燃料オフガスをリサイクルし、外部より新たに供給し
た燃料ガスと燃料オフガスとを混合させて燃料電池の燃
料電極に供給する燃料電池発電装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fuel cell power generation system for recycling fuel off-gas discharged from a fuel cell, mixing the fuel gas newly supplied from the outside with the fuel off-gas and supplying the mixed fuel gas to the fuel electrode of the fuel cell. Regarding the device.

【0002】[0002]

【従来の技術】最近になり、合成化学工場などで得られ
る副生水素を燃料電池の原燃料として利用するオンサイ
ト用燃料電池発電装置の開発が進めらている。また、こ
の燃料電池発電装置について、燃料電池から排出される
燃料オフガスをリサイクルし、外部より新たに供給した
燃料ガス(サイト側の副生水素)と燃料オフガスとを混
合させて燃料電池の燃料電極に供給し、原燃料消費量の
節減化,並びに燃料電池での水素利用率の改善を図るよ
うにした方式のものが知られている。
2. Description of the Related Art Recently, development of an on-site fuel cell power generator which utilizes by-product hydrogen obtained in a synthetic chemical factory as a raw fuel of a fuel cell has been advanced. Further, in this fuel cell power generation device, the fuel off gas discharged from the fuel cell is recycled, and the fuel gas (site by-product hydrogen) newly supplied from the outside is mixed with the fuel off gas to form a fuel electrode for the fuel cell. Is known to reduce the consumption of raw fuel and improve the hydrogen utilization rate in the fuel cell.

【0003】図5は前記した燃料オフガスのリサイクル
方式を採用した従来の燃料電池発電装置のプロセスフロ
ー図である。図において、1は燃料極1a,空気極1
b,冷却板1cを模式的に表した燃料電池(リン酸型燃
料電池)、2は燃料ガス供給系、3は反応空気供給系、
4は冷却水循環系である。ここで、燃料ガス供給系2は
燃料ガス供給回路2a,燃料オフガスリサイクル回路2
b,混合ガス回路2cに分かれ、燃料ガスと燃料オフガ
スとが合流する地点には燃料ガスを駆動ガスとして作動
するエジェクタポンプ5が接続されている。また、冷却
水循環系3には水蒸気分離器4aを備えており、該水蒸
気分離器4aで分離した水蒸気を暖房器などの排熱利用
設備6へ供給して排熱利用を行うようにしている。な
お、7は空気供給系3に備えた空気ブロア、8は冷却水
循環系4の冷却水循環ポンプ、9は排熱利用設備6の送
水ポンプ、10は圧力調節弁である。
FIG. 5 is a process flow diagram of a conventional fuel cell power generator which employs the above-mentioned fuel off-gas recycling system. In the figure, 1 is a fuel electrode 1a and an air electrode 1
b, a fuel cell (phosphoric acid type fuel cell) schematically showing the cooling plate 1c, 2 a fuel gas supply system, 3 a reaction air supply system,
4 is a cooling water circulation system. Here, the fuel gas supply system 2 includes a fuel gas supply circuit 2a and a fuel off gas recycle circuit 2
The ejector pump 5, which operates using the fuel gas as a driving gas, is connected to a point where the fuel gas and the fuel off-gas merge. Further, the cooling water circulation system 3 is provided with a steam separator 4a, and the steam separated by the steam separator 4a is supplied to the exhaust heat utilization equipment 6 such as a heater to utilize the exhaust heat. In addition, 7 is an air blower provided in the air supply system 3, 8 is a cooling water circulation pump of the cooling water circulation system 4, 9 is a water supply pump of the waste heat utilization facility 6, and 10 is a pressure control valve.

【0004】かかる構成で、燃料ガス(副生水素)と空
気を燃料電池1の燃料極1a,空気極1bに供給してそ
の電気化学反応により発電する。また、発電に伴う燃料
電池1の発熱は冷却板1cに冷却水を流して除熱し、電
池本体の運転温度を一定(約180℃)に維持するとと
もに、その排熱を水蒸気分離器4aより回収して排熱利
用設備6で有効活用している。
With this structure, fuel gas (by-product hydrogen) and air are supplied to the fuel electrode 1a and the air electrode 1b of the fuel cell 1 to generate electricity by the electrochemical reaction. In addition, heat generated by the fuel cell 1 due to power generation is removed by flowing cooling water through the cooling plate 1c to maintain the operating temperature of the cell body constant (about 180 ° C.) and recover the exhaust heat from the steam separator 4a. The waste heat utilization equipment 6 is effectively utilized.

【0005】また、燃料電池1の燃料極1aから排出す
る未反応の燃料オフガスは、リサイクル回路2bを通じ
てエジェクタポンプ5に吸い込まれ、外部から新たに供
給した燃料ガスと混合した後に、混合ガス回路2cを通
じて燃料電池1の燃料極1aへ供給するようにリサイク
ルする。これにより、外部から新たに供給する燃料ガス
の消費量節減と併せて、燃料電池1での水素利用率を低
めて発電効率の向上が図れる。
The unreacted fuel off-gas discharged from the fuel electrode 1a of the fuel cell 1 is sucked into the ejector pump 5 through the recycle circuit 2b, mixed with the fuel gas newly supplied from the outside, and then mixed gas circuit 2c. To be supplied to the fuel electrode 1a of the fuel cell 1 through. As a result, it is possible to reduce the consumption rate of the fuel gas newly supplied from the outside and reduce the hydrogen utilization rate in the fuel cell 1 to improve the power generation efficiency.

【0006】[0006]

【発明が解決しようとする課題】ところで、前記のよう
に燃料オフガスを新たに供給される低温の燃料ガスと混
合して燃料電池に供給するリサイクル方式を採用した燃
料電池発電装置では、次記のような問題点が生じる。す
なわち、燃料電池1では周知のように水素と酸素との電
気化学反応に伴って水が生成され、この反応生成水は水
蒸気のかたちで燃料オフガス,および排空気に随伴して
燃料電池から排出される。したがって、オフガスリサイ
クル回路2bに通流する高温の燃料オフガスには前記の
反応生成水が殆ど飽和蒸気の状態で含まれることにな
る。一方、燃料ガス供給回路2bを通じて外部から新た
に供給される燃料ガスは例えば常温に近い低温のガスで
あり、このために燃料オフガスと燃料ガスをエジェクタ
ポンプ5で混合させると燃料オフガスの温度が下がり、
このオフガスに含まれている水蒸気がエジェクタポンプ
5の内部,および混合ガス回路2cで凝縮して液体にな
る。
By the way, in the fuel cell power generator adopting the recycling system in which the fuel off gas is mixed with the newly supplied low temperature fuel gas and is supplied to the fuel cell as described above, Such problems arise. That is, in the fuel cell 1, as is well known, water is produced in association with an electrochemical reaction between hydrogen and oxygen, and this reaction-produced water is discharged from the fuel cell in the form of water vapor along with fuel off-gas and exhaust air. It Therefore, the high-temperature fuel off-gas flowing in the off-gas recycling circuit 2b contains the above-mentioned reaction-produced water in a substantially saturated vapor state. On the other hand, the fuel gas newly supplied from the outside through the fuel gas supply circuit 2b is, for example, a low temperature gas close to room temperature. Therefore, when the fuel off gas and the fuel gas are mixed by the ejector pump 5, the temperature of the fuel off gas decreases. ,
The water vapor contained in this off-gas is condensed inside the ejector pump 5 and in the mixed gas circuit 2c to become a liquid.

【0007】しかも、このような状態のまま燃料電池へ
のガス供給を行うと、凝縮水がガス配管中の随所に溜ま
って燃料ガスの通流を妨げる。このために、燃料電池へ
送り込む燃料ガスの流量,圧力が変動して安定した発電
が行えなくなるほか、ガス流量,圧力の脈動的な変化に
より燃料電池本体が機械的なストレスを受け、さらには
間欠的にガス欠状態が生じて電極触媒を劣化し、燃料電
池の寿命を縮めるといった問題に発展する。
Moreover, when the gas is supplied to the fuel cell in such a state, the condensed water accumulates everywhere in the gas pipe and hinders the flow of the fuel gas. For this reason, the flow rate and pressure of the fuel gas sent to the fuel cell fluctuates, and stable power generation cannot be performed. Further, the pulsating changes in the gas flow rate and pressure receive mechanical stress on the fuel cell main body, and even intermittent A gas shortage occurs, the electrode catalyst is deteriorated, and the life of the fuel cell is shortened.

【0008】本発明は上記の点にかんがみなされたもの
であり、その目的は前記課題を解決し、燃料オフガス中
に含まれる水分が新たに供給した燃料ガスとの混合状態
でガス管路中に凝縮するのを防止し、ガス管路中に溜ま
った凝縮水に起因する燃料電池への弊害を回避できるよ
うにした燃料電池発電装置を提供することにある。
The present invention has been conceived in view of the above points, and an object thereof is to solve the above-mentioned problems and to introduce water contained in fuel off-gas into a gas pipeline in a mixed state with fuel gas newly supplied. It is an object of the present invention to provide a fuel cell power generation device capable of preventing condensation and avoiding an adverse effect on the fuel cell due to condensed water accumulated in the gas pipeline.

【0009】[0009]

【課題を解決するための手段】上記目的は、本発明によ
り燃料電池発電装置を次記のように構成することにより
達成される。 1)第1の発明:燃料電池から排出される燃料オフガス
をリサイクルし、外部より新たに供給した燃料ガスと燃
料オフガスとを混合させて燃料電池の燃料電極に供給す
る燃料電池発電装置において、燃料電池のガス出口側と
ガス混合地点との間に配管した燃料オフガスのリサイク
ル回路に、オフガス中に含まれている水分を除去する除
湿手段を備えるものとする。
The above object can be achieved by the present invention by constructing a fuel cell power generator as follows. 1) The first invention: a fuel cell power generator that recycles fuel off-gas discharged from a fuel cell, mixes fuel gas newly supplied from the outside with fuel off-gas, and supplies the mixed fuel gas to a fuel electrode of a fuel cell. A dehumidifying means for removing water contained in the offgas is provided in the fuel offgas recycling circuit which is provided between the gas outlet side of the battery and the gas mixing point.

【0010】また、前記の除湿手段は、具体的に、冷却
水との熱交換により冷却して燃料オフガス中の水蒸気を
凝縮,除去する気水分離器として構成し、また、かかる
気水分離器は気水分離室と、該気水分離室を通過した低
温の燃料オフガスを気水分離室へ導入する前の高温の燃
料オフガスと熱交換して昇温させる加熱室との組合わせ
から構成で実施することもできる。
The dehumidifying means is specifically constituted as a steam separator for cooling by heat exchange with cooling water to condense and remove water vapor in the fuel off-gas, and such steam separator is also used. Is a combination of a steam separation chamber and a heating chamber that heats the low-temperature fuel off-gas passing through the steam-separation chamber with the high-temperature fuel off-gas before being introduced into the steam-water separation chamber to raise the temperature. It can also be implemented.

【0011】2)第2の発明:燃料電池から排出される
燃料オフガスをリサイクルし、外部より新たに供給した
燃料ガスと燃料オフガスとを混合させて燃料電池の燃料
電極に供給する燃料電池発電装置において、ガス混合地
点より上流側の燃料オフガスリサイクル回路,燃料ガス
供給回路,および下流側の混合ガス回路のうち、少なく
とも一つの回路に燃料オフガス中に含まれている水分が
混合ガス中で凝縮するのを防止するガス加熱手段を備え
るものとする。
2) Second invention: A fuel cell power generator which recycles the fuel off-gas discharged from the fuel cell, mixes the fuel gas newly supplied from the outside with the fuel off-gas, and supplies the mixed fuel gas to the fuel electrode of the fuel cell. At, in at least one of the fuel off-gas recycling circuit, the fuel gas supply circuit, and the downstream mixed gas circuit upstream of the gas mixing point, the water contained in the fuel off-gas condenses in the mixed gas. A gas heating means for preventing the above is provided.

【0012】また、前記のガス加熱手段は、燃料電池本
体の水冷却系より抽出した冷却水,ないしは水冷却系内
の水蒸気分離器より抽出した水蒸気を熱媒としてガス管
路に設けた熱交換器、あるいは、燃料電池より排出した
高温の燃料オフガスを熱媒としてガス管路に設けた熱交
換器で実施することができる。さらに、燃料オフガスの
リサイクル回路を含む燃料ガス供給系に対し、前記した
第1の発明による除湿手段と第2の発明によるガス加熱
手段とを併設して実施することもできる。
Further, the above-mentioned gas heating means is a heat exchange provided in the gas pipeline using the cooling water extracted from the water cooling system of the fuel cell main body or the steam extracted from the steam separator in the water cooling system as a heat medium. Or a high-temperature fuel off-gas discharged from the fuel cell can be used as a heat medium in a heat exchanger provided in the gas pipeline. Further, the dehumidifying means according to the first aspect of the invention and the gas heating means according to the second aspect of the invention may be provided together with the fuel gas supply system including the fuel off-gas recycling circuit.

【0013】[0013]

【作用】前記した第1の発明によれば、燃料電池から排
出した燃料オフガスはリサイクル回路を通流する過程で
除湿手段である気水分離器で除湿され、オフガスから凝
縮分離した液分はドレンとして気水分離器より系外に排
水される。したがって、オフガスは絶対湿度が低下して
殆ど水分を含まない状態で新たに外部から供給した燃料
ガスと混合されることになるので、ガス合流地点に設け
たエジェクタポンプの内部,およびこれに続く混合ガス
回路のガス管路中に凝縮水の生成が防げる。この場合
に、気水分離器の気水分離室で除湿した後のガスを、次
の加熱室で高温のオフガスとの熱交換により加熱するこ
とでオフガスの相対湿度が低下するので、低温の燃料ガ
スと混合した状態でもガス中に残る水分がより一層凝縮
し難くなる。
According to the first invention described above, the fuel off-gas discharged from the fuel cell is dehumidified by the steam separator which is a dehumidifying means in the process of flowing through the recycle circuit, and the liquid component condensed and separated from the off-gas is drained. As a result, it is discharged from the steam separator to the outside of the system. Therefore, since the off-gas is mixed with the fuel gas newly supplied from the outside in a state where the absolute humidity is lowered and contains almost no water, the inside of the ejector pump provided at the gas confluence point and the subsequent mixing. The formation of condensed water in the gas line of the gas circuit can be prevented. In this case, the gas after dehumidification in the steam separation chamber of the steam separator is heated by heat exchange with high-temperature off-gas in the next heating chamber, whereby the relative humidity of the off-gas decreases, so the low-temperature fuel Even in a state of being mixed with the gas, the water remaining in the gas becomes more difficult to condense.

【0014】また、第2の発明によれば、燃料ガス供給
系を流れる燃料オフガス,燃料ガス、ないしは燃料オフ
ガスと燃料ガスとの混合ガスをガス加熱手段で加熱,昇
温させるようにしたことにより、水分を含む燃料オフガ
スと新たに供給する燃料ガスとを混合した状態でも、混
合ガスが高温に保たれてその湿り度が飽和液線を超える
ことがない。これにより、燃料オフガスに含まれている
水分が混合ガス回路内で凝縮して凝縮水を生成するのを
防止できる。この場合に、ガス加熱手段の熱媒として燃
料電池の冷却水,余剰蒸気,ないしは高温のオフガスを
利用することで、ガス加熱に必要な熱を燃料電池発電装
置の系内で賄うことができる。
According to the second invention, the fuel off gas, the fuel gas flowing through the fuel gas supply system, or the mixed gas of the fuel off gas and the fuel gas is heated and heated by the gas heating means. Even in the state where the fuel off gas containing water and the fuel gas to be newly supplied are mixed, the mixed gas is kept at a high temperature and the wetness thereof does not exceed the saturated liquid line. As a result, it is possible to prevent the water contained in the fuel off gas from condensing in the mixed gas circuit to generate condensed water. In this case, by using cooling water of the fuel cell, excess steam, or high-temperature off-gas as the heat medium of the gas heating means, the heat required for heating the gas can be provided in the system of the fuel cell power generator.

【0015】加えて、前記したオフガスの除湿手段とガ
ス加熱手段を併用することで、凝縮水生成防止の効果が
より一層高まる。
In addition, the combined use of the off-gas dehumidifying means and the gas heating means further enhances the effect of preventing the generation of condensed water.

【0016】[0016]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。なお、各実施例の図中で図5に対応する同一部材
には同じ符号を付してその説明を省略する。 実施例1:図1は本発明の請求項1,2に対応する第1
の発明の実施例を示すものであり、図5の構成と比較し
て、燃料オフガス回路2bには除湿手段として気水分離
器11が新たに追加装備されている。この気水分離器1
1は冷却コイル11aを内蔵し、該冷却コイル11aに
外部から流す冷却水との熱交換により燃料電池1より排
出した燃料オフガスを冷却し、そのガス中に含まれてい
る水分を凝縮,分離した上でドレンとして系外に排水さ
せるように機能する。
Embodiments of the present invention will be described below with reference to the drawings. In the drawings of the respective embodiments, the same members corresponding to those in FIG. 5 are designated by the same reference numerals and the description thereof will be omitted. Embodiment 1 FIG. 1 shows a first embodiment corresponding to claims 1 and 2 of the present invention.
5 shows an embodiment of the invention of FIG. 5, and in comparison with the configuration of FIG. 5, a fuel-off gas circuit 2b is additionally equipped with a steam separator 11 as a dehumidifying means. This steam separator 1
Reference numeral 1 includes a cooling coil 11a, which cools fuel-off gas discharged from the fuel cell 1 by heat exchange with cooling water flowing from the outside to the cooling coil 11a, and condenses and separates water contained in the gas. It functions as a drain to drain the water outside the system.

【0017】かかる構成より、燃料オフガスに含まれて
いる水分(燃料電池1の電池反応に伴って生成した水の
水蒸気)の大半が除去されてオフガス自身の絶対湿度が
低下する。これより、外部より燃料ガス供給回路2aに
供給した低温の燃料ガスと燃料オフガスとをエジェクタ
ポンプ5を介して混合させた状態でも、エジェクタポン
プ5の内部、およびエジェクタポンプ5に続く混合ガス
回路2cで凝縮水が殆ど生成しない状態で燃料電池1の
運転が行える。この結果、ガス配管中に凝縮水が溜まる
ことがもなく、かつその凝縮水の生成に起因して燃料電
池1に供給する燃料ガスの流量,圧力が不安定となるな
どの弊害が回避できる。
With this structure, most of the water contained in the fuel off-gas (water vapor generated by the cell reaction of the fuel cell 1) is removed, and the absolute humidity of the off-gas itself decreases. As a result, even when the low-temperature fuel gas supplied from the outside to the fuel gas supply circuit 2a and the fuel off gas are mixed via the ejector pump 5, the inside of the ejector pump 5 and the mixed gas circuit 2c following the ejector pump 5 Thus, the fuel cell 1 can be operated in a state in which condensed water is hardly generated. As a result, condensed water does not accumulate in the gas pipe, and it is possible to avoid adverse effects such as unstable flow rate and pressure of the fuel gas supplied to the fuel cell 1 due to the generation of the condensed water.

【0018】実施例2:図2は本発明の請求項3に対応
する前記実施例1の応用実施例を示すものである。この
実施例においては、気水分離器11が、冷却コイル11
aを内蔵した気水分離室11bと、燃料電池1から出た
高温のオフガスを流す加熱コイル11cを内蔵した加熱
室11dとの組合わせから構成され、気水分離室11b
を通過して気水分離された低温の燃料オフガスが、次の
加熱室11dを通流する過程で気水分離室へ導入する前
の高温の燃料オフガスと熱交換して昇温させるように構
成されている。
Second Embodiment: FIG. 2 shows an application example of the first embodiment corresponding to claim 3 of the present invention. In this embodiment, the steam separator 11 is the cooling coil 11
The gas-water separation chamber 11b is a combination of a gas-water separation chamber 11b containing a and a heating chamber 11d containing a heating coil 11c for flowing the high-temperature off-gas discharged from the fuel cell 1.
The low-temperature fuel off-gas, which has been separated into steam and water by passing through the chamber, heat-exchanges with the high-temperature fuel-off gas before being introduced into the steam-separation chamber in the process of flowing through the next heating chamber 11d to raise the temperature. Has been done.

【0019】かかる構成により、燃料電池1から排出し
た燃料オフガスは、気水分離器11の気水分離室11b
にて冷却,除湿された後、次の加熱室11dで再び高温
のオフガスと熱交換して昇温される。したがって気水分
離器11を出たオフガスは相対湿度がさらに低下するこ
とになり、これにより燃料ガスと混合した際に生成する
凝縮水の防止効果がより一層高まる。
With this structure, the fuel off gas discharged from the fuel cell 1 is separated into the steam separation chamber 11b of the steam separator 11.
After being cooled and dehumidified in, the temperature is raised again by exchanging heat with high-temperature off-gas in the next heating chamber 11d. Therefore, the relative humidity of the off-gas that has left the steam separator 11 is further lowered, which further enhances the effect of preventing the condensed water generated when the off-gas is mixed with the fuel gas.

【0020】実施例3:図3は本発明の請求項4,5に
対応する第2の発明の一実施例を示すものであり、図5
の構成と較べて、燃料ガス供給系2の混合ガス回路2c
に熱交換器として機能するガス加熱器12が新たに追加
装備されている。このガス加熱器12はスチームトレー
スとして混合ガス回路2cの管路に巻きつけて配管した
加熱コイル12aへ燃料電池1の冷却水循環系4に備え
た水蒸気分離器4aより抽出した蒸気を熱媒として流す
ようにしている。
Embodiment 3 FIG. 3 shows an embodiment of the second invention corresponding to claims 4 and 5 of the present invention.
Compared with the configuration described above, the mixed gas circuit 2c of the fuel gas supply system 2
In addition, a gas heater 12 that functions as a heat exchanger is newly added. In this gas heater 12, the steam extracted from the steam separator 4a provided in the cooling water circulation system 4 of the fuel cell 1 flows as a heat medium to the heating coil 12a wound around the pipe of the mixed gas circuit 2c as a steam trace. I am trying.

【0021】かかる構成で、燃料電池1が運転している
状態では、水蒸気分離器4aには温度165℃,圧力6
Kg/cm2 程度で水と水蒸気とが貯留されており、ここか
ら抽出してガス加熱器12の加熱コイル12aに供給さ
れる水蒸気との熱交換により、混合ガス回路2cを通流
する燃料混合ガスが加熱,昇温される。これにより混合
ガスの相対湿度が低下し、水分を含む燃料オフガスと燃
料ガス供給回路2aを通じて供給される燃料ガスとをエ
ジェクタポンプ5で混合した後でも、混合ガス中に含ま
れている水分の凝縮が起き難くなるので、先記実施例1
と同等な効果が得られる。
With such a configuration, when the fuel cell 1 is in operation, the steam separator 4a has a temperature of 165 ° C. and a pressure of 6
Water and water vapor are stored at about Kg / cm 2 , and the fuel mixture flowing through the gas mixture circuit 2c is exchanged by heat exchange with water vapor extracted from this and supplied to the heating coil 12a of the gas heater 12. The gas is heated and heated. As a result, the relative humidity of the mixed gas is lowered, and even after the fuel off gas containing water and the fuel gas supplied through the fuel gas supply circuit 2a are mixed by the ejector pump 5, the water contained in the mixed gas is condensed. Is less likely to occur, the above-mentioned Example 1
An effect equivalent to is obtained.

【0022】なお、図3ではガス加熱器12を混合ガス
回路2cに設置した例を示したが、ほかに燃料ガス供給
回路2a,あるいは燃料オフガスのリサイクル回路2b
に設けも同等な効果が得られる。また、ガス加熱器12
の加熱コイル12aに流す熱媒としては、水蒸気分離器
4aより抽出した水蒸気に代えて燃料電池1の冷却水循
環系4から抽出した高温側の冷却水(水温約170
℃),あるいは水蒸気分離器4aより抽出したブローダ
ウン水を利用することも可能である。さらに、当該斐ガ
ス加熱器12とともに、リサイクル回路2bには実施例
1で述べた気水分離器11を併用して実施することもで
きる。
Although FIG. 3 shows an example in which the gas heater 12 is installed in the mixed gas circuit 2c, a fuel gas supply circuit 2a or a fuel off gas recycling circuit 2b may also be used.
The same effect can be obtained by providing the above. Also, the gas heater 12
As the heat medium flowing through the heating coil 12a, the high temperature side cooling water extracted from the cooling water circulation system 4 of the fuel cell 1 in place of the steam extracted from the steam separator 4a (water temperature of about 170
Alternatively, it is possible to use blowdown water extracted from the steam separator 4a. Further, the steam-water separator 11 described in the first embodiment can be used together with the Hi-gas heater 12 in the recycle circuit 2b.

【0023】実施例4:図4は本発明の請求項6に対応
する第2の発明の応用実施例を示すものであり、この実
施例においては、混合ガス回路2cの配管路に設けたガ
ス加熱器12に燃料電池1より排出した高温の燃料オフ
ガスを通流させ、このオフガスとの熱交換で混合ガスを
加熱,昇温して水分の凝縮を防止するようにしたもので
ある。
Embodiment 4 FIG. 4 shows an application embodiment of the second invention corresponding to claim 6 of the present invention. In this embodiment, the gas provided in the pipeline of the mixed gas circuit 2c is shown. The high-temperature fuel off-gas discharged from the fuel cell 1 is caused to flow through the heater 12, and the mixed gas is heated and heated by heat exchange with the off-gas to prevent condensation of water.

【0024】なお、図示の各実施例は、化学工場などの
サイト側から得た副生水素を原燃料として燃料電池に直
接供給するようにした燃料電池発電装置を示したが、天
然ガスなどを原燃料として、この原燃料を燃料改質系で
水素リッチなガスに改質して燃料電池に供給するように
した燃料電池発電装置にも適用できることは勿論であ
る。そして、この場合には燃料電池から排出する燃料オ
フガスの一部を燃料改質器のバーナに供給して消費し、
残りをリサイクルして改質ガスに合流させて燃料電池に
供給する。
Although each of the illustrated embodiments shows a fuel cell power generator in which by-product hydrogen obtained from a site such as a chemical factory is directly supplied as a raw fuel to a fuel cell, natural gas or the like is used. As a raw fuel, it is needless to say that the raw fuel can be applied to a fuel cell power generation device which is reformed into a hydrogen-rich gas in a fuel reforming system and supplied to a fuel cell. Then, in this case, a part of the fuel off-gas discharged from the fuel cell is supplied to the burner of the fuel reformer and consumed,
The rest is recycled and merged with the reformed gas to be supplied to the fuel cell.

【0025】[0025]

【発明の効果】以上述べたように、本発明によれば、燃
料電池から排出した燃料オフガスをリサイクルさせて外
部から新たに供給する燃料ガスと混合させる際に、燃料
オフガス回路に設けた除湿手段,あるいは燃料ガス供給
系のガス回路に設けたガス加熱手段の働きにより、燃料
オフガス中に含まれている水分(電池反応で生じた生成
水)がガス合流地点に設けたエジェクタポンプの内部,
ないしこれに続く混合ガス回路の配管路内で凝縮するの
を防止でき、これにより凝縮水が燃料供給系のガス配管
内に溜まって燃料ガスの流れを妨げることなしに、燃料
電池へ供給する燃料ガスの流量,圧力を安定に保った状
態で発電運転を行うことができる。
As described above, according to the present invention, when the fuel off gas discharged from the fuel cell is recycled and mixed with the fuel gas newly supplied from the outside, the dehumidifying means provided in the fuel off gas circuit. , Or by the action of the gas heating means provided in the gas circuit of the fuel gas supply system, the water contained in the fuel off-gas (water generated by the cell reaction) is provided inside the ejector pump at the gas confluence point,
It is possible to prevent condensation in the pipeline of the mixed gas circuit that follows or to prevent the condensed water from accumulating in the gas pipeline of the fuel supply system and obstructing the flow of the fuel gas, and supplying the fuel to the fuel cell. Power generation operation can be performed with the gas flow rate and pressure kept stable.

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

【図1】本発明の実施例1に対応する燃料電池発電装置
のシステムフロー図
FIG. 1 is a system flow diagram of a fuel cell power generation device corresponding to a first embodiment of the present invention.

【図2】本発明の実施例2に対応する気水分離器,およ
びその周辺回路図
FIG. 2 is a steam-water separator corresponding to Embodiment 2 of the present invention, and a peripheral circuit diagram thereof.

【図3】本発明の実施例3に対応する燃料電池発電装置
のシステムフロー図
FIG. 3 is a system flow diagram of a fuel cell power generator corresponding to Example 3 of the present invention.

【図4】本発明の実施例4に対応する燃料電池発電装置
のシステムフロー図
FIG. 4 is a system flow diagram of a fuel cell power generator corresponding to Example 4 of the present invention.

【図5】従来における燃料電池発電装置のシステムフロ
ー図
FIG. 5 is a system flow diagram of a conventional fuel cell power generator.

【符号の説明】 1 燃料電池 1a 燃料極 1b 空気極 1c 冷却板 2 燃料ガス供給系 2a 燃料ガス供給回路 2b 燃料オフガスリサイクル回路 2c 混合ガス回路 3 反応空気供給系 4 冷却水循環系 4a 水蒸気分離器 5 エジェクタポンプ 11 気水分離器(除湿手段) 11b 気水分離室 11d 加熱室 12 ガス加熱器(ガス加熱手段)[Explanation of reference numerals] 1 fuel cell 1a fuel electrode 1b air electrode 1c cooling plate 2 fuel gas supply system 2a fuel gas supply circuit 2b fuel off-gas recycling circuit 2c mixed gas circuit 3 reaction air supply system 4 cooling water circulation system 4a steam separator 5 Ejector pump 11 Air-water separator (dehumidifying means) 11b Air-water separating chamber 11d Heating chamber 12 Gas heater (gas heating means)

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】燃料電池から排出される燃料オフガスをリ
サイクルし、外部より新たに供給した燃料ガスと燃料オ
フガスとを混合させて燃料電池の燃料電極に供給する燃
料電池発電装置において、燃料電池のガス出口とガス混
合地点との間に配管した燃料オフガスのリサイクル回路
に、オフガス中に含まれている水分を除去する除湿手段
を備えたことを特徴とする燃料電池発電装置。
1. A fuel cell power generator that recycles fuel off-gas discharged from a fuel cell, mixes the fuel gas newly supplied from the outside with the fuel off-gas and supplies the mixed fuel gas to a fuel electrode of the fuel cell. A fuel cell power generator comprising a dehumidifying means for removing water contained in the offgas in a fuel offgas recycling circuit provided between the gas outlet and the gas mixing point.
【請求項2】請求項1記載の燃料電池発電装置におい
て、除湿手段が冷却水との熱交換により冷却して燃料オ
フガス中の水蒸気を凝縮,除去する気水分離器であるこ
とを特徴とする燃料電池発電装置。
2. The fuel cell power generator according to claim 1, wherein the dehumidifying means is a steam separator that cools by heat exchange with cooling water to condense and remove water vapor in the fuel off gas. Fuel cell power generator.
【請求項3】請求項2記載の燃料電池発電装置におい
て、気水分離器が気水分離室と、該気水分離室を通過し
た低温の燃料オフガスを気水分離室へ導入する前の高温
な燃料オフガスと熱交換して昇温させる加熱室との組合
わせからなることを特徴とする燃料電池発電装置。
3. The fuel cell power generator according to claim 2, wherein the steam-water separator has a steam-water separation chamber and a high temperature before the low-temperature fuel off-gas passing through the steam-water separation chamber is introduced into the steam-water separation chamber. A fuel cell power generator comprising a combination of a heating chamber for exchanging heat with various fuel off-gas to raise the temperature.
【請求項4】燃料電池から排出される燃料オフガスをリ
サイクルし、外部より新たに供給した燃料ガスと燃料オ
フガスとを混合させて燃料電池の燃料電極に供給する燃
料電池発電装置において、ガス合流地点より上流側の燃
料オフガスリサイクル回路,燃料ガス供給回路,または
下流側の混合ガス回路のうちの少なくとも一つの回路に
燃料オフガス中に含まれている水分が混合ガス中で凝縮
するのを防止するガス加熱手段を備えたことを特徴とす
る燃料電池発電装置。
4. A fuel cell power generator that recycles fuel off-gas discharged from a fuel cell, mixes fuel off-gas newly supplied from the outside with fuel off-gas, and supplies the mixed fuel gas to a fuel electrode of a fuel cell. Gas that prevents water contained in the fuel off gas from condensing in the mixed gas in at least one of the fuel off gas recycling circuit on the upstream side, the fuel gas supply circuit, or the mixed gas circuit on the downstream side. A fuel cell power generator comprising a heating means.
【請求項5】請求項4記載の燃料電池発電装置におい
て、ガス加熱手段が、燃料電池本体の水冷却系より抽出
した冷却水,ないしは水冷却系内の水蒸気分離器より抽
出した水蒸気を熱媒とする熱交換器であることを特徴と
する燃料電池発電装置。
5. The fuel cell power generator according to claim 4, wherein the gas heating means heats the cooling water extracted from the water cooling system of the fuel cell main body or the steam extracted from the steam separator in the water cooling system. A fuel cell power generation device, comprising:
【請求項6】請求項4記載の燃料電池発電装置におい
て、ガス加熱手段が、燃料電池より排出した高温の燃料
オフガスを熱媒とする熱交換器であることを特徴とする
燃料電池発電装置。
6. The fuel cell power generator according to claim 4, wherein the gas heating means is a heat exchanger using a high temperature fuel off-gas discharged from the fuel cell as a heat medium.
【請求項7】燃料オフガスのリサイクル回路を含む燃料
ガス供給系に請求項1記載の除湿手段と請求項4記載の
ガス加熱手段とを併設したことを特徴とする燃料電池発
電装置。
7. A fuel cell power generator comprising a dehumidifying means according to claim 1 and a gas heating means according to claim 4, which are provided together with a fuel gas supply system including a fuel off-gas recycling circuit.
JP7126036A 1995-05-25 1995-05-25 Fuel cell generator Pending JPH08321316A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7126036A JPH08321316A (en) 1995-05-25 1995-05-25 Fuel cell generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7126036A JPH08321316A (en) 1995-05-25 1995-05-25 Fuel cell generator

Publications (1)

Publication Number Publication Date
JPH08321316A true JPH08321316A (en) 1996-12-03

Family

ID=14925093

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7126036A Pending JPH08321316A (en) 1995-05-25 1995-05-25 Fuel cell generator

Country Status (1)

Country Link
JP (1) JPH08321316A (en)

Cited By (14)

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Publication number Priority date Publication date Assignee Title
JP2002184439A (en) * 2000-10-05 2002-06-28 Honda Motor Co Ltd Fuel cell system
JP2003109628A (en) * 2001-09-27 2003-04-11 Toto Ltd Fuel cell system
JP2003178779A (en) * 2001-12-12 2003-06-27 Nissan Motor Co Ltd Fuel circulation equipment of fuel cell system
JP2005019221A (en) * 2003-06-26 2005-01-20 Honda Motor Co Ltd Fuel cell system
JP2006134620A (en) * 2004-11-04 2006-05-25 Honda Motor Co Ltd Fuel cell system
WO2005065124A3 (en) * 2003-12-23 2006-09-14 Utc Fuel Cells Llc Fuel cell stack including hydrogen pumping fuel cells
JP2007048493A (en) * 2005-08-08 2007-02-22 Hitachi Ltd Fuel cell power generating system
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JP2011155011A (en) * 2011-03-22 2011-08-11 Honda Motor Co Ltd Fuel cell system
JP2012028233A (en) * 2010-07-27 2012-02-09 Nissan Motor Co Ltd Fuel cell system
KR101142474B1 (en) * 2009-09-18 2012-05-08 한국전력공사 Polymer Electrolyte Fuel Cell System
US8241806B2 (en) 2004-11-08 2012-08-14 Honda Motor Co., Ltd. Fuel cell system
US8263270B2 (en) 2005-04-26 2012-09-11 Honda Motor Co., Ltd. Fuel cell vehicle and water discharging method for fuel cell vehicle
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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002184439A (en) * 2000-10-05 2002-06-28 Honda Motor Co Ltd Fuel cell system
JP2003109628A (en) * 2001-09-27 2003-04-11 Toto Ltd Fuel cell system
JP2003178779A (en) * 2001-12-12 2003-06-27 Nissan Motor Co Ltd Fuel circulation equipment of fuel cell system
JP2005019221A (en) * 2003-06-26 2005-01-20 Honda Motor Co Ltd Fuel cell system
JP2007516585A (en) * 2003-12-23 2007-06-21 ユーティーシー フューエル セルズ,エルエルシー Hydrogen pump fuel cell
WO2005065124A3 (en) * 2003-12-23 2006-09-14 Utc Fuel Cells Llc Fuel cell stack including hydrogen pumping fuel cells
US7449260B2 (en) * 2003-12-23 2008-11-11 Utc Power Corporation Fuel cell stack including hydrogen pumping fuel cells
JP2006134620A (en) * 2004-11-04 2006-05-25 Honda Motor Co Ltd Fuel cell system
US8241806B2 (en) 2004-11-08 2012-08-14 Honda Motor Co., Ltd. Fuel cell system
US8263270B2 (en) 2005-04-26 2012-09-11 Honda Motor Co., Ltd. Fuel cell vehicle and water discharging method for fuel cell vehicle
JP2007048493A (en) * 2005-08-08 2007-02-22 Hitachi Ltd Fuel cell power generating system
KR101142474B1 (en) * 2009-09-18 2012-05-08 한국전력공사 Polymer Electrolyte Fuel Cell System
CN102044686A (en) * 2009-10-16 2011-05-04 丰田纺织株式会社 Fuel cell system
US8835071B2 (en) 2009-10-16 2014-09-16 Toyota Boshoku Kabushiki Kaisha Fuel cell system including oxidation gas supply pipe integrated with coolant supply pipe
JP2012028233A (en) * 2010-07-27 2012-02-09 Nissan Motor Co Ltd Fuel cell system
JP2011155011A (en) * 2011-03-22 2011-08-11 Honda Motor Co Ltd Fuel cell system
KR101406616B1 (en) * 2012-12-21 2014-06-11 주식회사 포스코 Circulation countrol type fuel cell module

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