JP2000223143A - Fuel-cell power generation system - Google Patents

Fuel-cell power generation system

Info

Publication number
JP2000223143A
JP2000223143A JP11025940A JP2594099A JP2000223143A JP 2000223143 A JP2000223143 A JP 2000223143A JP 11025940 A JP11025940 A JP 11025940A JP 2594099 A JP2594099 A JP 2594099A JP 2000223143 A JP2000223143 A JP 2000223143A
Authority
JP
Japan
Prior art keywords
gas
fuel
fuel cell
activation
generated
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
JP11025940A
Other languages
Japanese (ja)
Inventor
Yasumoto Kubota
康幹 久保田
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.)
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 JP11025940A priority Critical patent/JP2000223143A/en
Publication of JP2000223143A publication Critical patent/JP2000223143A/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
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Landscapes

  • Fuel Cell (AREA)

Abstract

PROBLEM TO BE SOLVED: To effectively use hydrogen energy that was wasted as unnecessary gas, and eliminate requirement of facility and power for reforming raw fuel, by supplying gas generated in an activation reaction in a manufacturing process for activated carbon and using it for power generation. SOLUTION: Activation generated gas generated in an activation furnace 11 is guided through an impurity removing device 13 and a steam concentration adjuster 14 to a CO transformer 5 for CO transformation together with adequate steam. When CO concentration in fuel gas supplied to a fuel cell 1 is high, a cell characteristic of the fuel cell 1 is reduced. Therefore, CO in the activation generated gas and the steam are reacted in the CO transformer 5, to be transformed to carbon dioxide and water, and the CO concentration is reduced to lower than about 1%, for example. Such process is applied to the activation generated gas to produce fuel gas, the fuel gas is made to flow to a fuel electrode of the fuel cell 1, air guided through a blower is made to flow to an oxidant electrode, and power generation is performed. Generated power is direct power, therefore, is converted to alternating current by an inverter 15, and supplied to a load.

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】この発明は活性炭の製造工程
において発生する水素リッチなガスを燃料ガスとして使
用する燃料電池発電システムに関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fuel cell power generation system using, as a fuel gas, a hydrogen-rich gas generated in a process for producing activated carbon.

【0002】[0002]

【従来の技術】燃料電池は燃料の持つ化学エネルギーを
直接電気エネルギーに変換するものであり、電解質層を
挟持する一対の燃料電極及び酸化剤電極に、外部のガス
供給系から燃料ガスと酸化剤ガスとをそれぞれ供給し、
各電極の電極触媒層上で燃料ガスおよび酸化剤ガスを電
気化学的に反応させ、その結果として系外に電気エネル
ギーを取り出す発電装置の一種である。
2. Description of the Related Art A fuel cell directly converts the chemical energy of fuel into electric energy. A fuel cell and an oxidant electrode sandwiching an electrolyte layer are supplied with fuel gas and oxidant from an external gas supply system. And gas, respectively,
This is a type of power generation device in which a fuel gas and an oxidizing gas are electrochemically reacted on an electrode catalyst layer of each electrode, and as a result, electric energy is taken out of the system.

【0003】燃料ガスには、原燃料である炭化水素系の
気体燃料(天然ガス等)あるいは液体燃料(メタノー
ル、ナフサ等)を燃料処理システムにおいて水素リッチ
な燃料ガスに改質したものが用いられている。
[0003] As a fuel gas, a hydrocarbon gas fuel (natural gas, etc.) or a liquid fuel (methanol, naphtha, etc.), which is a raw fuel, is reformed into a hydrogen-rich fuel gas in a fuel processing system. ing.

【0004】図2に気体燃料を用いる一般的な燃料電池
発電システムの燃料処理システム10の概略図を示す。
燃料処理システム10では、原燃料ガスは、まず脱硫器
2で硫黄分を除去され、次に水蒸気と共に改質器3に送
られる。改質器3にはバーナ4が設けられており、改質
触媒が充填された図示しない改質管は約750℃に昇温
されている。原燃料はこの改質管内を通流する間に水蒸
気と反応して水素リッチなガスに改質される。その後、
CO変成器5へ導かれ、改質ガス中の一酸化炭素濃度を
低減される。
FIG. 2 is a schematic view of a fuel processing system 10 of a general fuel cell power generation system using gaseous fuel.
In the fuel processing system 10, the raw fuel gas is first subjected to sulfur removal by the desulfurizer 2, and then sent to the reformer 3 together with steam. The reformer 3 is provided with a burner 4, and the temperature of a reforming tube (not shown) filled with a reforming catalyst is raised to about 750 ° C. The raw fuel reacts with water vapor while flowing through the reforming pipe to be reformed into a hydrogen-rich gas. afterwards,
The gas is led to the CO converter 5 to reduce the concentration of carbon monoxide in the reformed gas.

【0005】ところで、吸着剤や触媒担体として用いら
れる活性炭は、木炭や木材乾留物等の原料を約600℃
の不活性雰囲気中で十分に炭化した後、炭化物の比表面
積を増加し吸着能を高めるために水蒸気や二酸化炭素中
で賦活して製造される。図3に、このような一般的な活
性炭の製造システムを示す。
[0005] Activated carbon used as an adsorbent or a catalyst carrier is obtained by using a raw material such as charcoal or wood distillate at about 600 ° C.
After sufficient carbonization in an inert atmosphere, activated in steam or carbon dioxide in order to increase the specific surface area of the carbide and increase the adsorption capacity. FIG. 3 shows such a general activated carbon production system.

【0006】炭化物の水蒸気賦活反応は下記(1)式で表
され、水素と一酸化炭素が生成される。 C+H2O→CO+H2 ・・・ (1) そして、生成した一酸化炭素がさらに下記(2)式に示す
様に水蒸気と反応すると、二酸化炭素と水素に富んだガ
スとなる。
[0006] The steam activation reaction of carbide is represented by the following equation (1), and hydrogen and carbon monoxide are produced. C + H 2 O → CO + H 2 (1) Then, when the generated carbon monoxide further reacts with water vapor as shown in the following formula (2), a gas rich in carbon dioxide and hydrogen is obtained.

【0007】 CO+H2O→CO2+H2 ・・・ (2) 上記の(1)または(2)式の賦活反応により賦活炉11で発生
したガスは、従来、図3に示すように不要なガスとして
排気により大気に放出されていた。
CO + H 2 O → CO 2 + H 2 (2) The gas generated in the activation furnace 11 by the activation reaction of the above formula (1) or (2) is conventionally unnecessary as shown in FIG. It was released to the atmosphere by exhaust as gas.

【0008】[0008]

【発明が解決しようとする課題】上述のように、従来の
燃料電池発電システムにおいては、原燃料ガスを改質し
て燃料電池発電に用いられる水素リッチな燃料ガスを得
るための複雑かつ容量の大きい装置を要し、また、バー
ナー4の燃焼用空気を供給するブロア6(図2)の動力
用電力も必要であるのに対し、一方、活性炭の製造工程
においては、燃料電池の燃料ガスとして有効に利用でき
る水素に富んだ排ガスが不要なガスとして無駄に捨てら
れていた。
As described above, the conventional fuel cell power generation system has a complicated and large capacity for reforming a raw fuel gas to obtain a hydrogen-rich fuel gas used for fuel cell power generation. A large apparatus is required, and power for driving a blower 6 (FIG. 2) for supplying combustion air for the burner 4 is also required. On the other hand, in the process of producing activated carbon, fuel gas for a fuel cell is used. Exhaust gas rich in hydrogen that can be effectively used was wasted as unnecessary gas.

【0009】本発明においては、上述の水素エネルギー
を有効活用するとともに原燃料を改質するための設備又
はそのための動力に消費される電力を不要または削減す
ることが可能な燃料電池発電システムを提供することを
目的とする。
According to the present invention, there is provided a fuel cell power generation system capable of making effective use of the above-mentioned hydrogen energy and eliminating or reducing the power consumed for the equipment for reforming the raw fuel or the power for the equipment. The purpose is to do.

【0010】[0010]

【課題を解決するための手段】本発明は、活性炭製造工
程において不要なガスとして廃棄されていた賦活反応に
より生成する水素に富んだガスを燃料電池の燃料ガスと
して発電に有効に活用することとした。
SUMMARY OF THE INVENTION The present invention is to effectively utilize a hydrogen-rich gas produced by an activation reaction, which has been discarded as an unnecessary gas in an activated carbon production process, as a fuel gas for a fuel cell for power generation. did.

【0011】[0011]

【発明の実施の形態】本願発明の燃料電池発電システム
の実施例を図1に示す。図1に示すように、本発明の燃
料電池発電システムは、活性炭の製造工程において賦活
炉11で賦活反応により生成された水素リッチな賦活生
成ガスを燃料電池1の燃料ガスとして有効利用するもの
である。
FIG. 1 shows an embodiment of a fuel cell power generation system according to the present invention. As shown in FIG. 1, the fuel cell power generation system of the present invention effectively utilizes a hydrogen-rich activation product gas generated by an activation reaction in an activation furnace 11 in a production process of activated carbon as a fuel gas of a fuel cell 1. is there.

【0012】賦活炉11で発生した賦活生成ガスは、賦
活生成ガス供給路12を通流して不純物除去装置13及
び水蒸気濃度調節器14を経て、CO変成反応に適量の
水蒸気と共にCO変成器5へ導かれる。燃料電池1に供
給される燃料ガス中に含まれる一酸化炭素の濃度が高い
と燃料電池の電池特性を低下させるため、CO変成器5
にて、賦活生成ガス中の一酸化炭素と水蒸気を反応(上
記(2)式)させることにより二酸化炭素と水素に変成し
て一酸化炭素濃度を1%程度以下に減少させる。
The activation product gas generated in the activation furnace 11 flows through the activation product gas supply path 12, passes through the impurity removing device 13 and the steam concentration controller 14, and is sent to the CO converter 5 together with an appropriate amount of water vapor for the CO conversion reaction. Be guided. If the concentration of carbon monoxide contained in the fuel gas supplied to the fuel cell 1 is high, the cell characteristics of the fuel cell are degraded.
Then, carbon monoxide and water vapor in the activation product gas are reacted with each other (formula (2)) to convert them into carbon dioxide and hydrogen, thereby reducing the carbon monoxide concentration to about 1% or less.

【0013】賦活生成ガスに上述の処理を行った後、こ
れを燃料ガスとして燃料電池1の燃料電極に、一方図示
しないブロアにより導入した空気を酸化剤電極に通流し
て発電を行う。発電により得られる電力は直流電力であ
るから、インバータ15により交流に変換して負荷に供
給される。
After the above-described treatment is performed on the activated product gas, the generated gas is used as a fuel gas to flow to the fuel electrode of the fuel cell 1 and air introduced by a blower (not shown) to the oxidant electrode to generate power. Since the power obtained by the power generation is DC power, the power is converted into AC by the inverter 15 and supplied to the load.

【0014】上記の実施例においては、燃料電池への燃
料ガスの供給は、活性炭製造システムから賦活生成ガス
供給路12を通じて直接供給される水素リッチな賦活生
成ガスのみに頼る構成であるが、これに限られるもので
はなく、賦活生成ガスの生成量が少ない場合に備えて他
の水素ガス供給手段を併設してもよい。また、あるい
は、賦活生成ガスの生成量の増減に対応するため、賦活
生成ガスの生成量が多い場合にこれを貯蔵しておくボン
ベを不純物除去装置13の上段側の賦活発生ガス供給
路、不純物除去装置13と水蒸気濃度調節器14との
間、若しくはCOガス変成器5と燃料電池1との間のい
ずれかの位置に有する構成とすることとしても良い。
In the above embodiment, the supply of the fuel gas to the fuel cell relies only on the hydrogen-rich activated product gas directly supplied from the activated carbon production system through the activated product gas supply passage 12. However, the present invention is not limited to this, and other hydrogen gas supply means may be provided in addition to the case where the amount of the activated product gas is small. Alternatively, in order to cope with an increase or a decrease in the amount of the activated product gas, when the amount of the activated product gas generated is large, a cylinder for storing the activated product gas is supplied to the activation generating gas supply passage on the upper side of the impurity removing device 13. It may be configured to be provided at any position between the removing device 13 and the steam concentration controller 14 or between the CO gas converter 5 and the fuel cell 1.

【0015】[0015]

【発明の効果】本願発明は、燃料電池に供給する燃料ガ
スとして、活性炭の製造工程における賦活反応により生
成するガスを用いることとしたことにより、従来廃棄し
ていた水素の化学エネルギーを有効利用して発電し、省
エネルギーに寄与することができる。また、天然ガス等
の気体原燃料またはメタノール等の液体燃料を改質する
ための改質器を設けなくとも、水素リッチなガスを簡単
な構成で燃料電池に供給することが可能となるので、小
容量・低コストで燃料電池発電システムを提供・運転す
ることが可能である。
According to the present invention, the gas generated by the activation reaction in the production process of activated carbon is used as the fuel gas to be supplied to the fuel cell, so that the chemical energy of conventionally discarded hydrogen can be effectively used. To generate electricity and contribute to energy conservation. Also, it is possible to supply a hydrogen-rich gas to the fuel cell with a simple configuration without providing a reformer for reforming a gaseous fuel such as natural gas or a liquid fuel such as methanol. It is possible to provide and operate a fuel cell power generation system with small capacity and low cost.

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

【図1】本願発明の燃料電池発電システムの概略図FIG. 1 is a schematic diagram of a fuel cell power generation system according to the present invention.

【図2】活性炭製造工程を示す図FIG. 2 is a diagram showing an activated carbon production process.

【図3】従来の燃料電池発電システムの概略図FIG. 3 is a schematic diagram of a conventional fuel cell power generation system.

【符号の説明】[Explanation of symbols]

1 燃料電池 2 脱硫器 3 改質器 4 バーナ 5 CO変成器 6 空気ブロア 10 燃料処理システム 11 賦活炉 12 賦活生成ガス供給路 13 不純物除去装置 14 水蒸気濃度調節器 15 インバータ DESCRIPTION OF SYMBOLS 1 Fuel cell 2 Desulfurizer 3 Reformer 4 Burner 5 CO converter 6 Air blower 10 Fuel treatment system 11 Activation furnace 12 Activation generated gas supply channel 13 Impurity removal device 14 Steam concentration controller 15 Inverter

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】活性炭の製造工程における賦活反応により
生成するガスを燃料電池に供給して発電に用いることを
特徴とする燃料電池発電システム。
1. A fuel cell power generation system, wherein a gas generated by an activation reaction in a production process of activated carbon is supplied to a fuel cell and used for power generation.
【請求項2】前記ガスをCO変成器で一酸化炭素濃度を
低減したのち燃料電池に供給する請求項1に記載の燃料
電池発電装置。
2. The fuel cell power generator according to claim 1, wherein the gas is supplied to a fuel cell after the concentration of carbon monoxide is reduced by a CO converter.
JP11025940A 1999-02-03 1999-02-03 Fuel-cell power generation system Pending JP2000223143A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11025940A JP2000223143A (en) 1999-02-03 1999-02-03 Fuel-cell power generation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11025940A JP2000223143A (en) 1999-02-03 1999-02-03 Fuel-cell power generation system

Publications (1)

Publication Number Publication Date
JP2000223143A true JP2000223143A (en) 2000-08-11

Family

ID=12179765

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11025940A Pending JP2000223143A (en) 1999-02-03 1999-02-03 Fuel-cell power generation system

Country Status (1)

Country Link
JP (1) JP2000223143A (en)

Similar Documents

Publication Publication Date Title
JP6397502B2 (en) Reformer / electrolyzer / refiner (REP) assembly for hydrogen production, system incorporating the assembly, and hydrogen production method
KR101992123B1 (en) Energy storage using an rep with an engine
KR100961838B1 (en) External reforming type molten carbonate fuel cell system
JP4318920B2 (en) Fuel cell system
JPH0395867A (en) Solid electrolyte fuel cell
JP2006031989A (en) Method and system for power generation by solid oxide fuel cell
JP2004520694A5 (en)
JP3644667B2 (en) Fuel cell power generator
JP4403230B2 (en) Operation method of fuel cell power generator
JP3784751B2 (en) Solid oxide fuel cell system
US7311985B2 (en) Device and method for supplying hydrogen to a fuel cell, and the use thereof for electric vehicle traction
JP4112222B2 (en) Operation method of fuel cell reformer
JP2000223143A (en) Fuel-cell power generation system
JP2016184550A (en) Gas manufacturing apparatus
JP3872006B2 (en) Fuel cell power generation system
JP4620399B2 (en) Control method of fuel cell power generation system
JP4442204B2 (en) Fuel cell power generation system
JPS60177571A (en) Coke oven gas energy recovery power-generating method
JP3609961B2 (en) Fuel cell power generator
JP2003178790A (en) Fuel cell power generation system
WO2013150717A1 (en) Hydrogen purification device, hydrogen generation device, and fuel cell system
JP2001146405A (en) Apparatus for reforming fuel and method for operating the same
JP2016184549A (en) Gas production device
JP3932263B2 (en) Solid oxide fuel cell with fuel reforming mechanism
JP2005174783A (en) Solid polymer fuel cell power generating system