JPH02119061A - Methanol reformer of fuel cell - Google Patents

Methanol reformer of fuel cell

Info

Publication number
JPH02119061A
JPH02119061A JP63271271A JP27127188A JPH02119061A JP H02119061 A JPH02119061 A JP H02119061A JP 63271271 A JP63271271 A JP 63271271A JP 27127188 A JP27127188 A JP 27127188A JP H02119061 A JPH02119061 A JP H02119061A
Authority
JP
Japan
Prior art keywords
gas
reformer
load
fuel
burner
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
JP63271271A
Other languages
Japanese (ja)
Inventor
Takashi Oda
小田 貴史
Takashi Koshiba
小柴 孝
Hideo Hagino
秀雄 萩野
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP63271271A priority Critical patent/JPH02119061A/en
Publication of JPH02119061A publication Critical patent/JPH02119061A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
    • 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

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

PURPOSE:To increase load response capability by detecting increase in a load of a cell and thermal instability in a reformer, vaporizing a specified amount of mixed solution by heat exchange with reformer flue gas, and supplying the vaporized gas to a gas burner. CONSTITUTION:Increase in a load is detected with a load current detector 9, and a pump 5 is driven and control valves 7 is opened with an arithmetic output signal of a controller 10. A specified amount of mixed solution is vaporized while it flows in a branch passage 6 with a heat exchanger 8 which is heated with a flue gas, and the vaporized gas is supplied to a gas burner 2 as additional fuel. The supply amount of a reformed fuel is increased with a control valve 11, and fuel gas corresponding to a load is supplied from a reformer to quickly follow load variation. Even when heating value in the reformer is decreased by drop in a flow rate of exhaust fuel gas caused by condensed water in the passages or valves, this is also detected and solved in the same way.

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は燃料電池発電システムのメタノール燃料改質装
;nに関するものである。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to methanol fuel reforming for a fuel cell power generation system;

(ロ)従来の技術 メタノール改質器にお(jる起動時のバーナー燃料は、
燃料タンクの統一化と燃料保安の問題から改質燃料と同
じらのを用いている。これはメタノールと水とをモル比
1 : 1.34で混合したものである。このようなメ
タノール燃焼の場合着火↑↑の悪さから1力噴霧による
霧化燃焼法が採用されるが、流量制御に灯点があり、特
に小量の流量制御では圧力低下を伴い燃焼可能な噴霧形
態をとることは不可能である。そのため噴霧ノズルは、
燃料の最大流量に合わせて選定される。
(b) In the conventional technology methanol reformer, the burner fuel at startup is
The same fuel as reformed fuel is used due to unification of fuel tanks and fuel safety issues. This is a mixture of methanol and water at a molar ratio of 1:1.34. In the case of such methanol combustion, the atomization combustion method using single force spray is adopted due to poor ignition, but there is a key point in controlling the flow rate, especially when controlling the flow rate of a small amount, the pressure decreases and the spray becomes combustible. It is impossible to take any form. Therefore, the spray nozzle
Selected according to maximum fuel flow rate.

−・方電池運転中のバーナー燃料は、改質器で生成して
電池に供給された燃料ガスの排ガスであり、これがガス
バーナーで燃焼され、発電システム全体の燃料効率向上
を図っている。
- Burner fuel during battery operation is the exhaust gas of the fuel gas generated in the reformer and supplied to the battery, which is combusted in the gas burner to improve the fuel efficiency of the entire power generation system.

しかし定常運転中負荷の増大などに対し、バーナーPA
!量不足から改質器で生成する燃料ガス量が不足し、負
荷変動に追従できない。この場合、噴霧バーナーでpj
%歌不足を補償することは前記の如き噴霧バーナーの特
性から実質的に不可能である。
However, due to an increase in load during steady operation, the burner PA
! Due to insufficient quantity, the amount of fuel gas generated by the reformer is insufficient and cannot follow load fluctuations. In this case, pj with a spray burner
It is virtually impossible to compensate for the % loss due to the characteristics of the atomizing burner as described above.

(ハ)発明が解決しようとする課題 本発明は前記問題点を解消し、負荷応答性にすぐれた燃
料電池のメタノール改質装置を提供する乙のである。
(c) Problems to be Solved by the Invention The present invention solves the above-mentioned problems and provides a methanol reforming device for a fuel cell with excellent load responsiveness.

(ニ)課題を解決するための手段 本発明はメタノールと水の混合液を気化・改質して燃料
電池へ供給される燃料ガスを生成する改質器と、始動時
前記混合液を燃焼する噴霧バーナー及び電池作動時前記
燃料ガスの排ガスを燃焼するガスバーナーからなる改質
バーナーとを備え、電池の負荷増大時や改質器内の熱的
不安定時にこれを検出し、H足温合液の所定量を、改質
器煙道ガスとの熱交換により気化1〜で前記ガスバーナ
ーに補給する経路を設けたものである。
(d) Means for Solving the Problems The present invention provides a reformer that vaporizes and reformes a mixture of methanol and water to generate fuel gas to be supplied to a fuel cell, and a reformer that combusts the mixture at startup. It is equipped with a reforming burner consisting of a spray burner and a gas burner that burns the exhaust gas of the fuel gas when the battery is activated, and detects when the load on the battery increases or when there is thermal instability in the reformer, A route is provided for replenishing a predetermined amount of the liquid to the gas burner through vaporization 1 through heat exchange with the reformer flue gas.

(ホ)作用 本発明ではメタノールと水の混合液を改質器煙道ガスで
熱交換して気化し、これを電池から排出される燃料ガス
(改質ガス)の燃料用ガスバーナーに供給して同時燃焼
させることにより、改質器の不足熱漬を補い、電池の負
荷追従性を向上する。
(E) Function In the present invention, a mixture of methanol and water is vaporized by heat exchange with the reformer flue gas, and this is supplied to a fuel gas burner for fuel gas (reformed gas) discharged from the battery. By simultaneously burning the fuel, the insufficient heating of the reformer is compensated for and the load followability of the battery is improved.

(へ)実施例 范電システムはメタノール・水混合液の燃料タンク(T
)、改質器(RF) 、燃料電池(FC)及びインバー
タ(I NV)からなる。
(f) The practical example of the electric power system is a methanol/water mixture fuel tank (T
), a reformer (RF), a fuel cell (FC) and an inverter (INV).

改質器(RF)のバーナーは、前記混合液を燃焼する噴
霧バーナー(1)と電池(FC)から排出ぎバた44ト
燃料ガスを燃焼するガスバーナー(2)とを有する。
The burner of the reformer (RF) has a spray burner (1) that burns the liquid mixture and a gas burner (2) that burns the fuel gas discharged from the battery (FC).

システムの起動時タンク(T)内の混合液が噴霧バーナ
ー(1)で燃焼され、改質器内の温度が所定値に達する
と、混合液が改質燃料として器内の気化部(3)を経て
改質部(4)に供給される。この混合液は気化・改質さ
れて水素リッチガスを生成し、これが燃料ガスとして電
池(FC)に供給される。
When the system is started, the mixed liquid in the tank (T) is burned in the spray burner (1), and when the temperature inside the reformer reaches a predetermined value, the mixed liquid is used as reformed fuel in the vaporization section (3) inside the reformer. It is then supplied to the reforming section (4). This liquid mixture is vaporized and reformed to produce hydrogen-rich gas, which is supplied to the cell (FC) as fuel gas.

このようにして改質器(RF)より燃料ガスが発生する
状態では、噴霧バーナー(1)の燃焼を停止し、電池(
F’ C)からの排燃料ガスをガスバーナー(2)に供
給して燃焼させ、改質器の熱源とする。
In this way, when fuel gas is generated from the reformer (RF), combustion in the spray burner (1) is stopped and the battery (
The exhaust fuel gas from F'C) is supplied to the gas burner (2) and combusted to serve as a heat source for the reformer.

本発明では混合液を噴霧バーナー(1)に供給するポン
プ(5)の下流側より分岐1−てガスバーナー(2)に
至る経路(6)を設け、この経路(6)には、調整弁(
7)及び改質器煙道ガスとの熱交換部(8)が介在して
いる。
In the present invention, a path (6) is provided from the downstream side of the pump (5) that supplies the mixed liquid to the spray burner (1) through a branch 1 to the gas burner (2), and this path (6) has a regulating valve. (
7) and a heat exchange section (8) with the reformer flue gas are interposed.

今負荷(+−)が増大して燃料ガスの利用率が向−卜す
れば、排燃料ガスのガスバーナーでの燃焼が不安定とな
り、改質器内の熱量が不足して改質ガスの発生量も減少
し、負荷の変動に追従することができない。
If the load (+-) increases and the fuel gas utilization rate improves, the combustion of the exhaust fuel gas in the gas burner will become unstable, and the amount of heat in the reformer will be insufficient, causing the reformed gas to The amount generated also decreases, making it impossible to follow load fluctuations.

そのため本発明ではp、荷電流検出1s(9)で負荷の
増大を検出し、制?M器(10)の演算出力信号によリ
ボンブ(5)を駆動すると同時に調整弁(7)を開く。
Therefore, in the present invention, an increase in load is detected and controlled by p and load current detection 1s (9). The control valve (7) is opened at the same time as the ribbon valve (5) is driven by the calculation output signal of the M device (10).

この状態で所定量の混合液は分岐経路(6)を流れる間
に煙道ガスで常に加熱されている熱交換部(8)で直ち
に気化され、ガスバーナー(2)へ追加の燃料として供
給される。これと同時に改質燃料の供給量を調整弁(1
1)により所定量増加し、負荷に応じた燃料ガスを改質
器(RF)より送り出して負荷変動に迅速に追従する。
In this state, while flowing through the branch path (6), a predetermined amount of the mixed liquid is immediately vaporized in the heat exchange section (8), which is constantly heated with flue gas, and is supplied to the gas burner (2) as additional fuel. Ru. At the same time, the supply amount of reformed fuel is adjusted by the regulating valve (1
1), the fuel gas is increased by a predetermined amount and sent out from the reformer (RF) according to the load to quickly follow load fluctuations.

尚負荷変動以外に排燃料ガスの流量が、管路や弁に凝縮
した水分により低下して改質器内の熱量不足が5在生じ
た場合にも、これを検出して前記と同様に対処できる。
In addition to load fluctuations, if the flow rate of exhaust fuel gas decreases due to moisture condensed in the pipes or valves, resulting in a lack of heat in the reformer, this will be detected and dealt with in the same way as above. can.

(ト)  発明の効果 」−述の如く本発明によれば、電池負荷の増大時や改質
器内の熱的不安定時に、これを検出して混合燃料を改質
器煙道ガスどの熱交換により気化し、電池排燃料ガスと
共にガスバーナーで燃焼させることができるので、改質
器の熱量不足を補って負荷変動などに対する追従性を向
」ニすることが可能となり、燃料電池発電システムの特
性改善が達成さね、る。
(g) Effects of the Invention - As described above, according to the present invention, when the battery load increases or the temperature in the reformer becomes unstable, this is detected and the mixed fuel is transferred to the heat of the reformer flue gas. By exchanging it, it can be vaporized and combusted in a gas burner along with the battery exhaust fuel gas, making it possible to compensate for the lack of heat in the reformer and improve response to load fluctuations. Improvement in characteristics has not been achieved.

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

図面は本発明メタノール改質装置を備える燃料電池発電
システムのブロック図である。 T、混合液のタンク、RF:改質器、FC:燃料電池、
INV:インバータ、1:噴霧バーナー、2:ガスバー
ナー、3:気化部、4:改質部、5:燃焼用燃料供給ポ
ンプ、6:分岐経路、7.11:調整弁、9:負荷検出
器、lO二制御組
The drawing is a block diagram of a fuel cell power generation system equipped with the methanol reformer of the present invention. T, mixed liquid tank, RF: reformer, FC: fuel cell,
INV: Inverter, 1: Spray burner, 2: Gas burner, 3: Vaporization section, 4: Reforming section, 5: Combustion fuel supply pump, 6: Branch path, 7.11: Regulating valve, 9: Load detector , lO2 control group

Claims (1)

【特許請求の範囲】 1 メタノールと水の混合液を気化・改質して燃料電池
へ供給される燃料ガスを生成する改質器と、始動時前記
混合液を燃焼する噴霧バーナー及び電池作動時前記電池
の排燃料ガスを燃焼するガスバーナーからなる改質用バ
ーナーとを備え、前記電池の負荷増大時や改質器内の熱
的不安定時にこれを検出して前記混合液の所定量を、前
記改質器煙道ガスとの熱交換により気化して前記ガスバ
ーナーに補給する経路を設けたことを特徴とする燃料電
池のメタノール改質装置。 2 請求項1において、前記経路は、混合液を前記噴霧
バーナーに送る供給ポンプの下流側より分岐し、且調整
弁を有することを特徴とする燃料電池のメタノール改質
装置。
[Scope of Claims] 1. A reformer that vaporizes and reforms a mixture of methanol and water to generate fuel gas to be supplied to a fuel cell, a spray burner that burns the mixture at startup, and when the battery is in operation. and a reforming burner consisting of a gas burner that burns the exhaust fuel gas of the battery, and detects when the load on the battery increases or when there is thermal instability in the reformer and adjusts the predetermined amount of the mixed liquid. . A methanol reforming device for a fuel cell, comprising a path for vaporizing the gas by heat exchange with the reformer flue gas and replenishing the gas burner. 2. The methanol reforming device for a fuel cell according to claim 1, wherein the path branches from a downstream side of a supply pump that sends the mixed liquid to the spray burner, and has a regulating valve.
JP63271271A 1988-10-27 1988-10-27 Methanol reformer of fuel cell Pending JPH02119061A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63271271A JPH02119061A (en) 1988-10-27 1988-10-27 Methanol reformer of fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63271271A JPH02119061A (en) 1988-10-27 1988-10-27 Methanol reformer of fuel cell

Publications (1)

Publication Number Publication Date
JPH02119061A true JPH02119061A (en) 1990-05-07

Family

ID=17497759

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63271271A Pending JPH02119061A (en) 1988-10-27 1988-10-27 Methanol reformer of fuel cell

Country Status (1)

Country Link
JP (1) JPH02119061A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996032753A1 (en) * 1995-04-12 1996-10-17 International Fuel Cells Corporation Fuel processing apparatus having a furnace for fuel cell power plant
EP0920064A1 (en) * 1997-11-26 1999-06-02 General Motors Corporation Fuel cell system with combustor-heated reformer
KR100461270B1 (en) * 2002-06-29 2004-12-10 현대자동차주식회사 Fuel feeding system of fuel cell vehicle
KR100464051B1 (en) * 2002-07-13 2005-01-03 엘지전자 주식회사 Fuel cell system
EP3900917A1 (en) 2020-04-20 2021-10-27 Shibuya Packaging System Corporation Packing machine

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996032753A1 (en) * 1995-04-12 1996-10-17 International Fuel Cells Corporation Fuel processing apparatus having a furnace for fuel cell power plant
US5931658A (en) * 1995-04-12 1999-08-03 International Fuel Cells Fuel cell power plant furnace
EP0920064A1 (en) * 1997-11-26 1999-06-02 General Motors Corporation Fuel cell system with combustor-heated reformer
US6077620A (en) * 1997-11-26 2000-06-20 General Motors Corporation Fuel cell system with combustor-heated reformer
KR100461270B1 (en) * 2002-06-29 2004-12-10 현대자동차주식회사 Fuel feeding system of fuel cell vehicle
KR100464051B1 (en) * 2002-07-13 2005-01-03 엘지전자 주식회사 Fuel cell system
EP3900917A1 (en) 2020-04-20 2021-10-27 Shibuya Packaging System Corporation Packing machine

Similar Documents

Publication Publication Date Title
US6565817B1 (en) Reformer for a fuel cell
JP2003197243A (en) Unified fuel processing equipment for rapid starting and operation control
JP2009504558A (en) Fuel cell system and method for operating reformer
CN107534168A (en) Fuel cell system
CA2365815C (en) Recovery system of heat energy in a fuel cell system
JP2004192958A (en) Fuel cell system
CN108461781B (en) Method for starting up a fuel cell device and fuel cell device
US6887607B1 (en) Fuel cell system for generating electric energy and heat
US20080118795A1 (en) Cogeneration System Using Fuel Cell
WO2020054003A1 (en) Fuel cell system
JPH02119061A (en) Methanol reformer of fuel cell
JP4366285B2 (en) Burner and fuel cell system
JP2003077517A (en) Fuel cell system
JPH07169474A (en) Methanol switching type fuel cell system
JP4346943B2 (en) System using reformer
JP2003529896A (en) Method for vaporizing and / or overheating fuel
JPH01253167A (en) Fuel cell power generator
JPH0773896A (en) Fuel cell power generator
JP2006342047A (en) Reformer, method for controlling pump in fuel cell system, and control unit
JPH0293207A (en) Hot air room-heater
JPH1069919A (en) Fuel cell generating system
JPH0697618B2 (en) Fuel cell power generator
JPS60212971A (en) Fuel cell power generating system and its startng method
JPH0821409B2 (en) Fuel cell generator
JPH0261966A (en) Gasifier of power generator of fuel battery