JP2000351604A - Hydrogen supply system for hydrogen fueled equipment - Google Patents

Hydrogen supply system for hydrogen fueled equipment

Info

Publication number
JP2000351604A
JP2000351604A JP11166212A JP16621299A JP2000351604A JP 2000351604 A JP2000351604 A JP 2000351604A JP 11166212 A JP11166212 A JP 11166212A JP 16621299 A JP16621299 A JP 16621299A JP 2000351604 A JP2000351604 A JP 2000351604A
Authority
JP
Japan
Prior art keywords
hydrogen
storage
storage unit
reformer
storage material
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.)
Granted
Application number
JP11166212A
Other languages
Japanese (ja)
Other versions
JP4229527B2 (en
Inventor
Shigeru Tsunokake
繁 角掛
Masashi Takahashi
昌志 高橋
Masaki Kamiyama
雅樹 上山
Junichi Kitagawa
淳一 北川
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.)
Honda Motor Co Ltd
Japan Metals and Chemical Co Ltd
Original Assignee
Honda Motor Co Ltd
Japan Metals and Chemical 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 Honda Motor Co Ltd, Japan Metals and Chemical Co Ltd filed Critical Honda Motor Co Ltd
Priority to JP16621299A priority Critical patent/JP4229527B2/en
Publication of JP2000351604A publication Critical patent/JP2000351604A/en
Application granted granted Critical
Publication of JP4229527B2 publication Critical patent/JP4229527B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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
    • Y02E60/32Hydrogen storage
    • 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

  • Hydrogen, Water And Hydrids (AREA)
  • Fuel Cell (AREA)

Abstract

(57)【要約】 【課題】 燃料電池の運転開始を迅速に行い、またその
運転を確実に継続することが可能であって、改質器が持
つ問題点が水素供給に影響しないようにした水素供給シ
ステムを提供する。 【解決手段】 水素供給システム1は、アルコール、ガ
ソリン等の原料から水素を生成する改質器3と、改質器
3により生成された水素を吸蔵し、次いでその吸蔵水素
を放出して水素を燃料とする燃料電池2に供給する水素
貯蔵器15とを有する。水素貯蔵器15は、水素を吸蔵
し易い第1貯蔵部151 と、水素を放出し易い第2貯蔵
部152 とを有する。第1貯蔵部151 に改質器3から
の水素を一旦吸蔵させ、その第1貯蔵部151 からの放
出水素を第2貯蔵部152 に吸蔵させておくことによ
り、燃料電池2の運転開始をその第2貯蔵部152 から
の放出水素で行い、その後の燃料電池2の運転継続を第
1貯蔵部151 からの放出水素で行う。
(57) [Summary] [PROBLEMS] To quickly start the operation of a fuel cell and to reliably continue the operation, so that the problems of the reformer do not affect the hydrogen supply. Provide a hydrogen supply system. SOLUTION: A hydrogen supply system 1 includes a reformer 3 that generates hydrogen from a raw material such as alcohol and gasoline, and stores the hydrogen generated by the reformer 3, and then releases the stored hydrogen to generate hydrogen. And a hydrogen storage 15 for supplying the fuel cell 2 as fuel. Hydrogen reservoir 15 has hydrogen as first storage unit 15 1 easily occludes, a second reservoir 15 2 is easy to release hydrogen. Temporarily occluded hydrogen from the reformer 3 in the first storage section 15 1, by keeping the release of hydrogen from the first storage unit 15 1 that is occluded in the second storage unit 15 2, the operation of the fuel cell 2 performed starting with release of hydrogen from the second storage unit 15 2 performs the continuous operation of the subsequent fuel cell 2 with a release hydrogen from the first storage unit 15 1.

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】本発明は水素を燃料とする機
器への水素供給システム、特に、水素を燃料とする機器
に水素を供給すべく、アルコール、ガソリン等の原料か
ら水素を生成するようにした水素供給システムに関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a system for supplying hydrogen to equipment using hydrogen as a fuel, and more particularly to a method for producing hydrogen from a raw material such as alcohol or gasoline to supply hydrogen to equipment using hydrogen as a fuel. Hydrogen supply system.

【0002】[0002]

【従来の技術】従来、この種の水素供給システムは、水
素生成のために改質器を備えている。
2. Description of the Related Art Conventionally, this kind of hydrogen supply system is provided with a reformer for producing hydrogen.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、現状の
改質器は、起動するまでの時間が長く、そのため、前記
機器としての燃料電池を電源とする電気自動車において
は始動スイッチを入れても直ちに発進することができ
ず、また水素生成量増加の要求に対する応答性が鈍く、
そのため電気自動車においてはその加速性が悪い、とい
った問題がある。
However, the current reformer takes a long time to start, and therefore, in an electric vehicle powered by a fuel cell as the device, the reformer starts immediately even if the start switch is turned on. And the response to the demand for increased hydrogen production is slow,
Therefore, the electric vehicle has a problem that its acceleration is poor.

【0004】[0004]

【課題を解決するための手段】本発明は、水素貯蔵器を
備え、そこからの放出水素のみを機器に供給するように
し、これにより、改質器が持つ問題点が機器への水素供
給に影響しないようにした前記水素供給システムを提供
することを目的とする。
SUMMARY OF THE INVENTION The present invention comprises a hydrogen storage device, and supplies only hydrogen released from the hydrogen storage device to the equipment. It is an object of the present invention to provide the hydrogen supply system that has no influence.

【0005】前記目的を達成するため本発明によれば、
アルコール、ガソリン等の原料から水素を生成する改質
器と、前記改質器により生成された水素を吸蔵し、次い
でその吸蔵水素を放出して水素を燃料とする機器に供給
することが可能な水素貯蔵器とを有し、その水素貯蔵器
は、第1の水素吸蔵材を備えた第1貯蔵部と、第2の水
素吸蔵材を備えた第2貯蔵部とを有し、両水素吸蔵材に
おいて、水素の吸蔵し易さに関しては前記第1の水素吸
蔵材が前記第2の水素吸蔵材に比べて優れており、一
方、吸蔵水素の放出し易さに関しては前記第2の水素吸
蔵材が前記第1の水素吸蔵材に比べて優れており、前記
第1貯蔵部に前記改質器からの水素を一旦吸蔵させ、そ
の第1貯蔵部からの放出水素を前記第2貯蔵部に吸蔵さ
せておくことにより、前記機器の運転開始をその第2貯
蔵部からの放出水素で行い、その後の前記機器の運転継
続を前記第1貯蔵部からの放出水素で行う、水素を燃料
とする機器への水素供給システムが提供される。
[0005] To achieve the above object, according to the present invention,
Alcohol, a reformer that generates hydrogen from a raw material such as gasoline, and occludes the hydrogen generated by the reformer, and then releases the occluded hydrogen to supply it to equipment using hydrogen as a fuel A hydrogen storage device, wherein the hydrogen storage device has a first storage portion provided with a first hydrogen storage material and a second storage portion provided with a second hydrogen storage material. In the material, the first hydrogen storage material is superior to the second hydrogen storage material in terms of ease of storing hydrogen, while the second hydrogen storage material is superior in terms of ease of releasing stored hydrogen. The material is superior to the first hydrogen storage material, and the first storage unit temporarily stores hydrogen from the reformer, and the hydrogen released from the first storage unit is stored in the second storage unit. By storing the occlusion, the operation of the device can be started and the hydrogen released from the second storage unit Performed, performs continued operation of subsequent said apparatus with a release hydrogen from the first storage unit, a hydrogen supply system is provided to the equipment using hydrogen as fuel.

【0006】例えば、機器の休止中において改質器を作
動させ、その改質器で生成された水素を第1貯蔵部に吸
蔵させる。この水素の吸蔵は第1の水素吸蔵材が水素を
吸蔵し易い性質を有するので、スムーズに、且つ十分に
行われる。
For example, the reformer is operated while the equipment is at rest, and the hydrogen generated in the reformer is stored in the first storage unit. This hydrogen storage is performed smoothly and sufficiently because the first hydrogen storage material has the property of easily storing hydrogen.

【0007】第1吸蔵部から第2吸蔵部への水素の移送
において、第1吸蔵部からの吸蔵水素の放出は、第1の
水素吸蔵材が水素を放出しにくい性質を持つことを考慮
して、その第1の水素吸蔵材の温度を加熱により高める
ことによって行われ、これにより高圧な放出水素が得ら
れる。第2貯蔵部における第2の水素吸蔵材は水素を吸
蔵しにくい性質を有するが、第1吸蔵部からの放出水素
は高圧であるため第2貯蔵部に十分に吸蔵される。
In the transfer of hydrogen from the first storage unit to the second storage unit, the release of the stored hydrogen from the first storage unit is performed in consideration of the fact that the first hydrogen storage material has a property of hardly releasing hydrogen. This is performed by increasing the temperature of the first hydrogen storage material by heating, whereby high-pressure released hydrogen is obtained. The second hydrogen storage material in the second storage unit has a property of hardly storing hydrogen, but the released hydrogen from the first storage unit is at a high pressure and is sufficiently stored in the second storage unit.

【0008】そして、機器の運転開始時には、第2貯蔵
部より水素を放出させて機器に供給する。この放出水素
の供給は、機器の運転開始時に同時に始動させた改質器
が定常状態に到るまで行われる。第2貯蔵部からの水素
の放出は、第2の水素吸蔵材が水素を放出し易い性質を
有するので、迅速に且つ十分に行われる。
[0008] When the operation of the equipment is started, hydrogen is released from the second storage unit and supplied to the equipment. The supply of the released hydrogen is performed until the reformer started at the same time as the operation start of the apparatus reaches a steady state. The release of hydrogen from the second storage unit is performed quickly and sufficiently because the second hydrogen storage material has a property of easily releasing hydrogen.

【0009】その後の機器の運転継続を第1貯蔵部から
の放出水素で行うので、機器の要求水素量が増加したと
きには第1貯蔵部からの放出水素量を増し、一方、前記
要求水素量が減少したときには第1貯蔵部からの放出水
素量を減らす。
[0009] Since the subsequent operation of the equipment is performed using the hydrogen released from the first storage unit, when the required hydrogen amount of the equipment increases, the amount of hydrogen released from the first storage unit is increased. When the amount decreases, the amount of hydrogen released from the first storage unit is reduced.

【0010】したがって、この水素供給システムによれ
ば、改質器の応答遅れ等の問題点が機器への水素供給に
影響することを回避することができる。
Therefore, according to this hydrogen supply system, it is possible to prevent the problems such as the response delay of the reformer from affecting the hydrogen supply to the equipment.

【0011】[0011]

【発明の実施の形態】図1に示す水素供給システム1
は、水素を燃料とする機器としての燃料電池2を電源と
する電気自動車に搭載される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS A hydrogen supply system 1 shown in FIG.
Is mounted on an electric vehicle powered by a fuel cell 2 as a device using hydrogen as a fuel.

【0012】水素供給システム1において、改質器3
は、アルコール、ガソリン等の原料から水素を生成す
る。また第1,第2調湿器41 ,42 は加湿機能および
除湿機能を有するもので、それらの一端側に第1連通口
1 を、また他端側に第2連通口52 をそれぞれ有す
る。両第1連通口51 間は導管6を介して接続され、そ
の導管6に、第1調湿器51 側より第2調湿器52 側に
向って第1,第2,第3三方弁3V1 ,3V2 ,3V3
が装置される。それらの第1,第2ポートp1,p2は
導管6の第1調湿器51 側と第2調湿器52 側とにそれ
ぞれ接続される。第2三方弁3V2 の第3ポートp3に
は導管7を介して改質器3の供給口8が接続される。ま
た第1,第3三方弁3V1 ,3V3 の第3ポートp3は
導管9,10を介して第4三方弁3V4 の第1,第2ポ
ートp1,p2にそれぞれ接続され、その第4三方弁3
4 の第3ポートp3は導管11を介して燃料電池2の
入口12に接続される。燃料電池2の出口13は第1排
出管141 を介して改質器3の燃焼系に接続され、これ
により燃料電池2の排ガス中の可燃成分が燃焼されて、
その発生熱は改質器3における改質反応に用いられる。
In the hydrogen supply system 1, the reformer 3
Generates hydrogen from raw materials such as alcohol and gasoline. The first, second humidistat 4 1, 4 2 those having a humidifying function and a dehumidifying function, their one end first communication port on the side 5 1 and the other end second communication port on the side 5 2 Have each. Both the first communication port 5 1 between is connected via a conduit 6, its conduit 6, first towards from the first humidistat 5 1 side to the second humidistat 5 2 side, the second, third the three-way valve 3V 1, 3V 2, 3V 3
Is installed. First of them, the second port p1, p2 are respectively connected to the first humidistat 5 1 side and the second humidistat 5 2 side of the conduit 6. Inlet 8 of the reformer 3 is connected via a conduit 7 to the third port p3 of the second three-way valve 3V 2. The first, third port p3 of the third three-way valve 3V 1, 3V 3 first fourth three-way valve 3V 4 via conduit 9 and 10, respectively connected to the second port p1, p2, the fourth Three-way valve 3
The third port p3 of V 4 is connected to the inlet 12 of the fuel cell 2 via a conduit 11. Outlet 13 of the fuel cell 2 is connected to the reformer 3 a combustion system through the first exhaust pipe 14 1, thereby being combustible components in the exhaust gas of the fuel cell 2 is burned,
The generated heat is used for a reforming reaction in the reformer 3.

【0013】第1,第2調湿器41 ,42 の両第2連通
口52 間は導管16を介して接続され、その導管16
に、第1調湿器41 側より第2調湿器42 側に向って第
5,第6,第7三方弁3V5 ,3V6 ,3V7 が装置さ
れる。それらの第1,第2ポートp1,p2は導管16
の第1調湿器41 側と第2調湿器42 側とにそれぞれ接
続され、また第6三方弁3V6 の第3ポートp3は水素
貯蔵器15の入口側に接続される。
[0013] The first, second humidistat 4 1, 4 2 in both the second communication port 5 2 between are connected via a conduit 16, the conduit 16
The fifth, sixth, seventh three-way valve 3V 5, 3V 6, 3V 7 is device towards from the first humidistat 4 1 side to the second humidistat 4 2 side. The first and second ports p1 and p2 are connected to the conduit 16
It is first humidistat 4 1 side and each of the second humidistat 4 2 side of the connection, and the third port p3 of the sixth three-way valve 3V 6 is connected to the inlet side of the hydrogen reservoir 15.

【0014】水素貯蔵器15は、改質器3により生成さ
れた水素を第1または第2調湿器4 1 ,42 を介し供給
されてそれを吸蔵し、またその吸蔵水素を放出して第1
または第2調湿器41 ,42 を介して燃料電池2に供給
することができる。その水素貯蔵器15は、第1の水素
吸蔵材MH1 を備えた第1貯蔵部151 と、第2の水素
吸蔵材MH2 を有する第2貯蔵部152 とを有する。第
1,第2の水素吸蔵材MH1 ,MH2 としては水素吸蔵
合金または炭素材が用いられる。第1の水素吸蔵材MH
1 のプラトー領域を示す温度は第2の水素吸蔵材MH2
のそれよりも高く、したがって改質器3からの比較的高
温な水素の吸蔵し易さに関しては第1の水素吸蔵材MH
1 が第2の水素吸蔵材MH2 に比べて優れているが、常
温下での吸蔵水素の放出し易さに関しては第2の水素吸
蔵材MH2 が第1の水素吸蔵材MH1 に比べて優れてい
る。つまり、両水素吸蔵材MH1 ,MH2 において、水
素吸蔵特性に関しては、同一温度・同一圧力下では第1
の水素吸蔵材MH1 が第2の水素吸蔵材MH2 に比べて
水素吸蔵の平衡圧が低く、一方、水素放出特性に関して
は、同一温度・同一圧力下では第2の水素吸蔵材MH2
が第1の水素吸蔵材MH1 に比べて水素放出の平衡圧が
高いのである。実施例では第1の水素吸蔵材MH1 はA
B5系合金、例えばMmNi4.9 Al0.1 合金よりな
り、また第2の水素吸蔵材MH2 はAB5系合金、例え
ばMmNi4.77Al0.23合金よりなる。各化学式におい
て、Mmはランタン系ミッシュメタルを意味する。
The hydrogen storage 15 is generated by the reformer 3.
The first or second humidity controller 4 1, 4TwoSupply via
And occlude it and release the stored hydrogen to the first
Or the second humidity controller 41, 4TwoTo fuel cell 2 via
can do. The hydrogen storage 15 stores the first hydrogen
Storage material MH11st storage part 15 provided with1And the second hydrogen
Storage material MHTwoSecond storage unit 15 havingTwoAnd No.
1, the second hydrogen storage material MH1, MHTwoAs hydrogen storage
An alloy or a carbon material is used. First hydrogen storage material MH
1The temperature indicating the plateau region of the second hydrogen storage material MHTwo
And therefore relatively high from reformer 3
Regarding the ease of storing hot hydrogen, the first hydrogen storage material MH
1Is the second hydrogen storage material MHTwoIs better than
Regarding the ease of release of stored hydrogen under temperature, the second hydrogen absorption
Storage material MHTwoIs the first hydrogen storage material MH1Better than
You. That is, both hydrogen storage materials MH1, MHTwoAt the water
Regarding element storage characteristics, the first temperature and pressure
Hydrogen storage material MH1Is the second hydrogen storage material MHTwoCompared to
Equilibrium pressure for hydrogen storage is low, while hydrogen release characteristics
Is the second hydrogen storage material MH at the same temperature and the same pressure.Two
Is the first hydrogen storage material MH1The equilibrium pressure of hydrogen release is
It is expensive. In the embodiment, the first hydrogen storage material MH is used.1Is A
B5 series alloy, for example, MmNi4.9Al0.1More than alloy
And the second hydrogen storage material MHTwoIs an AB5-based alloy, for example
MmNi4.77Al0.23Made of alloy. Each chemical formula
Mm means lanthanum-based misch metal.

【0015】第1貯蔵部151 は、第1の水素吸蔵材M
1 を内蔵した少なくとも3つ、図示例では3つの第1
〜第3タンクT1 〜T3 を備え、それらタンクT1 〜T
3 の入口17は導管18により相互に接続され、その導
管18の分岐部19が別の導管20を介して第6三方弁
3V6 の第3ポートp3に接続される。導管18におい
て、各タンクT1 〜T3 の入口17と分岐部19との間
に第1,第2,第3二方弁2V1 ,2V2 ,2V3 がそ
れぞれ装置される。第1〜第3タンクT1 〜T 3 の出口
21は導管22により相互に接続され、その導管22の
集合部23が第2排出管142 を介して第1排出管14
1 の下流側に接続される。導管22において、各タンク
1 〜T3 の出口21と集合部23との間に第8,第
9,第10三方弁3V8 ,3V9 ,3V10がそれぞれ装
置される。それら三方弁3V8 ,3V9 ,3V10の第
1,第2ポートp1,p2は導管22の第1〜第3タン
クT1〜T3 側および集合部23側にそれぞれ接続され
る。第8三方弁3V8 の第3ポートp3は導管24を介
して第11三方弁3V11の第1ポートp1に接続され、
また第9三方弁3V9 および第10三方弁3V10の第3
ポートp3は導管25,26を介して第12三方弁3V
12の第1,第2ポートp1,p2にそれぞれ接続され
る。その第12三方弁3V12の第3ポートp3は導管2
7を介して第11三方弁3V11の第2ポートp2に接続
される。
First storage unit 151Is the first hydrogen storage material M
H1At least three, in the illustrated example, three first
~ Third tank T1~ TThreeAnd the tank T1~ T
ThreeInlets 17 are interconnected by conduits 18
The branch 19 of the pipe 18 is connected via another conduit 20 to a sixth three-way valve.
3V6To the third port p3. Smell in conduit 18
And each tank T1~ TThreeBetween the entrance 17 and the branch 19
First, second, third two-way valve 2V1, 2VTwo, 2VThreeBut
Each is installed. First to third tanks T1~ T ThreeExit
21 are interconnected by a conduit 22,
The collecting part 23 is the second discharge pipe 14TwoThrough the first discharge pipe 14
1Connected to the downstream side. In conduit 22, each tank
T1~ TThreeBetween the outlet 21 and the collecting part 23 of the
9, 10th three-way valve 3V8, 3V9, 3VTenAre individually
Is placed. Those three-way valves 3V8, 3V9, 3VTenNo.
The first and second ports p1 and p2 are the first to third tanks of the conduit 22.
K T1~ TThreeSide and the collecting section 23 side, respectively.
You. 8th 3-way valve 3V8Through the conduit 24
And the 11th three-way valve 3V11Connected to the first port p1 of
9th three-way valve 3V9And 10th three-way valve 3VTenThe third
The port p3 is connected to the twelfth three-way valve 3V via the conduits 25 and 26.
12Connected to the first and second ports p1 and p2, respectively.
You. The 12th three-way valve 3V12The third port p3 of the conduit 2
11th three-way valve 3V through 711Connected to the second port p2
Is done.

【0016】第2貯蔵部152 は第2の水素吸蔵材MH
2 を内蔵した少なくとも1つ、図示例では1つの第4タ
ンクT4 を備える。第4タンクT4 の入口17に導管2
9を介して第13三方弁3V13の第1ポートp1が接続
され、その第2ポートp2は導管30を介して第11三
方弁3V11の第3ポートp3に接続される。第4タンク
4 の出口21に導管32を介して第4二方弁2V4
接続され、その第4二方弁2V4 に導管33を介して第
14三方弁3V14の第1ポートp1が接続される。また
その導管33に第13三方弁3V13の第3ポートp3が
導管34を介して接続される。第14三方弁3V14の第
2ポートp2は導管35を介して第5三方弁3V5 の第
3ポートp3に接続され、また第3ポートp3は導管3
6を介して第7三方弁3V7 の第3ポートp3に接続さ
れる。
The second storage section 15 2 is provided with a second hydrogen storage material MH.
2 at least one with a built-in comprises one of the fourth tank T 4 in the illustrated example. Conduit 2 to the fourth tank T 4 of the inlet 17
The first port p1 of a 13 three-way valve 3V 13 is connected via the 9, its second port p2 is connected to the third port p3 of the 11 three-way valve 3V 11 via a conduit 30. A fourth two-way valve 2V 4 is connected to the outlet 21 of the fourth tank T 4 via a conduit 32, and the first port p1 of the fourteenth three-way valve 3V 14 is connected to the fourth two-way valve 2V 4 via a conduit 33. Is connected. The third port p3 of the 13 three-way valve 3V 13 is connected via conduit 34 to the conduit 33. 14th second port p2 of the three-way valve 3V 14 is connected to the third port p3 of the fifth three-way valve 3V 5 via conduit 35, and the third port p3 conduit 3
Through 6 are connected to the third port p3 of the seventh three-way valve 3V 7.

【0017】第1,第2調湿器41 ,42 は第1貯蔵部
151 の水素吸蔵性を向上させるべく、改質器3からの
水素に除湿処理を施し、また燃料電池2の発電性能を向
上させるべく、放出水素に加湿処理を施す。この場合、
第1,第2調湿器41 ,42の含水量をそれぞれCw
1,Cw2としたとき、例えば、Cw1<Cw2であれ
ば第1調湿器41 が除湿処理に、一方、第2調湿器42
が加湿処理にそれぞれ用いられる。
[0017] The first, second humidistat 4 1, 4 2 in order to improve the first hydrogen absorbing of reservoir 15 1, subjected to a dehumidifying processing hydrogen from the reformer 3 and the fuel cell 2 The released hydrogen is humidified in order to improve the power generation performance. in this case,
The water content of each of the first and second humidifiers 4 1 and 4 2 is calculated as Cw
1, when the Cw2, for example, Cw1 <First humidistat 4 1 dehumidification process if Cw2, while the second humidistat 4 2
Are used for the humidification treatment, respectively.

【0018】このような使用の結果、両含水量Cw1,
Cw2の関係が逆転してCw1>Cw2となれば、第1
調湿器41 は、除湿機能発揮後、加湿機能発揮可能状態
となり、一方、第2調湿器42 は、加湿機能発揮後、除
湿機能発揮可能状態となったもので、今度は第1調湿器
1 が加湿処理に、一方、第2調湿器42 が除湿処理に
それぞれ用いられる。このような使い分は1台の調湿器
によっても可能であるが、2台の調湿器41 ,42 を備
え、それらの間に含水量の差を設けると、除湿および加
湿処理に適確に対応することができる。前記のような除
湿および加湿作用を行うものとしては、モレキュラシー
ブを挙げることができる。
As a result of such use, both water contents Cw1,
If the relationship of Cw2 is reversed and Cw1> Cw2, the first
Humidistat 4 1 after dehumidification function exhibit, become humidifying function capable of exhibiting state, while the second humidistat 4 2 after humidifying function exhibit, which was a dehumidification function capable of exhibiting state, this time the first humidistat 4 1 to the humidifying treatment, while the second humidistat 4 2 are used respectively in the dehumidifying process. Such use content is also possible by one of the humidistat, tone two humidifier 4 1, 4 comprises two, providing a difference in water content between them, the dehumidification and humidification We can respond appropriately. Molecular sieves may be used to perform the dehumidifying and humidifying effects as described above.

【0019】必要に応じて、両調湿器41 ,42 に、改
質器3からの水素に含まれた炭酸ガス、酸素等の不純ガ
ス成分を除去する機能を持たせることができる。図中、
Vは逆止弁である。
If necessary, both humidity controllers 4 1 and 4 2 may have a function of removing impure gas components such as carbon dioxide and oxygen contained in hydrogen from the reformer 3. In the figure,
V is a check valve.

【0020】(1) 例えば、翌朝において電気自動車
の走行を確実に開始させるためには、夜間駐車中であっ
て、燃料電池2の運転休止中に次のような水素貯蔵作業
を行う。便宜上、作業開始前においては水素貯蔵器15
の第1〜第4タンクT1 〜T 4 は空(カラ)状態である
とする。
(1) For example, in the next morning,
To ensure that the vehicle starts
The following hydrogen storage operation is performed while the operation of the fuel cell 2 is stopped.
I do. For convenience, before starting the operation, the hydrogen storage 15
First to fourth tanks T1~ T FourIs empty
And

【0021】(1)−a 図1に示すように、第1,第
2調湿器41 ,42 の両含水量Cw1,Cw2の間には
Cw1≒Cw2の関係が成立し、それらは除湿機能発揮
可能状態にあるものとする。弁切換操作によって、第2
〜第4タンクT2 〜T4 の入口17への経路を遮断した
状態において、改質器3→第2三方弁3V2 →第3三方
弁3V3 →第2調湿器42 →第7三方弁3V7 →第6三
方弁3V6 →第1二方弁2V1 →第1タンクT1 →第8
三方弁3V8 →第2排出管142 の経路を確立させる。
そして改質器3を作動させ、その改質器3で生成された
比較的高温な水素を、除湿処理発揮可能状態にある第2
調湿器42 を経て第1貯蔵部151 の第1タンクT1
吸蔵させる。この水素の吸蔵は第1の水素吸蔵材MH1
が改質器3からの比較的高温な水素を吸蔵し易い性質を
有し、且つその水素に除湿処理が施されているので、ス
ムーズに、且つ十分に行われる。第1の水素吸蔵材MH
1に吸蔵されなかった過剰の水素は第2排出管142
経て改質器3の燃焼系に導かれ、そこで燃焼されて、そ
の発生熱は改質器3における改質反応に用いられる。ま
た水素に含まれ、且つ第1の水素吸蔵材MH1 に吸蔵さ
れない炭酸ガス等の不純ガス成分は第1タンクT1 の出
口21を通じて第2排出管8に排出されるので、第1タ
ンクT1 内における不純ガス成分の濃度上昇が回避され
る。この第1タンクT1 への水素の貯蔵は、そのタンク
1 が充填状態(満状態)となるまで行う。両含水量C
w1,Cw2の関係は、Cw1≒Cw2→Cw1<Cw
2となる。
[0021] (1) As shown in -a Figure 1, first, between the second humidistat 4 1, 4 2 of both moisture content Cw1, Cw2 established relationship Cw1 ≒ Cw2, they It is assumed that the dehumidifying function can be exhibited. By the valve switching operation, the second
In a state in which the path to the inlet 17 of the fourth to fourth tanks T 2 to T 4 is shut off, the reformer 3 → the second three-way valve 3V 2 → the third three-way valve 3V 3 → the second humidity controller 4 2 → the seventh. Three-way valve 3V 7 → Sixth three-way valve 3V 6 → First two-way valve 2V 1 → First tank T 1 → Eighth
The three-way valve 3V 8 → establishing a second path of the discharge pipe 14 2.
Then, the reformer 3 is operated, and the relatively high-temperature hydrogen generated in the reformer 3 is desorbed from the second dehumidification-processable second hydrogen.
Humidistat 4 2 via first occluding the first tank T 1 of the reservoir 15 1. This hydrogen storage is performed by the first hydrogen storage material MH 1
Has the property of easily absorbing relatively high-temperature hydrogen from the reformer 3, and the hydrogen is subjected to a dehumidifying treatment, so that the hydrogen is smoothly and sufficiently performed. First hydrogen storage material MH
Excess hydrogen not occluded in 1 is guided to the reformer 3 a combustion system through the second exhaust pipe 14 2, where it is combusted, the heat generated is used for the reforming reaction in the reformer 3. Further, an impurity gas component such as carbon dioxide which is contained in hydrogen and is not occluded by the first hydrogen storage material MH 1 is discharged to the second discharge pipe 8 through the outlet 21 of the first tank T 1 , so that the first tank T An increase in the concentration of the impurity gas component in 1 is avoided. Storage of hydrogen into the first tank T 1 is carried out until the tank T 1 is a filling state (full state). Both water content C
The relationship between w1 and Cw2 is Cw1 ≒ Cw2 → Cw1 <Cw
It becomes 2.

【0022】(1)−b 第1貯蔵部151 の第1タン
クT1 から第2貯蔵部152 の第4タンクT4 への水素
の移送に当っては、図2に示すように、弁切換操作によ
って、第1タンクT1 の入口17への経路および第4タ
ンクT4 の出口21からの経路をそれぞれ遮断すると共
に、第1タンクT1 →第8三方弁3V8 →第11三方弁
3V11→第13三方弁3V13→第4タンクT4 の経路を
確立させる。第1タンクT1 からの吸蔵水素の放出は、
常温下における第1の水素吸蔵材MH1 の水素を放出し
にくい性質を考慮して、その第1の水素吸蔵材MH1
温度を加熱により60℃以上に高めることによって行わ
れ、これにより高圧な放出水素が得られる。第4タンク
4 における第2の水素吸蔵材MH2 は、第1タンクT
1 からの比較的高温な放出水素を吸蔵しにくい性質を有
するが、その放出水素は高圧でもあるため第4タンクT
4 に十分に吸蔵される。この場合、改質器3による生成
水素を燃焼させて、その燃焼熱により第1の水素吸蔵材
MH1 を加熱することが可能である。第4タンクT4
充填状態となった後はその入口17への経路を弁切換操
作により遮断する(図3参照)。
[0022] (1) from the first tank T 1 of the -b first storage unit 15 1 hitting the transfer of hydrogen into the second storage unit 15 2 of the fourth tank T 4, as shown in FIG. 2, the valve switching operation, the route and the route along with cutting off each of the fourth tank T 4 of the outlet 21, the first tank T 1 → eighth three-way valve 3V 8 → 11 three sides to the first tank T 1 of the inlet 17 to establish a path of the valve 3V 11 → 13 three-way valve 3V 13 → fourth tank T 4. The release of the stored hydrogen from the first tank T 1 is as follows:
Taking into account the first release little aptitude the hydrogen in the hydrogen storage material MH 1 at room temperature under, the first temperature of the hydrogen storage material MH 1 done by increasing the 60 ° C. or higher by heating, thereby the high pressure Hydrogen released. The second hydrogen storage material MH 2 in the fourth tank T 4 is stored in the first tank T 4.
Although it has the property that it is difficult to absorb the relatively high-temperature released hydrogen from the first tank, the released hydrogen is also at a high pressure, so that the fourth tank T
4 occluded enough. In this case, by burning hydrogen produced by the reformer 3, it is possible to heat the first hydrogen storage material MH 1 by the combustion heat. After the fourth tank T 4 becomes filled state blocked by Bensetsu換操operation the route to the inlet 17 (see FIG. 3).

【0023】また弁切換操作により、改質器3→第2三
方弁3V2 →第1三方弁3V1 →第1調湿器41 →第5
三方弁3V5 →第6三方弁3V6 →第3二方弁2V3
第3タンクT3 →第10三方弁3V10→第2排出管14
2 の経路が確立されているので、改質器3で生成された
水素が除湿処理を施された後第3タンクT3 に吸蔵され
る。第3タンクT3 が充填状態となった後はその入口1
7への経路および出口21からの経路を弁切換操作によ
り遮断する(図3参照)。両含水量Cw1,Cw2の関
係は、Cw1<Cw2→Cw1≒Cw2となる。
Further, by the valve switching operation, the reformer 3 → the second three-way valve 3V 2 → the first three-way valve 3V 1 → the first humidity controller 4 1 → the fifth.
Three-way valve 3V 5 → Sixth three-way valve 3V 6 → Third two-way valve 2V 3
Third tank T 3 → Tenth three-way valve 3V 10 → Second discharge pipe 14
Since 2 paths are established, hydrogen produced in the reformer 3 are inserted in the third tank T 3 after being subjected to dehumidifying treatment. After the third tank T 3 has been filled, its inlet 1
The path to 7 and the path from the outlet 21 are shut off by a valve switching operation (see FIG. 3). The relationship between the two water contents Cw1 and Cw2 is Cw1 <Cw2 → Cw1 ≒ Cw2.

【0024】(2) 電気自動車の走行開始時、つまり
燃料電池2の運転開始時において、第1,第2調湿器4
1 ,42 の両含水量Cw1,Cw2の間にはCw1≒C
w2の関係が成立しているものとする。図3に示すよう
に、弁切換操作によって、第4タンクT4 →第4二方弁
2V4 →第14三方弁3V14→第7三方弁3V7 →第2
調湿器42 →第3三方弁3V3 →第4三方弁3V4 →燃
料電池2の経路を確立させる。これにより第2貯蔵部1
2 、つまり第4タンクT4 より水素が放出され、加湿
処理を施された後燃料電池2に供給される。この放出水
素の供給は燃料電池2の運転開始時に同時に始動させた
改質器3が定常状態に到るまで行われる。燃料電池2の
運転に伴い電気自動車が走行する。第4タンクT4 から
の水素の放出は、第2の水素吸蔵材MH2 が常温下で水
素を放出し易い性質を有するので、約25℃でスムーズ
に、且つ十分に行われる。両含水量Cw1,Cw2の関
係は、Cw1≒Cw2→Cw1>Cw2となる。
(2) When the electric vehicle starts running, that is, when the fuel cell 2 starts operating, the first and second humidity controllers 4
Cw1 ≒ C between the water content Cw1 and Cw2 of 1 and 4 2
It is assumed that the relationship of w2 is established. As shown in FIG. 3, the fourth tank T 4 → the fourth two-way valve 2V 4 → the fourteenth three-way valve 3V 14 → the seventh three-way valve 3V 7 → the second by the valve switching operation.
The path of the humidity controller 4 2 → the third three-way valve 3V 3 → the fourth three-way valve 3V 4 → the fuel cell 2 is established. Thereby, the second storage unit 1
5 2 , that is, hydrogen is released from the fourth tank T 4 and supplied to the fuel cell 2 after humidification. The supply of the released hydrogen is performed until the reformer 3 started simultaneously with the start of operation of the fuel cell 2 reaches a steady state. The electric vehicle runs with the operation of the fuel cell 2. The release of hydrogen from the fourth tank T 4 is performed smoothly and sufficiently at about 25 ° C. because the second hydrogen storage material MH 2 has a property of easily releasing hydrogen at room temperature. The relationship between the two water contents Cw1 and Cw2 is Cw1 ≒ Cw2 → Cw1> Cw2.

【0025】(3) 改質器3が定常状態に到ったと
き、図4に示すように弁切換操作によって第4タンクT
4 の出口21からの経路を遮断する。そして第3タンク
3 →第10三方弁3V10→第12三方弁3V12→第1
1三方弁3V11→第13三方弁3V13→第14三方弁3
14→第5三方弁3V5 →第1調湿器41 →第1三方弁
3V1 →第4三方弁3V4 →燃料電池2の経路を確立さ
せる。これにより第3タンクT3 からの放出水素が加湿
処理を施された後燃料電池2に供給されるので電気自動
車の走行が継続される。電気自動車の加速時には、第3
タンクT3 の出口21における開度を広げて放出水素量
を増加し、一方、減速時には、第3タンクT3 の出口2
1における開度を狭めて放出水素量を減少させる。
(3) When the reformer 3 reaches a steady state, the fourth tank T is operated by a valve switching operation as shown in FIG.
The path from the exit 21 of 4 is cut off. And the third tank T 3 → the tenth three-way valve 3V 10 → the twelfth three-way valve 3V 12 → the first
1 three-way valve 3V 11 → 13 three-way valve 3V 13 → 14 three-way valve 3
V 14 → establishing a fifth three-way valve 3V 5 → first humidistat 4 1 → first three-way valve 3V 1 → fourth path of the three-way valve 3V 4 → the fuel cell 2. Thus since the desorbed hydrogen from the third tank T 3 is supplied to the fuel cell 2 after having been subjected to moistening the electric vehicle is traveling it is continued. When accelerating the electric vehicle, the third
The amount of hydrogen released is increased by widening the opening at the outlet 21 of the tank T 3 , while at the time of deceleration, the outlet 2 of the third tank T 3 is increased.
1, the amount of released hydrogen is reduced by narrowing the opening degree.

【0026】また改質器3→第2三方弁3V2 →第3三
方弁3V3 →第2調湿器42 →第7三方弁3V7 →第6
三方弁3V6 →第2二方弁2V2 →第2タンクT2 →第
9三方弁3V9 →第2排出管142 の経路を確立させ
る。これにより改質器3からの水素が除湿処理を施され
た後第2タンクT2 に吸蔵される。両含水量Cw1,C
w2の関係は、Cw1>Cw2→Cw1<Cw2とな
る。
[0026] The reformer 3 → the second three-way valve 3V 2 → the third three-way valve 3V 3 → the second humidistat 4 2 → seventh three-way valve 3V 7 → sixth
The three-way valve 3V 6 → establishing a second two-way valve 2V 2 → second tank T 2 → 9 three-way valve 3V 9 → the second path of the discharge pipe 14 2. Thus the hydrogen from the reformer 3 are inserted into the second tank T 2 after being subjected to dehumidifying treatment. Both water content Cw1, C
The relationship of w2 is Cw1> Cw2 → Cw1 <Cw2.

【0027】図5は図4の場合に次ぐ走行段階を示し、
この段階では第1,第2調湿器41,42 の両含水量C
w1,Cw2の間にCw1<Cw2の関係が成立して、
第2タンクT2 からの水素の放出、第2調湿器42 によ
る放出水素への加湿処理および燃料電池2への加湿後の
放出水素の供給が行われ、また改質器3による水素の生
成、第1調湿器41 による生成水素への除湿処理および
第1タンクT1 における除湿後の生成水素の吸蔵が行わ
れている。これにより両含水量Cw1,Cw2の関係
は、Cw1<Cw2→Cw1>Cw2となる。
FIG. 5 shows the next driving stage after that of FIG.
At this stage, both the water content C of the first and second humidifiers 4 1 and 4 2
The relationship of Cw1 <Cw2 is established between w1 and Cw2,
The release of hydrogen from the second tank T 2 , the humidification of the released hydrogen by the second humidifier 42, and the supply of the released hydrogen after humidification to the fuel cell 2 are performed. production, storage of generated hydrogen after dehumidification in the dehumidifying processing and the first tank T 1 of the the first humidistat 4 1 due to the production of hydrogen is taking place. Thus, the relationship between the two water contents Cw1 and Cw2 is Cw1 <Cw2 → Cw1> Cw2.

【0028】図6は図5の場合に次ぐ走行段階を示し、
この段階では第1,第2調湿器41,42 の両含水量C
w1,Cw2の間にCw1>Cw2の関係が成立して、
第1タンクT1 からの水素の放出、第1調湿器41 によ
る放出水素への加湿処理および燃料電池2への加湿後の
放出水素の供給が行われ、また改質器3による水素の生
成、第2調湿器42 による生成水素への除湿処理および
第3タンクT3 における除湿後の生成水素の吸蔵が行わ
れている。これにより両含水量Cw1,Cw2の関係
は、Cw1>Cw2→Cw1<Cw2となる。
FIG. 6 shows the next driving stage after that of FIG.
At this stage, both the water content C of the first and second humidifiers 4 1 and 4 2
The relationship of Cw1> Cw2 is established between w1 and Cw2,
Release of hydrogen from the first tank T 1, the supply of desorbed hydrogen after humidification to humidification and the fuel cell 2 to the first humidistat 4 1 due to the release of hydrogen takes place, also of hydrogen by the reformer 3 production, storage of generated hydrogen after dehumidification in the second humidistat 4 2 dehumidifying processing and the third tank T 3 to generate hydrogen by is performed. Thus, the relationship between the two water contents Cw1 and Cw2 is Cw1> Cw2 → Cw1 <Cw2.

【0029】このように第1貯蔵部152 においては、
燃料電池2の運転継続下で第1〜第3タンクT1 〜T3
のうち1つのタンクT1 ,T2 ,T3 が水素放出状態に
あるとき、別の1つのタンクT3 ,T1 ,T2 が水素吸
蔵状態にある。
[0029] In this way the first storage unit 15 2,
While the operation of the fuel cell 2 is continued, the first to third tanks T 1 to T 3
When one of the tanks T 1 , T 2 , T 3 is in the hydrogen releasing state, another tank T 3 , T 1 , T 2 is in the hydrogen absorbing state.

【0030】なお、水素貯蔵器15の第1,第2貯蔵部
151 ,152 において、必要に応じ、タンクの数を実
施例の場合よりも増すか、或は第1,第2の吸蔵材MH
1 ,MH2 の量を増して、それら貯蔵部151 ,152
の水素吸蔵能力(水素吸蔵容量)を増大させることが行
われる。また水素を燃料とする機器としては、燃料電池
の外に内燃機関を挙げることができる。
In the first and second storage sections 15 1 and 15 2 of the hydrogen storage device 15, the number of tanks may be increased as required, or the first and second storage sections may be used. Material MH
1 and MH 2 , so that their storages 15 1 , 15 2
To increase the hydrogen storage capacity (hydrogen storage capacity). In addition, examples of equipment using hydrogen as fuel include an internal combustion engine in addition to a fuel cell.

【0031】[0031]

【発明の効果】請求項1記載の発明によれば、前記のよ
うな手段を採用することによって、機器の運転開始を迅
速に行い、またその運転を確実に継続することが可能で
あって、改質器が持つ問題点が水素供給に影響しないよ
うにした水素供給システムを提供することができる。
According to the first aspect of the present invention, by employing the above means, it is possible to quickly start the operation of the equipment and to continue the operation without fail. It is possible to provide a hydrogen supply system in which the problems of the reformer do not affect the hydrogen supply.

【0032】請求項2記載の発明によれば、機器への水
素供給を間断なく行って、その運転を確実に継続し得る
水素供給システムを提供することができる。
According to the second aspect of the present invention, it is possible to provide a hydrogen supply system that can supply hydrogen to equipment without interruption and continue its operation reliably.

【0033】請求項3記載の発明によれば、前記のよう
な手段を採用することによって、水素貯蔵器への水素吸
蔵性を向上させると共に特に、前記機器としての燃料電
池の発電性能を向上させることが可能な水素供給システ
ムを提供することができる。
According to the third aspect of the present invention, by employing the above-described means, the hydrogen storage capacity of the hydrogen storage can be improved, and in particular, the power generation performance of the fuel cell as the device is improved. Capable of providing a hydrogen supply system capable of performing the above.

【0034】請求項4,5記載の発明によれば、水素に
対し加湿処理および除湿処理を確実に施すことが可能な
水素供給システムを提供することができる。
According to the fourth and fifth aspects of the present invention, it is possible to provide a hydrogen supply system capable of reliably performing humidification processing and dehumidification processing on hydrogen.

【0035】請求項6記載の発明によれば、前記のよう
な手段を採用することによって、機器の運転開始を迅速
に行い、またその運転を確実に継続することが可能であ
って、改質器が持つ問題点が水素供給に影響しないよう
にした水素供給システムを提供することができる。
According to the sixth aspect of the present invention, by employing the above-described means, it is possible to quickly start the operation of the equipment and to continue the operation without fail. It is possible to provide a hydrogen supply system in which the problems of the vessel do not affect the hydrogen supply.

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

【図1】燃料電池の運転休止中において、第1タンクに
水素を吸蔵させている状態を示す水素供給システムの説
明図である。
FIG. 1 is an explanatory diagram of a hydrogen supply system showing a state in which hydrogen is stored in a first tank during suspension of operation of a fuel cell.

【図2】第1タンクから第4タンクへ水素を移送し、ま
た第3タンクに水素を吸蔵させている状態を示す水素供
給システムの説明図である。
FIG. 2 is an explanatory diagram of a hydrogen supply system showing a state where hydrogen is transferred from a first tank to a fourth tank and hydrogen is stored in a third tank.

【図3】燃料電池の運転開始時において、第4タンクか
ら水素を放出して燃料電池に供給している状態を示す水
素供給システムの説明図である。
FIG. 3 is an explanatory diagram of a hydrogen supply system showing a state in which hydrogen is released from a fourth tank and supplied to the fuel cell when the fuel cell starts operating.

【図4】電気自動車の走行中において、第3タンクから
水素を放出し、一方、第2タンクに水素を吸蔵させてい
る状態を示す水素供給システムの説明図である。
FIG. 4 is an explanatory diagram of a hydrogen supply system showing a state in which hydrogen is released from a third tank while the electric vehicle is running, and hydrogen is stored in a second tank.

【図5】電気自動車の走行中において、第2タンクから
水素を放出し、一方、第1タンクに水素を吸蔵させてい
る状態を示す水素供給システムの説明図である。
FIG. 5 is an explanatory diagram of a hydrogen supply system showing a state in which hydrogen is released from a second tank and hydrogen is stored in a first tank while the electric vehicle is running.

【図6】電気自動車の走行中において、第1タンクから
水素を放出し、一方、第3タンクに水素を吸蔵させてい
る状態を示す水素供給システムの説明図である。
FIG. 6 is an explanatory diagram of a hydrogen supply system showing a state in which hydrogen is released from a first tank and hydrogen is stored in a third tank while the electric vehicle is running.

【符号の説明】[Explanation of symbols]

1 水素供給システム 2 燃料電池(機器) 3 改質器 41 ,42 第1,第2調湿器 15 水素貯蔵器 151 ,152 第1,第2貯蔵部 Cw1,Cw2 含水量 MH1 ,MH2 第1,第2の水素吸蔵材 T1 ,T2 ,T3 第1,第2,第3タンクREFERENCE SIGNS LIST 1 hydrogen supply system 2 fuel cell (equipment) 3 reformer 4 1 , 4 2 first and second humidifier 15 hydrogen storage 15 1 , 15 2 first and second storage unit Cw1, Cw2 water content MH 1 , MH 2 First and second hydrogen storage materials T 1 , T 2 , T 3 First, second and third tanks

───────────────────────────────────────────────────── フロントページの続き (72)発明者 高橋 昌志 茨城県つくば市東光台5−9−6 日本重 化学工業株式会社筑波研究所内 (72)発明者 上山 雅樹 埼玉県和光市中央1丁目4番1号 株式会 社本田技術研究所内 (72)発明者 北川 淳一 埼玉県和光市中央1丁目4番1号 株式会 社本田技術研究所内 Fターム(参考) 4G040 AA14 AA25 EA02 EA03 EA06 EB31 5H027 AA02 BA01 BA09 BA14  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Masashi Takahashi 5-9-6 Tokodai, Tsukuba, Ibaraki Pref. Inside Tsukuba Research Laboratories, Nippon Heavy Industries, Ltd. (72) Inventor Masaki Ueyama 1-4-4 Chuo, Wako, Saitama No. 1 In Honda R & D Co., Ltd. (72) Inventor Junichi Kitagawa 1-4-1 Chuo, Wako-shi, Saitama F-term in Honda R & D Co., Ltd. (Reference) 4G040 AA14 AA25 EA02 EA03 EA06 EB31 5H027 AA02 BA01 BA09 BA14

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 アルコール、ガソリン等の原料から水素
を生成する改質器(3)と、前記改質器(3)により生
成された水素を吸蔵し、次いでその吸蔵水素を放出して
水素を燃料とする機器(2)に供給することが可能な水
素貯蔵器(15)とを有し、その水素貯蔵器(15)
は、第1の水素吸蔵材(MH1 )を備えた第1貯蔵部
(151 )と、第2の水素吸蔵材(MH2 )を備えた第
2貯蔵部(152 )とを有し、両水素吸蔵材(MH1
MH2 )において、水素の吸蔵し易さに関しては前記第
1の水素吸蔵材(MH1 )が前記第2の水素吸蔵材(M
2)に比べて優れており、一方、吸蔵水素の放出し易
さに関しては前記第2の水素吸蔵材(MH2 )が前記第
1の水素吸蔵材(MH1 )に比べて優れており、前記第
1貯蔵部(151 )に前記改質器(3)からの水素を一
旦吸蔵させ、その第1貯蔵部(151 )からの放出水素
を前記第2貯蔵部(152 )に吸蔵させておくことによ
り、前記機器(2)の運転開始をその第2貯蔵部(15
2 )からの放出水素で行い、その後の前記機器(2)の
運転継続を前記第1貯蔵部(151 )からの放出水素で
行うことを特徴とする、水素を燃料とする機器への水素
供給システム。
1. A reformer (3) for producing hydrogen from a raw material such as alcohol or gasoline, and hydrogen stored by the reformer (3) is absorbed, and then the stored hydrogen is released to produce hydrogen. A hydrogen storage (15) that can be supplied to a device (2) that is a fuel, and the hydrogen storage (15)
Has a first storage unit (15 1 ) provided with a first hydrogen storage material (MH 1 ) and a second storage unit (15 2 ) provided with a second hydrogen storage material (MH 2 ) , Both hydrogen storage materials (MH 1 ,
MH 2 ), the first hydrogen storage material (MH 1 ) is replaced by the second hydrogen storage material (M
H 2 ), while the second hydrogen storage material (MH 2 ) is superior to the first hydrogen storage material (MH 1 ) with respect to the ease of releasing stored hydrogen. the temporarily occluded hydrogen from the reformer (3) to the first reservoir (15 1), said second reservoir (15 2) the release of hydrogen from the first reservoir (15 1) By storing it, the operation of the device (2) can be started at the second storage unit (15).
2 ) the hydrogen released from the first storage unit (15 1 ), and the operation of the device (2) is continued using the hydrogen released from the first storage unit (15 1 ). Feeding system.
【請求項2】 前記第1貯蔵部(151 )は少なくとも
3つのタンク(T1,T2 ,T3 )を備え、前記機器
(2)の運転継続下では、1つの前記タンク(T1 ,T
2 ,T3 )が水素放出状態にあるとき、別の1つの前記
タンク(T3 ,T1 ,T2 )が水素吸蔵状態にある、請
求項1記載の水素を燃料とする機器への水素供給システ
ム。
2. The first storage unit (15 1 ) includes at least three tanks (T 1 , T 2 , T 3 ), and when the operation of the device (2) is continued, one tank (T 1 ) is provided. , T
2, when the T 3) is in the hydrogen release condition, the hydrogen of another one of said tanks (T 3, T 1, T 2) is in the hydrogen storage state, the hydrogen of claim 1, wherein the device for the fuel Feeding system.
【請求項3】 前記改質器(3)からの水素を前記第1
貯蔵部(151 )に吸蔵させる前に、その水素に除湿処
理を施し、また前記第1および第2貯蔵部(151 ,1
2 )からの放出水素を前記機器としての燃料電池
(2)に導入する前に、その放出水素に加湿処理を施
す、2台の調湿器(41 ,42 )を備えている、請求項
1または2記載の水素を燃料とする機器への水素供給シ
ステム。
3. The hydrogen from the reformer (3) is supplied to the first
Before storing the hydrogen in the storage section (15 1 ), the hydrogen is subjected to a dehumidification treatment, and the first and second storage sections (15 1 , 1
The release of hydrogen from 5 2) prior to introduction into the fuel cell (2) as the device performs humidification process to its release hydrogen, and includes two humidistat (4 1, 4 2), 3. A system for supplying hydrogen to equipment using hydrogen as claimed in claim 1 or 2.
【請求項4】 前記両調湿器(41 ,42 )は、除湿機
能発揮後、加湿機能発揮可能状態となり、且つ加湿機能
発揮後、除湿機能発揮可能状態となる、請求項3記載の
水素を燃料とする機器への水素供給システム。
4. The humidifier (4 1 , 4 2 ) according to claim 3, wherein after the dehumidifying function is exhibited, the humidifying function is enabled, and after the humidifying function is activated, the dehumidifying function is enabled. A hydrogen supply system for equipment that uses hydrogen as fuel.
【請求項5】 前記除湿処理に当っては両調湿器
(41 ,42 )のうち含水量(Cw1,Cw2)の少な
い方を使用し、また前記加湿処理に当っては両調湿器
(41 ,42 )のうち含水量(Cw1,Cw2)の多い
方を使用する、請求項3または4記載の水素を燃料とす
る機器への水素供給システム。
5. In the dehumidifying treatment, use one of the two humidifiers (4 1 , 4 2 ) having a smaller water content (Cw1, Cw2). In the humidifying treatment, use both humidifiers. vessel (4 1, 4 2) water content to use one with a lot of (Cw1, Cw2), hydrogen supply system of hydrogen according to claim 3 or 4, wherein the device for the fuel of the.
【請求項6】 アルコール、ガソリン等の原料から水素
を生成する改質器(3)と、前記改質器(3)により生
成された水素を吸蔵し、次いでその吸蔵水素を放出して
水素を燃料とする機器(2)に水素を供給することが可
能な水素貯蔵器(15)とを有し、その水素貯蔵器(1
5)は、第1の水素吸蔵材(MH1 )を備えた第1貯蔵
部(151 )と、第2の水素吸蔵材(MH2 )を備えた
第2貯蔵部(152 )とを有し、両水素吸蔵材(M
1 ,MH2 )において、水素吸蔵特性に関しては、同
一温度・同一圧力下では前記第1の水素吸蔵材(M
1 )が前記第2の水素吸蔵材(MH2 )に比べて水素
吸蔵の平衡圧が低く、一方、水素放出特性に関しては、
同一温度・同一圧力下では前記第2の水素吸蔵材(MH
2)が前記第1の水素吸蔵材(MH1 )に比べて水素放
出の平衡圧が高く、前記第1貯蔵部(151 )に前記改
質器(3)からの水素を一旦吸蔵させ、その第1貯蔵部
(151 )からの放出水素を前記第2貯蔵部(152
に吸蔵させておくことにより、前記機器(2)の運転開
始をその第2貯蔵部(152 )からの放出水素で行い、
その後の前記機器(2)の運転継続を前記第1貯蔵部
(151 )からの放出水素で行うことを特徴とする、水
素を燃料とする機器への水素供給システム。
6. A reformer (3) for producing hydrogen from a raw material such as alcohol or gasoline, and storing the hydrogen generated by the reformer (3), and then releasing the stored hydrogen to generate hydrogen. A hydrogen storage (15) capable of supplying hydrogen to a device (2) serving as a fuel;
5) includes a first storage unit (15 1 ) provided with a first hydrogen storage material (MH 1 ) and a second storage unit (15 2 ) provided with a second hydrogen storage material (MH 2 ). And both hydrogen storage materials (M
H 1 , MH 2 ), the hydrogen storage characteristics of the first hydrogen storage material (M
H 1 ) has a lower hydrogen storage equilibrium pressure than the second hydrogen storage material (MH 2 ).
At the same temperature and the same pressure, the second hydrogen storage material (MH)
2 ) has a higher equilibrium pressure for releasing hydrogen than the first hydrogen storage material (MH 1 ), and causes the first storage section (15 1 ) to temporarily store hydrogen from the reformer (3); The hydrogen released from the first storage unit (15 1 ) is transferred to the second storage unit (15 2 ).
By starting the operation of the device (2) with the hydrogen released from the second storage unit (15 2 ),
A hydrogen supply system for a device using hydrogen as fuel, wherein the operation of the device (2) thereafter is continued using the hydrogen released from the first storage unit (15 1 ).
JP16621299A 1999-06-14 1999-06-14 Hydrogen supply system for equipment using hydrogen as fuel Expired - Fee Related JP4229527B2 (en)

Priority Applications (1)

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Application Number Priority Date Filing Date Title
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JP2000351604A true JP2000351604A (en) 2000-12-19
JP4229527B2 JP4229527B2 (en) 2009-02-25

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002087730A3 (en) * 2001-04-30 2003-04-10 Battelle Memorial Institute Method and apparatus for thermal swing adsorption and thermally-enhanced pressure swing adsorption
US6630012B2 (en) 2001-04-30 2003-10-07 Battelle Memorial Institute Method for thermal swing adsorption and thermally-enhanced pressure swing adsorption

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002087730A3 (en) * 2001-04-30 2003-04-10 Battelle Memorial Institute Method and apparatus for thermal swing adsorption and thermally-enhanced pressure swing adsorption
US6630012B2 (en) 2001-04-30 2003-10-07 Battelle Memorial Institute Method for thermal swing adsorption and thermally-enhanced pressure swing adsorption
US6746515B2 (en) 2001-04-30 2004-06-08 Battelle Memorial Institute Method and apparatus for thermal swing adsorption and thermally-enhanced pressure swing adsorption
US6974496B2 (en) 2001-04-30 2005-12-13 Battelle Memorial Institute Apparatus for thermal swing adsorption and thermally-enhanced pressure swing adsorption

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