JP2000351602A - Hydrogen supply system for hydrogen fueled equipment - Google Patents
Hydrogen supply system for hydrogen fueled equipmentInfo
- Publication number
- JP2000351602A JP2000351602A JP11164940A JP16494099A JP2000351602A JP 2000351602 A JP2000351602 A JP 2000351602A JP 11164940 A JP11164940 A JP 11164940A JP 16494099 A JP16494099 A JP 16494099A JP 2000351602 A JP2000351602 A JP 2000351602A
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- way valve
- storage
- reformer
- supply system
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/32—Hydrogen storage
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Hydrogen, Water And Hydrids (AREA)
- Fuel Cell (AREA)
Abstract
(57)【要約】
【課題】 燃料電池の要求水素量を改質器の応答遅れに
より充足することができない時、その要求水素量を迅速
に充足し得る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して燃料電池2に供給す
る改質器3と、前記水素を貯蔵し、且つ放出することが
可能な水素貯蔵器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。改質器3からの水素に
除湿処理を施した後その水素を第1貯蔵部151 に一旦
吸蔵させ、次いでその吸蔵水素を放出して得られた高圧
な放出水素を第2貯蔵部152 に吸蔵させる。燃料電池
2の要求水素量を改質器3の応答遅れにより充足するこ
とができない時、その要求水素量を充足すべく、第2貯
蔵部152 より水素を放出させ、その放出水素に加湿処
理を施した後燃料電池2に供給する。
(57) [Problem] To provide a hydrogen supply system capable of rapidly filling a required hydrogen amount of a fuel cell when the required hydrogen amount cannot be satisfied due to a response delay of a reformer. A hydrogen supply system (1) includes a reformer (3) that generates hydrogen from a raw material such as alcohol and gasoline and supplies the hydrogen to a fuel cell (2), and a hydrogen storage device that can store and release the hydrogen. 15. The hydrogen storage 15
Hydrogen as first storage unit 15 1 easily absorb, and a second storage unit 15 2 easy to release hydrogen. The hydrogen was subjected to a dehumidification process in the hydrogen from the reformer 3 is temporarily occluded in the first storage section 15 1, and then the high pressure release hydrogen obtained by releasing the occluded hydrogen second storage unit 15 2 Absorb. When it is not possible to satisfy the required amount of hydrogen fuel cell 2 by the response delay of the reformer 3, so as to satisfy the required hydrogen amount, to release hydrogen from the second storage unit 15 2, moisturized in its release hydrogen And then supplied to the fuel cell 2.
Description
【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
ら水素を生成する改質器を備え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 a device using hydrogen as a fuel, and more particularly to a reformer for producing hydrogen from a raw material such as alcohol or gasoline to supply hydrogen to a device using hydrogen as a fuel. The present invention relates to a hydrogen supply system provided with a vessel.
【0002】[0002]
【従来の技術】従来、この種の水素供給システムとして
は、改質器の応答遅れによる燃料電池への水素供給量の
不足分を充足すべく、水素吸蔵材としての水素吸蔵合金
を有する水素貯蔵装置を備えたものが知られている(例
えば、特開平2−56866号公報参照)。2. Description of the Related Art Conventionally, as a hydrogen supply system of this type, a hydrogen storage alloy having a hydrogen storage alloy as a hydrogen storage material has been used in order to satisfy a shortage of hydrogen supply to a fuel cell due to a response delay of a reformer. A device equipped with a device is known (for example, see Japanese Patent Application Laid-Open No. 2-56866).
【0003】[0003]
【発明が解決しようとする課題】水素吸蔵材としては、
水素を吸蔵し易く、また吸蔵水素を放出し易いものが理
想的であるが、現在、知られている水素吸蔵材は、水素
を吸蔵し易いものは水素を放出しにくく、一方、水素を
吸蔵しにくいものは水素を放出し易い、といったように
理想からはほど遠い性質を有する。Problems to be Solved by the Invention As a hydrogen storage material,
Ideally, a material that easily absorbs hydrogen and easily releases hydrogen is ideal.However, currently known hydrogen-absorbing materials are those that easily absorb hydrogen and hardly release hydrogen, while those that occlude hydrogen. Those that are hard to do have properties far from ideal, such as easy release of hydrogen.
【0004】このような状況下において、従来の水素吸
蔵装置に、例えば、水素を放出しにくい水素吸蔵材を用
いた場合には改質器の応答遅れ等による水素供給量の不
足分を迅速に充足することができず、一方、水素を吸蔵
しにくい水素吸蔵材を用いた場合には、吸蔵量不足から
前記水素供給量の不足分を充足することができない、と
いうおそれがある。Under such circumstances, for example, when a hydrogen storage material that does not easily release hydrogen is used in the conventional hydrogen storage device, the shortage of the hydrogen supply amount due to a delay in the response of the reformer or the like can be quickly solved. In the case where a hydrogen storage material that cannot store hydrogen sufficiently is used, there is a possibility that the shortage of the hydrogen supply amount cannot be satisfied due to the insufficient storage amount.
【0005】[0005]
【課題を解決するための手段】本発明は、機器の要求水
素量を改質器により充足することができない時、その要
求水素量を迅速に充足し得る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 It is an object of the present invention to provide a hydrogen supply system capable of quickly filling a required hydrogen amount of a device when the required hydrogen amount cannot be satisfied by a reformer. And
【0006】前記目的を達成するため本発明によれば、
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改質器を備え
た水素供給システムにおいて、前記改質器により生成さ
れた水素を吸蔵し、且つ放出することが可能な水素貯蔵
器を有し、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、前記改質器からの水素に除湿処理を
施した後その水素を前記第1貯蔵部に一旦吸蔵させ、次
いでその吸蔵水素を放出して得られた水素を前記第2貯
蔵部に吸蔵させ、前記機器の要求水素量を前記改質器に
より充足することができない時、その要求水素量を充足
すべく、前記第2貯蔵部より吸蔵水素を放出させる、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。[0006] In order to achieve the above object, according to the present invention,
In a hydrogen supply system including a reformer that generates hydrogen from a raw material such as alcohol or gasoline to supply hydrogen to a device using hydrogen as a fuel, the hydrogen generated by the reformer is absorbed and released. A first storage unit having a first hydrogen storage material, and a second storage unit having a second hydrogen storage material. In both hydrogen storage materials, the first hydrogen storage material is superior to the second hydrogen storage material with respect to the ease of hydrogen storage, while the second hydrogen storage material is superior to the second hydrogen storage material in terms of ease of hydrogen storage. The hydrogen storage material of No. 2 is superior to the first hydrogen storage material, and after dehumidifying the hydrogen from the reformer, the hydrogen is temporarily stored in the first storage unit, and then the hydrogen is stored. The hydrogen obtained by releasing hydrogen is stored in the second storage unit, A hydrogen supply system for hydrogen-fueled equipment, wherein when the required hydrogen amount of equipment cannot be satisfied by the reformer, the stored hydrogen is released from the second storage unit in order to satisfy the required hydrogen amount. Is provided.
【0007】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、それに除湿処
理を施した後第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し、
且つ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。[0007] For example, the reformer is operated while the equipment is at rest, and the hydrogen generated in the reformer is subjected to a dehumidifying process and then stored in the first storage unit. This hydrogen storage has a property that the first hydrogen storage material easily stores hydrogen,
And because the dehumidification treatment is applied to hydrogen,
And it is performed sufficiently.
【0008】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.
【0009】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。[0009] 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. 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.
【0010】[0010]
【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.
【0011】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
もので、その生成された水素を燃料電池2に供給すべ
く、その供給口4が燃料電池2の入口5に供給管6を介
して接続される。燃料電池2の出口7は排出管8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
Is for generating hydrogen from a raw material such as alcohol or gasoline. In order to supply the generated hydrogen to the fuel cell 2, a supply port 4 is connected to an inlet 5 of the fuel cell 2 via a supply pipe 6. You. The outlet 7 of the fuel cell 2 is connected to the combustion system of the reformer 3 via a discharge pipe 8, whereby the fuel cell 2
The combustible components in the exhaust gas are burned, and the generated heat is used for the reforming reaction in the reformer 3.
【0012】供給管6において、その改質器3側に第1
三方弁3V1 が、またその燃料電池2側に第2三方弁3
V2 がそれぞれ装置される。第1三方弁3V1 の第1,
第2ポートp1,p2は供給管6の上流側と下流側とに
それぞれ接続され、また第2三方弁3V2 の第1,第2
ポートp1,p2も、前記同様に供給管6の上流側と下
流側とにそれぞれ接続される。第1三方弁3V1 の第3
ポートp3と第2三方弁3V2 の第3ポートp3とは導
管91 を介して接続され、その導管91 に第3三方弁3
V3 が装置される。その第3三方弁3V3 の第1,第2
ポートp1,p2は導管91 の第1,第2三方弁3
V1 ,3V2 側にそれぞれ接続される。供給管6におけ
る第2三方弁3V2 よりも下流側と、導管91 の第2,
第3三方弁3V2 ,3V3 間とが、別の導管92 を介し
て接続され、その導管92 に第1二方弁2V1 が装置さ
れる。In the supply pipe 6, the first
Three-way valve 3V 1 is also a second three-way valve 3 to the fuel cell 2 side
V 2 are each installed. The first of the first three-way valve 3V 1
Second port p1, p2 upstream and respectively connected to the downstream side, and the first second three-way valve 3V 2 of supply pipe 6, the second
The ports p1 and p2 are connected to the upstream side and the downstream side of the supply pipe 6, respectively, as described above. Third of the first three-way valve 3V 1
Port p3 and the second third port p3 of the three-way valve 3V 2 is connected via a conduit 9 1, 3-way valve 3 to the conduit 9 1
V 3 is the device. The first and second of the third three-way valve 3V3
Port p1, p2 the first conduit 9 1, second three-way valve 3
V 1 and 3V 2 are respectively connected. And downstream of the second three-way valve 3V 2 in the feed pipe 6, the second conduit 9 1,
And between the third three-way valve 3V 2, 3V 3 is connected via another conduit 9 2, first two-way valve 2V 1 is apparatus to the conduit 9 2.
【0013】第1,第2調湿器101 ,102 はそれぞ
れ加湿機能および除湿機能を有し、且つ選択的に使用さ
れるもので、それらの一端側に第1連通口11を、また
他端側に第2連通口12をそれぞれ有する。両第1連通
口11間は導管131 により接続され、その導管131
に第4三方弁3V4 が装置される。第4三方弁3V4の
第1,第2ポートp1,p2は導管131 の第1,第2
調湿器101 ,102側にそれぞれ接続され、また第3
ポートp3は、導管14を介して第3三方弁3V3 の第
3ポートp3に接続される。両第2連通口12間は導管
132 により接続され、その導管132 に第5三方弁3
V5 が装置される。第5三方弁3V5 の第1,第2ポー
トp1,p2は導管132 の第1,第2調湿器101 ,
102 側にそれぞれ接続され、第3ポートp3は導管1
41 を介して水素貯蔵器15の入口側に接続される。そ
の導管141 に第6三方弁3V6 が装置されており、そ
の第1,第2ポートp1,p2は導管141 の第5三方
弁3V5 側と水素貯蔵器15の入口側とにそれぞれ接続
され、第3ポートp3は導管142 を介して水素貯蔵器
15の出口側に接続される。The first and second humidifiers 10 1 and 10 2 have a humidifying function and a dehumidifying function, respectively, and are selectively used. A first communication port 11 is provided at one end of the first and second humidifiers. A second communication port 12 is provided at the other end. During both the first communication port 11 is connected via line 13 1, its conduit 13 1
The fourth three-way valve 3V 4 is apparatus. The fourth three-way valve first 3V 4, second ports p1, p2 the first conduit 13 1, second
Connected to the humidifiers 10 1 and 10 2 , respectively.
Port p3 is connected to the third port p3 of the third three-way valve 3V 3 through a conduit 14. Both second communication port 12 between is connected by a conduit 13 2, the fifth three-way valve 3 to the conduit 13 2
V 5 is the device. The fifth three-way valve first 3V 5, second port p1, p2 the first conduit 13 2, second humidistat 10 1,
It is connected to the 10 2 side, and the third port p3 conduit 1
4 through 1 are connected to the inlet side of the hydrogen reservoir 15. In that conduit 14 1 is the sixth three-way valve 3V 6 is apparatus, the first, second port p1, p2, respectively on the inlet side of the fifth three-way valve 3V 5 side and the hydrogen reservoir 15 of the conduit 14 1 is connected, the third port p3 is connected via a conduit 14 2 on the outlet 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1三方弁3V1 、第3三方弁3V3 、第4
三方弁3V4 、第1または第2調湿器101 ,102 、
第5三方弁3V5 および第6三方弁3V6 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6三
方弁3V6 、第5三方弁3V5 、第1または第2調湿器
101 ,102 、第4三方弁3V4 、第3三方弁3V3
および第2三方弁3V 2 を介し、または第6三方弁3V
6 、第5三方弁3V5 、第1または第2調湿器101 ,
102 、第4三方弁3V4 、第3三方弁3V3 および第
1二方弁2V1を介してそれぞれ燃料電池2に供給する
ことができる。The hydrogen storage 15 is generated by the reformer 3.
3 V of the first three-way valve1, 3rd three-way valve 3VThree, Fourth
Three-way valve 3VFour, First or second humidity controller 101, 10Two,
Fifth three-way valve 3VFiveAnd 6th three-way valve 3V6Supplied via
And occlude it, and release the occluded hydrogen.
3-way valve6, 5th three-way valve 3VFive, First or second humidity controller
101, 10Two, 4th three-way valve 3VFour, 3rd three-way valve 3VThree
And the second three-way valve 3V TwoOr through the sixth three-way valve 3V
6, 5th three-way valve 3VFive, First or second humidity controller 101,
10Two, 4th three-way valve 3VFour, 3rd three-way valve 3VThreeAnd the first
1 two-way valve 2V1To the fuel cell 2 via
be able to.
【0015】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MH1 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MH1 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M
H2 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AB5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MmN
i4.77Al0.23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。[0015] The hydrogen storage unit 15 has first and reservoir 15 1 having a first hydrogen storage material MH 1, the second and the reservoir 15 2 having a second hydrogen storage material MH 2. As the first and second hydrogen storage materials MH 1 and MH 2 , a hydrogen storage alloy or a carbon material is used. Temperature indicating the first plateau region of the hydrogen storage material MH 1 is with respect to a relatively high temperature storage and ease of hydrogen from the second higher than that of the hydrogen storage material MH 2, therefore the reformer 3 first of hydrogen storage material MH 1 is superior to the second hydrogen storage material MH 2, a second hydrogen storage material M with respect to release and ease of occlusion of hydrogen at room temperature under
H 2 is better than the first hydrogen storage material MH 1. In other words, with respect to the hydrogen storage characteristics of the two hydrogen storage materials MH 1 and MH 2 , the first hydrogen storage material MH 1 is more equilibrium in hydrogen storage than the second hydrogen storage material MH 2 under the same temperature and the same pressure. The pressure is low. On the other hand, with respect to the hydrogen release characteristics, at the same temperature and the same pressure, the second hydrogen storage material MH 2
Equilibrium pressure of hydrogen compared to the hydrogen absorption material MH 1 release is higher for. In the embodiment, the first hydrogen storage material MH 1 is made of an AB5 alloy, for example, an MmNi 4.9 Al 0.1 alloy, and the second hydrogen storage material MH 2 is made of an AB5 alloy, for example, MmN
i Made of 4.77 Al 0.23 alloy. In each chemical formula, Mm
Means lantern-based misch metal.
【0016】第1貯蔵部151 は、第1の水素吸蔵材M
H1 を内蔵した1つ以上、図示例では2つの第1,第2
タンクT1 ,T2 を備え、両タンクT1 ,T2 の入口1
9間を接続する導管20に第7三方弁3V7 が装置され
る。第7三方弁3V7 の第1,第2ポートp1,p2は
導管20の第1,第2タンクT1 ,T2 側にそれぞれ接
続され、また第3ポートp3は、第6三方弁3V6 を装
置された導管141 に接続される。両タンクT1 ,T2
の出口21間は導管22により接続され、その導管22
に第8三方弁3V8 が装置される。第8三方弁3V8 の
第1,第2ポートp1,p2は導管22における第1,
第2タンクT1 ,T2 側にそれぞれ接続され、また第3
ポートp3は導管23を介して排出管8に接続される。The first storage unit 15 1, the first hydrogen storage material M
One or more with a built-in H 1, the first two in the illustrated example, the second
Includes a tank T 1, T 2, of both tanks T 1, T 2 inlet 1
Seventh three-way valve 3V 7 is apparatus to the conduit 20 which connects the 9. The seventh three-way valve 3V 7 first, the first second port p1, p2 conduit 20, respectively connected to the second tank T 1, T 2 side, and the third port p3 is the sixth three-way valve 3V 6 is connected to a conduit 14 1 is device. Both tanks T 1 , T 2
Are connected by a conduit 22, and the conduit 22
Eighth three-way valve 3V 8 is apparatus. First in the first, second port p1, p2 conduit 22 of the eighth three-way valve 3V 8,
Connected to the second tanks T 1 and T 2 , respectively.
The port p3 is connected to the discharge pipe 8 via the conduit 23.
【0017】第2貯蔵部152 は第2の水素吸蔵材MH
2 を内蔵した1つ以上、図示例では1つの第3タンクT
3 を備える。第1,第2タンクT1 ,T2 の出口21間
を接続する導管22において、第1タンクT1 および第
8三方弁3V8 間に、別の導管24の一端が接続され、
その他端は第3タンクT3 の入口19に接続される。そ
の導管24に第9三方弁3V9 が装置され、第9三方弁
3V9 の第1,第2ポートp1,p2は導管24の第
1,第3タンクT1 ,T3 側にそれぞれ接続される。ま
た第1,第2タンクT1 ,T2 の出口21間を接続する
導管22において、第2タンクT2 および第8三方弁3
V8 間に、別の導管25の一端が接続され、その他端は
第9三方弁3V9 の第3ポートp3に接続される。第3
タンクT3の出口21に導管26を介して第2二方弁2
V2 が接続され、その第2二方弁2V2 に導管142 が
接続される。なお、実施例では第1〜第3タンクT1 〜
T3の水素吸蔵容量は略等しい。[0017] The second storage unit 15 2 second hydrogen storage material MH
2 one or more with a built-in, one third tank T in the illustrated example
3 is provided. First, in the conduit 22 that connects the second tank T 1, T 2 of the outlet 21, between the first tank T 1 and the eighth three-way valve 3V 8, one end of another conduit 24 is connected,
The other end is connected to the third tank T 3 of the inlet 19. In that the conduit 24 is the ninth three-way valve 3V 9 is device, first ninth three-way valve 3V 9, second port p1, p2 are respectively connected to the first, third tank T 1, T 3 side of the conduit 24 You. In a conduit 22 connecting the outlets 21 of the first and second tanks T 1 and T 2 , a second tank T 2 and an eighth three-way valve 3 are connected.
Between V 8, one end of another conduit 25 is connected, the other end thereof is connected to the third port p3 of the ninth three-way valve 3V 9. Third
The second two-way valve via a conduit 26 to the outlet 21 of the tank T 3 2
V 2 is connected, the conduit 14 2 is connected to the second two-way valve 2V 2. In the embodiment, the first to third tanks T 1 to T 1 are used .
Hydrogen storage capacity of T 3 are substantially equal.
【0018】第1,第2調湿器101 ,102 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101,102 の含水量をそれぞ
れCw1,Cw2としたとき、例えば、Cw1<Cw2
であれば第1調湿器101 が除湿処理に、一方、第2調
湿器102 が加湿処理にそれぞれ用いられる。[0018] The first, second humidistat 10 1, 10 2 in order to improve the hydrogen absorption properties of the first storage unit 15 1 performs the dehumidifying process to 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, when the water contents of the first and second humidity controllers 10 1 and 10 2 are respectively Cw1 and Cw2, for example, Cw1 <Cw2
If the first humidistat 10 1 dehumidification process, while the second humidistat 10 2 are used respectively in the humidification.
【0019】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101 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102 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101 が加湿処理に、一方、第2調湿器102 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10
1 ,102 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
The humidifier 10 1 is in a state in which the humidifying function can be exhibited after the dehumidifying function is exhibited, while the second humidifier 10 2 is in a state in which the dehumidifying function can be exhibited after the humidifying function is exhibited.
Humidistat 10 1 to moistening, while the second humidistat 10 2 are used respectively in the dehumidifying process. Such usage is 1
Although two humidifiers are also possible, two humidifiers 10
By providing 1 and 10 2 and providing a difference in water content between them, it is possible to appropriately cope with dehumidification and humidification. Molecular sieves may be used to perform the dehumidifying and humidifying effects as described above.
【0020】必要に応じて、両調湿器101 ,10
2 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 10 1 , 10
The function of removing impurity gas components such as carbon dioxide and oxygen contained in hydrogen from the reformer 3 can be given to the second. In the figure, V is a check valve.
【0021】(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3タンクT1 〜T 3 は空(カラ)状態である
とする。各図面において、「E」は空状態を、また
「F」は充填状態(満状態)を、さらに「<F/E」は
水素が放出されて、空ではないが充填状態でもない状態
(<F)か、または空状態(E)にあることをそれぞれ
示す。(1) For example, in the next morning, an electric vehicle
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 third tanks T1~ T ThreeIs empty
And In each drawing, “E” indicates an empty state, and
“F” indicates the filled state (full state), and “<F / E” indicates
Hydrogen is released and is not empty but not filled
(<F) or empty (E) respectively
Show.
【0022】(1)−a 図1に示すように、第9三方
弁3V9 を切換えて、第1貯蔵部151 の第1タンクT
1 →第9三方弁3V9 →第2貯蔵部152 の第3タンク
T3の経路を遮断する。また第2二方弁2V2 を切換え
て、第3タンクT3 →第2二方弁2V2 →第6三方弁3
V6 の経路を遮断する。この場合、第1,第2調湿器1
01 ,102 の両含水量Cw1,Cw2の間にはCw1
<Cw2の関係が成立しているものとする。[0022] (1) As shown in -a Figure 1, it switches the ninth three-way valve 3V 9, the first tank T of the first reservoir 15 1
1 → 9 three-way valve 3V 9 → the second path of the third tank T 3 of the reservoir 15 2 to block. Further, the second two-way valve 2V 2 is switched so that the third tank T 3 → the second two-way valve 2V 2 → the sixth three-way valve 3
To cut off the route of V 6. In this case, the first and second humidity controllers 1
0 1, 10 both moisture content of 2 Cw1, between Cw2 Cw1
It is assumed that the relationship of <Cw2 is established.
【0023】この状態において、第1,第3〜第8三方
弁3V1 ,3V3 〜3V8 を切換えて、改質器3→第1
三方弁3V1 →第3三方弁3V3 →第4三方弁3V4 →
第1調湿器101 →第5三方弁3V5 →第6三方弁3V
6 →第7三方弁3V7 →第1タンクT1 →第8三方弁3
V8 →排出管8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1調湿器101 を経
て第1貯蔵部151 の第1タンクT1 に吸蔵させる。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MH1 に吸蔵されな
かった過剰の水素は排出管8を経て改質器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T1 が充填状態(満状態)と
なるまで行う。In this state, the first, third to eighth three-way valves 3V 1 , 3V 3 to 3V 8 are switched, and the reformer 3 → first
3-way valve 3V 1 → 3rd 3-way valve 3V 3 → 4th 3-way valve 3V 4 →
1st humidity controller 10 1 → 5th 3-way valve 3V 5 → 6th 3-way valve 3V
6 → 7th 3-way valve 3V 7 → 1st tank T 1 → 8th 3-way valve 3
V 8 → Establish the path of the discharge pipe 8. The reformer 3 is actuated and the reformer at a relatively high temperature hydrogen produced by 3, first the first storage unit 15 1 via the first humidistat 10 1 in the process exert state dehumidification to be inserted in the tank T 1. Since the first hydrogen storage material MH 1 has a property of easily storing relatively high-temperature hydrogen from the reformer 3 and the hydrogen has been subjected to the dehumidifying treatment, the hydrogen is stored smoothly. And it is performed sufficiently. Excess hydrogen not stored in the first hydrogen storage material MH 1 is led to the combustion system of the reformer 3 through the discharge pipe 8 and burned there, and the generated heat is converted by the reforming reaction in the reformer 3. Used for Impurity gas components, such as carbon dioxide, which are contained in hydrogen and are not occluded by the first hydrogen storage material MH 1 , are discharged through the outlet 21 of the first tank T 1 through the outlet 21.
Is exhausted, the concentration increase of the impurity gas component in the first tank T 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).
【0024】(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3タンクT3 への水素
の移送に当っては、図2に示すように、第7,第8三方
弁3V7 ,3V8 を切換えて、第1調湿器101 →第5
三方弁3V5 →第6三方弁3V6 →第7三方弁3V7 →
第1タンクT1 →第8三方弁3V8 →排出管8の経路を
遮断すると共に、第9三方弁3V9 を切換えて、第1タ
ンクT1 →第9三方弁3V9 →第3タンクT3 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 の
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3タンク
T3 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3タンクT
3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。[0024] (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 third tank T 3, as shown in FIG. 2, By switching the seventh and eighth three-way valves 3V 7 and 3V 8 , the first humidity controller 10 1 → fifth
Three-way valve 3V 5 → Sixth three-way valve 3V 6 → Seventh three-way valve 3V 7 →
The first tank T 1 → the eighth three-way valve 3V 8 → the path of the discharge pipe 8 is cut off, and the ninth three-way valve 3V 9 is switched to the first tank T 1 → the ninth three-way valve 3V 9 → the third tank T Establish the route of 3 . 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 third tank T 3
Although it has a property that it is difficult to occlude the relatively high-temperature released hydrogen from the first tank, the third tank T
3 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.
【0025】また第7,第8三方弁3V7 ,3V8 の切
換えにより、改質器3→第1三方弁3V1 →第3三方弁
3V3 →第4三方弁3V4 →第1調湿器101 →第5三
方弁3V5 →第6三方弁3V6 →第7三方弁3V7 →第
2タンクT2 →第8三方弁3V8 →排出管8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第2タ
ンクT2 に吸蔵される。By switching the seventh and eighth three-way valves 3V 7 and 3V 8 , the reformer 3 → the first three-way valve 3V 1 → the third three-way valve 3V 3 → the fourth three-way valve 3V 4 → the first humidity control. Since the route of the vessel 10 1 → the fifth three-way valve 3V 5 → the sixth three-way valve 3V 6 → the seventh three-way valve 3V 7 → the second tank T 2 → the eighth three-way valve 3V 8 → the discharge pipe 8 is established, is hydrogen produced in the reformer 3 are inserted into the second tank T 2.
【0026】(1)−c 図3に示すように、第3タン
クT3 が充填状態となり、一方、第1タンクT1 が空状
態となったとき、第9三方弁3V9 を切換えて第1タン
クT 1 →第9三方弁3V9 →第3タンクT3 の経路を遮
断する。また第2タンクT2が充填状態となったとき、
第7,第8三方弁3V7 ,3V8 を切換えて、再び、改
質器1→第1三方弁3V1 →第3三方弁3V3 →第4三
方弁3V4→第1調湿器101 →第5三方弁3V5 →第
6三方弁3V6 →第7三方弁3V7 →第1タンクT1 →
第8三方弁3V8 →排出管8の経路を確立させて第1タ
ンクT1 に水素を吸蔵させる。(1) -c As shown in FIG.
K TThreeIs filled, while the first tank T1Is empty
State, when the ninth three-way valve 3V9Switch to the first
K T 1→ 9th three-way valve 3V9→ Third tank TThreeBlock the path of
Refuse. The second tank TTwoWhen is filled
Seventh and eighth three-way valves 3V7, 3V8And switch again
Porcelain 1 → First three-way valve 3V1→ 3rd three-way valve 3VThree→ No.43
3-way valve 3V4-> first humidity controller 101→ Fifth three-way valve 3VFive→ No.
6 three-way valve 3V6→ 7th three-way valve 3V7→ First tank T1→
8th 3-way valve 3V8→ Establish the route of the discharge pipe 8 and
Link T1To absorb hydrogen.
【0027】(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1
01 ,102 の両含水量Cw1,Cw2の間にはCw1
<Cw2の関係が成立しているものとする。図4に示す
ように、第2,第3,第4三方弁3V2 ,3V3 ,3V
4 および第1二方弁2V1 の切換えによって、第2調湿
器102 →第4三方弁3V4 →第3三方弁3V3 →第2
三方弁3V2 →燃料電池2の経路が確立されると共に第
1二方弁2V1 が導管18を遮断している状態におい
て、第5,第6三方弁3V5 ,3V6 および第2二方弁
2V2 を切換えて第3タンクT3 →第2二方弁2V2 →
第6三方弁3V6 →第5三方弁3V5 →第2調湿器10
2 の経路を確立させる。これにより第2貯蔵部152 、
つまり第3タンクT3 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3タンクT3 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。(2) When the electric vehicle starts running, that is, when the fuel cell 2 starts operating, the first and second humidifiers 1
0 1, 10 both moisture content of 2 Cw1, between Cw2 Cw1
It is assumed that the relationship of <Cw2 is established. As shown in FIG. 4, the second, third, and fourth three-way valves 3V 2 , 3V 3 , and 3V
By 4 and the first two-way valve 2V 1 switching, second humidistat 10 2 → fourth three-way valve 3V 4 → the third three-way valve 3V 3 → second
Three-way valve 3V 2 → Fifth and sixth three-way valves 3V 5 , 3V 6 and second two-way valve 3V 2 in a state where the path of fuel cell 2 is established and first two-way valve 2V 1 shuts off conduit 18. Switch the valve 2V 2 to the third tank T 3 → the second two-way valve 2V 2 →
6th 3-way valve 3V 6 → 5th 3-way valve 3V 5 → 2nd humidity controller 10
Establish the second route. Thereby, the second storage unit 15 2 ,
That is, hydrogen is released from the third tank T 3 , and is 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. Release of hydrogen from the third tank T 3 is performed smoothly and sufficiently at about 25 ° C. since the second hydrogen storage material MH 2 has a property of easily releasing hydrogen at room temperature.
【0028】この間に、第1三方弁3V1 を切換えて改
質器3→第1三方弁3V1 →第3三方弁3V3 →第4三
方弁3V4 →第2調湿器102 の経路を遮断し、一方、
改質器3→第1三方弁3V1 →第2三方弁3V2 の経路
を確立させておく。[0028] During this time, it switches the first three-way valve 3V 1 reformer 3 → the first three-way valve 3V 1 → the third three-way valve 3V 3 → fourth three-way valve 3V 4 → the second humidistat 10 second path Shut off, while
A path from the reformer 3 to the first three-way valve 3V 1 → the second three-way valve 3V 2 is established.
【0029】(3) 改質器3が定常状態に到ったと
き、図5に示すように第2三方弁3V 2 を切換えて、改
質器3→第1三方弁3V1 →第2三方弁3V2 →燃料電
池2の経路を確立させる。これにより電気自動車の走行
が継続される。また第2二方弁2V2 を切換えて、第3
タンクT3 →第2二方弁2V2 →第6三方弁3V6 →第
5三方弁3V5 →第2調湿器102 の経路を遮断すると
共に第9三方弁3V9 を切換えて、第2タンクT2 →第
9三方弁3V9 →第3タンクT3 の経路を確立させる。
これにより、水素を第2タンクT2 から第3タンクT3
に移送することができる。(3) When the reformer 3 reaches a steady state
As shown in FIG. 5, the second three-way valve 3V TwoSwitch to
Porcelain 3 → First three-way valve 3V1→ 2nd three-way valve 3VTwo→ Fuel electricity
The path of pond 2 is established. This allows electric vehicles to run
Is continued. The second two-way valve 2VTwoSwitch to the third
Tank TThree→ 2nd 2-way valve 2VTwo→ 6th three-way valve 3V6→ No.
5 three-way valve 3VFive→ Second humidifier 10TwoWhen you block the route of
Both 9th three-way valve 3V9Is switched to the second tank TTwo→ No.
9 three-way valve 3V9→ Third tank TThreeEstablish a route.
As a result, hydrogen is stored in the second tank TTwoFrom the third tank TThree
Can be transferred to
【0030】図6に示すように、第3タンクT3 が充填
状態となり、一方、第2タンクT2が空状態となったと
き、第9三方弁3V9 を切換えて第2タンクT2 →第9
三方弁3V9 →第3タンクT3 の経路を遮断する。また
第7,第8三方弁3V7 ,3V8 を切換えて、第7三方
弁3V7 →第2タンクT2 →第8三方弁3V8 →排出管
8の経路を確立させる。As shown in FIG. 6, when the third tank T 3 is in the filling state and the second tank T 2 is in the empty state, the ninth three-way valve 3V 9 is switched to switch the second tank T 2 → Ninth
Path of the three-way valve 3V 9 → third tank T 3 is cut off. Further, the seventh and eighth three-way valves 3V 7 and 3V 8 are switched to establish the path of the seventh three-way valve 3V 7 → the second tank T 2 → the eighth three-way valve 3V 8 → the discharge pipe 8.
【0031】(4) 前記水素貯蔵過程で第1調湿器1
01 が水素の除湿処理に用いられたことからその含水量
Cw1が増加し、一方、前記運転開始過程で第2調湿器
10 2 が水素の加湿処理に用いられたことからその含水
量Cw2が減少し、その結果、電気自動車の加速時に
は、第1,第2調湿器101 ,102 の両含水量Cw
1,Cw2の間にはCw1>Cw2の関係が成立してい
るものとする。(4) The first humidity controller 1 in the hydrogen storage process
01Was used for the dehumidification of hydrogen and its water content
Cw1 increases, while the second humidity controller
10 TwoWas used for humidification of hydrogen,
The quantity Cw2 decreases, and as a result, when the electric vehicle accelerates
Is the first and second humidity controller 101, 10TwoBoth water content Cw
1 and Cw2, the relationship of Cw1> Cw2 holds.
Shall be.
【0032】また電気自動車の加速時には、改質器3の
応答遅れにより、その改質器3の水素供給量が燃料電池
2の要求水素量に満たなくなる。この場合には、図7に
示すように第4,第5三方弁3V4 ,3V5 および第
1,第2二方弁2V1 ,2V2を切換えて、第3タンク
T3 →第2二方弁2V2 →第6三方弁3V6 →第5三方
弁3V5 →第1調湿器101 →第4三方弁3V4 →第3
三方弁3V3 →第1二方弁2V1 →燃料電池2の経路を
確立させ、改質器3による水素量の不足分を第3タンク
T3 からの放出水素により充足する。When the electric vehicle is accelerating, the hydrogen supply amount of the reformer 3 becomes less than the required hydrogen amount of the fuel cell 2 due to a response delay of the reformer 3. In this case, as shown in FIG. 7, the fourth and fifth three-way valves 3V 4 and 3V 5 and the first and second two-way valves 2V 1 and 2V 2 are switched to change the third tank T 3 → the second second valve. 2-way valve 2V 2 → 6th 3-way valve 3V 6 → 5th 3-way valve 3V 5 → 1st humidity controller 10 1 → 4th 3-way valve 3V 4 → 3rd
The three-way valve 3V 3 → to establish a first two-way valve 2V 1 → path of the fuel cell 2, the shortage of the amount of hydrogen by the reformer 3 filled by releasing hydrogen from the third tank T 3.
【0033】改質器3からの水素供給量が燃料電池2の
要求水素量を満たしたとき、第1,第2二方弁2V1 ,
2V2 を図6に示したごとく切換えて、前記経路、つま
り第3タンクT3 →……→燃料電池2の経路を遮断す
る。第3タンクT3 における水素消費量は第1タンクT
1 からの水素の移送により充足される。When the amount of hydrogen supplied from the reformer 3 satisfies the required amount of hydrogen of the fuel cell 2, the first and second two-way valves 2V 1 ,
Switches as showed 2V 2 in FIG. 6, to cut off the path, that is, the third tank T 3 → ...... → path of the fuel cell 2. The hydrogen consumption in the third tank T 3 is
Filled by transfer of hydrogen from 1 .
【0034】(5) 電気自動車の減速時においても第
1,第2調湿器101 ,102 の両含水量Cw1,Cw
2の間にはCw1>Cw2の関係が成立しているものと
する。図8に示すように、第1,第3〜第6三方弁3V
1 ,3V3 〜3V6 を切換えて、改質器3→第1三方弁
3V1 →第3三方弁3V3 →第4三方弁3V4 →第2調
湿器102 →第5三方弁3V5 →第6三方弁3V5 →第
7三方弁3V7 →第2タンクT2 →第8三方弁3V8 →
排出管8の経路を確立させ、これにより改質器3の応答
遅れによる余剰水素を第2タンクT2 に吸蔵させる。第
2タンクT2 が充填状態となれば、余剰水素は第1タン
クT1 に充填される。(5) Even when the electric vehicle decelerates, both the water contents Cw1, Cw of the first and second humidity controllers 10 1 , 10 2 are obtained.
It is assumed that the relationship of Cw1> Cw2 holds between the two. As shown in FIG. 8, the first, third to sixth three-way valves 3V
1, 3V 3 by switching the ~3V 6, the reformer 3 → first three-way valve 3V 1 → third three-way valve 3V 3 → fourth three-way valve 3V 4 → second humidistat 10 2 → fifth three-way valve 3V 5 → 6th 3-way valve 3V 5 → 7th 3-way valve 3V 7 → 2nd tank T 2 → 8th 3-way valve 3V 8 →
To establish a path of the discharge pipe 8, thereby occluding the excess hydrogen due to the response delay of the reformer 3 to the second tank T 2. If the second tank T 2 is familiar with the filling state, the excess hydrogen is filled in the first tank T 1.
【0035】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.
【0036】[0036]
【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、水素貯蔵器への水素
吸蔵性を向上させ、また機器の要求水素量を改質器によ
り充足することができない時、その要求水素量を水素貯
蔵器により迅速に充足す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 first aspect of the present invention, by adopting the above means, the hydrogen storage capacity of the hydrogen storage can be improved, and the required amount of hydrogen of the equipment can be satisfied by the reformer. When it is not possible to do so, it is possible to provide a hydrogen supply system capable of quickly filling the required amount of hydrogen with the hydrogen storage.
【0037】請求項2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、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 second aspect of the present invention, it is possible to provide a hydrogen supply system capable of improving the power generation performance of a fuel cell as the device by employing the above means. it can.
【0038】請求項3〜5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
で、且つ利便性のある調湿器を備えた水素供給システム
を提供することができる。According to the third to fifth aspects of the present invention, it is possible to provide a hydrogen supply system having a humidifier that is capable of reliably performing humidification processing and dehumidification processing on hydrogen and that has a convenient humidifier. Can be.
【0039】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、水素貯蔵器への水素吸
蔵性を向上させ、また機器の要求水素量を改質器により
充足することができない時、その要求水素量を水素貯蔵
器により迅速に充足す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 sixth aspect of the present invention, by adopting the above means, the hydrogen storage capacity of the hydrogen storage can be improved, and the required amount of hydrogen of the equipment can be satisfied by the reformer. When it is not possible to provide a hydrogen supply system, the required amount of hydrogen can be more quickly satisfied by the hydrogen storage.
【図1】燃料電池の運転休止中において、第1タンクに
水素を充填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. 1 is an explanatory diagram of a hydrogen supply system showing a state in which a first tank is being filled with hydrogen while a fuel cell is stopped.
【図2】第1タンクから第3タンクへ水素を移送し、ま
た第2タンクに水素を充填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. 2 is an explanatory diagram of a hydrogen supply system showing a state in which hydrogen is transferred from a first tank to a third tank and a second tank is filled with hydrogen.
【図3】第1タンクに再び水素を充填している状態を示
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 where a first tank is filled with hydrogen again.
【図4】燃料電池の運転開始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 an operation start state of a fuel cell.
【図5】電気自動車が走行し、また第2タンクから第3
タンクへ水素を移送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. 5 shows a state in which the electric vehicle is running,
It is explanatory drawing of the hydrogen supply system which shows the state which is transferring hydrogen to a tank.
【図6】電気自動車が走行し、また第2タンクに再び水
素を充填し得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 the hydrogen supply system showing a state in which the electric vehicle is running and the second tank can be filled with hydrogen again.
【図7】電気自動車の加速状態を示す水素供給システム
の説明図である。FIG. 7 is an explanatory diagram of a hydrogen supply system showing an acceleration state of the electric vehicle.
【図8】電気自動車の減速状態を示す水素供給システム
の説明図である。FIG. 8 is an explanatory diagram of a hydrogen supply system showing a deceleration state of the electric vehicle.
1 水素供給システム 2 燃料電池(機器) 3 改質器 101 ,102 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REFERENCE SIGNS LIST 1 hydrogen supply system 2 fuel cell (equipment) 3 reformer 10 1 , 10 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
───────────────────────────────────────────────────── 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 AA13 AA23 AA25 AA29 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 Inside Honda R & D Co., Ltd. (72) Inventor Junichi Kitagawa 1-4-1 Chuo, Wako-shi, Saitama F-term inside Honda R & D Co., Ltd. 4G040 AA13 AA23 AA25 AA29 5H027 AA02 BA01 BA09 BA14
Claims (6)
給すべく、アルコール、ガソリン等の原料から水素を生
成する改質器(3)を備えた水素供給システムにおい
て、前記改質器(3)により生成された水素を吸蔵し、
且つ放出することが可能な水素貯蔵器(15)を有し、
その水素貯蔵器(15)は、第1の水素吸蔵材(M
H1 )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(MH2 )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(M
H1 )に比べて優れており、前記改質器(3)からの水
素に除湿処理を施した後その水素を前記第1貯蔵部(1
51 )に一旦吸蔵させ、次いでその吸蔵水素を放出して
得られた水素を前記第2貯蔵部(152 )に吸蔵させ、
前記機器(2)の要求水素量を前記改質器(3)により
充足することができない時、その要求水素量を充足すべ
く、前記第2貯蔵部(152 )より吸蔵水素を放出させ
ることを特徴とする、水素を燃料とする機器への水素供
給システム。1. A hydrogen supply system comprising a reformer (3) for generating hydrogen from a raw material such as alcohol or gasoline in order to supply hydrogen to a device (2) using hydrogen as a fuel. Absorbing the hydrogen produced by (3),
And a hydrogen storage (15) capable of being released,
The hydrogen storage (15) is provided with a first hydrogen storage material (M
A first storage portion with a H 1) and (15 1), second reservoir having a second hydrogen storage material of (MH 2) and (15 2), both the hydrogen absorption material (MH 1, MH 2 ), the first hydrogen storage material (MH 1 )
Are superior to the second hydrogen storage material (MH 2 ), while the second hydrogen storage material (MH 2 ) is superior to the second hydrogen storage material (MH 2 ) in terms of the ease of releasing the stored hydrogen. M
H 1 ), the hydrogen from the reformer (3) is subjected to a dehumidifying treatment, and then the hydrogen is stored in the first storage unit (1).
5 1 ), and the hydrogen obtained by releasing the stored hydrogen is stored in the second storage unit (15 2 ).
When the required amount of hydrogen of the equipment (2) cannot be satisfied by the reformer (3), releasing the stored hydrogen from the second storage unit (15 2 ) to satisfy the required amount of hydrogen. A hydrogen supply system for a device using hydrogen as a fuel.
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、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. Before introducing hydrogen released from the second storage section (15 2 ) into a fuel cell (2) as the device,
2. The hydrogen supply system for hydrogen-powered equipment according to claim 1, wherein the released hydrogen is subjected to a humidification treatment.
器(101 ,102)を備え、その調湿器(101 ,1
02 )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2記載の水素を燃料とする機器への水素供給
システム。Wherein comprising the dehumidifying processing and humidifying process is performed humidistat (10 1, 10 2), the humidistat (10 1, 1
0 2 ) The hydrogen supply system for a device using hydrogen as a fuel according to claim 2, wherein after the dehumidifying function is exhibited, the humidifying function can be exhibited, and after the humidifying function, the dehumidifying function can be exhibited.
え、それら調湿器(101 ,102 )は選択的に使用さ
れる、請求項2または3記載の水素を燃料とする機器へ
の水素供給システム。Wherein said humidistat (10 1, 10 2) 2 Taisonae, they humidistat (10 1, 10 2) are selectively used, the fuel of hydrogen according to claim 2 or 3, wherein Hydrogen supply system to equipment.
1 ,102 )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(1
01 ,102 )のうち含水量(Cw1,Cw2)の多い
方を使用する、請求項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 dehumidification process, both humidity controllers (10
1 and 10 2 ), the one having a smaller water content (Cw1, Cw2) is used, and both humidifiers (1
0 1, 10 2) using the one with a lot of water content (Cw1, Cw2) of the hydrogen supply system of hydrogen according to claim 4, wherein the device for the fuel.
給すべく、アルコール、ガソリン等の原料から水素を生
成する改質器(3)を備えた水素供給システムにおい
て、前記改質器(3)により生成された水素を吸蔵し、
且つ放出することが可能な水素貯蔵器(15)を有し、
その水素貯蔵器(15)は、第1の水素吸蔵材(M
H1 )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(MH1 )が前記第2の水素吸蔵材(MH
2 )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(MH2 )が前記第1の水素吸蔵材(M
H1 )に比べて水素放出の平衡圧が高く、前記改質器
(3)からの水素に除湿処理を施した後その水素を前記
第1貯蔵部(151 )に一旦吸蔵させ、次いでその吸蔵
水素を放出して得られた水素を前記第2貯蔵部(1
52 )に吸蔵させ、前記機器(2)の要求水素量を前記
改質器(3)により充足することができない時、その要
求水素量を充足すべく、前記第2貯蔵部(152 )より
吸蔵水素を放出させることを特徴とする、水素を燃料と
する機器への水素供給システム。6. A hydrogen supply system comprising a reformer (3) for generating hydrogen from a raw material such as alcohol or gasoline in order to supply hydrogen to a device (2) using hydrogen as a fuel. Absorbing the hydrogen produced by (3),
And a hydrogen storage (15) capable of being released,
The hydrogen storage (15) is provided with a first hydrogen storage material (M
A first storage portion with a H 1) and (15 1), second reservoir having a second hydrogen storage material of (MH 2) and (15 2), both the hydrogen absorption material (MH 1, MH 2 ), with respect to the hydrogen storage characteristics, the first
Of the second hydrogen storage material (MH 1 )
2 ), the equilibrium pressure of hydrogen storage is lower than that of the second hydrogen storage material (MH 2 ) at the same temperature and the same pressure.
Since the equilibrium pressure for releasing hydrogen is higher than that of H 1 ), the hydrogen from the reformer (3) is subjected to a dehumidifying treatment, and then the hydrogen is temporarily stored in the first storage unit (15 1 ). The hydrogen obtained by releasing the stored hydrogen is stored in the second storage unit (1).
5 2 ), and when the required hydrogen amount of the equipment (2) cannot be satisfied by the reformer (3), the second storage section (15 2 ) is used to satisfy the required hydrogen amount. A hydrogen supply system for a device using hydrogen as fuel, characterized by releasing more stored hydrogen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16494099A JP4229526B2 (en) | 1999-06-11 | 1999-06-11 | Hydrogen supply system for equipment using hydrogen as fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16494099A JP4229526B2 (en) | 1999-06-11 | 1999-06-11 | Hydrogen supply system for equipment using hydrogen as fuel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000351602A true JP2000351602A (en) | 2000-12-19 |
| JP4229526B2 JP4229526B2 (en) | 2009-02-25 |
Family
ID=15802749
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16494099A Expired - Fee Related JP4229526B2 (en) | 1999-06-11 | 1999-06-11 | Hydrogen supply system for equipment using hydrogen as fuel |
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| Country | Link |
|---|---|
| JP (1) | JP4229526B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004307328A (en) * | 2003-03-25 | 2004-11-04 | Sanyo Electric Co Ltd | Hydrogen production method, hydrogen production apparatus and motor having the same |
| US7147690B2 (en) * | 2003-04-30 | 2006-12-12 | Honda Motor Co., Ltd. | Method for replenishing hydrogen to compressed hydrogen tank and hydrogen replenishing device |
| FR2893187A1 (en) * | 2005-11-10 | 2007-05-11 | Air Liquide | ELECTRIC POWER CONSUMER INSTALLATION USING A FUEL CELL AND METHOD OF SUPPLYING SUCH A INSTALLATION |
-
1999
- 1999-06-11 JP JP16494099A patent/JP4229526B2/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004307328A (en) * | 2003-03-25 | 2004-11-04 | Sanyo Electric Co Ltd | Hydrogen production method, hydrogen production apparatus and motor having the same |
| US7147690B2 (en) * | 2003-04-30 | 2006-12-12 | Honda Motor Co., Ltd. | Method for replenishing hydrogen to compressed hydrogen tank and hydrogen replenishing device |
| FR2893187A1 (en) * | 2005-11-10 | 2007-05-11 | Air Liquide | ELECTRIC POWER CONSUMER INSTALLATION USING A FUEL CELL AND METHOD OF SUPPLYING SUCH A INSTALLATION |
| WO2007057585A3 (en) * | 2005-11-10 | 2007-08-02 | Air Liquide | Electrical power consuming installation using a fuel cell and method of supplying one such installation |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4229526B2 (en) | 2009-02-25 |
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