JP2883789B2 - Hydrogen fueled vehicles - Google Patents
Hydrogen fueled vehiclesInfo
- Publication number
- JP2883789B2 JP2883789B2 JP5196514A JP19651493A JP2883789B2 JP 2883789 B2 JP2883789 B2 JP 2883789B2 JP 5196514 A JP5196514 A JP 5196514A JP 19651493 A JP19651493 A JP 19651493A JP 2883789 B2 JP2883789 B2 JP 2883789B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- hydrogen
- valve
- hydrogen gas
- heating
- 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.)
- Expired - Fee Related
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/20—Fuel cells in motive systems, e.g. vehicle, ship, plane
-
- 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
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02T90/40—Application of hydrogen technology to transportation, e.g. using fuel cells
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Air-Conditioning For Vehicles (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Fuel Cell (AREA)
- Output Control And Ontrol Of Special Type Engine (AREA)
- Sorption Type Refrigeration Machines (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は水素を燃料として動力を
得る水素燃料自動車に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hydrogen-fueled vehicle which is powered by hydrogen.
【0002】[0002]
【従来の技術】従来構想されている水素燃料自動車を図
2のブロック図に示す。水素吸蔵タンク100から放出
された水素ガスは水素空気式の燃料電池101に送ら
れ、燃料電池101は走行用モータ102や冷房用圧縮
機103やその他の車両用電気負荷(図示せず)に給電
する。燃料電池101の排熱は、ポンプ104により循
環される温水により水素吸蔵タンク100に送られ、水
素放出時の吸熱熱量として消費される。2. Description of the Related Art A conventional hydrogen-fueled vehicle is shown in a block diagram of FIG. The hydrogen gas released from the hydrogen storage tank 100 is sent to a hydrogen-air fuel cell 101, which supplies power to a running motor 102, a cooling compressor 103, and other electric loads (not shown) for a vehicle. I do. The exhaust heat of the fuel cell 101 is sent to the hydrogen storage tank 100 by the hot water circulated by the pump 104, and is consumed as the amount of heat absorbed when releasing hydrogen.
【0003】圧縮機103は通常の車両用冷房装置と同
様にふっ化物ガスを冷媒とする通常の冷凍サイクル装置
として運転され、これにより蒸発器105で吸熱が、コ
ンデンサ106で放熱が行われる。[0003] The compressor 103 is operated as a normal refrigeration cycle apparatus using a fluoride gas as a refrigerant, similarly to a normal vehicle cooling apparatus, whereby heat is absorbed by the evaporator 105 and heat is released by the condenser 106.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、上記し
た装置では、以下の問題点が生じた。まず、水素吸蔵タ
ンク100の水素ガス発生量は燃料電池101から水素
吸蔵タンク100への輸送熱量に依存する一方、燃料電
池101の排熱量は発電量すなわち水素消費量に依存す
ることになるので、水素ガス発生量が燃料電池101の
温度状態に依存することになり、制御が容易でない。However, the above-described apparatus has the following problems. First, the amount of hydrogen gas generated in the hydrogen storage tank 100 depends on the amount of heat transferred from the fuel cell 101 to the hydrogen storage tank 100, while the amount of exhaust heat of the fuel cell 101 depends on the amount of power generation, that is, the amount of hydrogen consumed. The amount of hydrogen gas generated depends on the temperature state of the fuel cell 101, and the control is not easy.
【0005】例えば、車両走行開始時には、燃料電池1
01は発熱を開始しておらず、開始してもしばらくは燃
料電池101からでる温水温度が低く、水素吸蔵タンク
100は充分な水素ガスを放出できない。また、車両用
冷房装置として従来多用されているふっ化物ガスを冷媒
とする冷凍サイクル装置はフロンによる環境破壊の点で
その使用中止が強く期待されている。For example, when the vehicle starts running, the fuel cell 1
No. 01 has not started to generate heat, and even after the start, the temperature of the hot water from the fuel cell 101 is low for a while, and the hydrogen storage tank 100 cannot release sufficient hydrogen gas. In addition, it has been strongly expected that the refrigeration cycle apparatus using a fluoride gas as a refrigerant, which has been widely used as a vehicle cooling apparatus, is stopped in terms of environmental destruction due to chlorofluorocarbons.
【0006】本発明は上記問題点に鑑みなされたもので
あり、水素ガス発生量の制御性を向上できるとともに、
フロンを用いず構成が簡単な車両用冷房装置を実現可能
な水素燃料自動車を提供することを、その解決すべき技
術課題としている。[0006] The present invention has been made in view of the above problems, and can improve the controllability of the amount of hydrogen gas generated.
An object of the present invention is to provide a hydrogen-fueled vehicle capable of realizing a vehicle cooling device having a simple configuration without using Freon.
【0007】[0007]
【課題を解決するための手段】本発明の水素燃料自動車
は、熱交換器が付設されるとともに金属水素化物を収蔵
する3個以上の吸発熱槽と、水素ガスを圧縮する圧縮機
と、それぞれ弁を介して前記各吸発熱槽と前記圧縮機の
吸入口とを水素ガス移送可能に連結する吸入側移送管路
と、それぞれ弁を介して前記各吸発熱槽と前記圧縮機の
吐出口とを水素ガス移送可能に連結する吐出側移送管路
と、前記各弁を順次に開閉制御して前記各吸発熱槽と前
記両管路のどちらかとの連通を順次切替える制御手段
と、前記吐出側移送管路から弁を介して供給される加圧
水素ガスを燃料として動力を発生する動力源と、を備え
ることを特徴としている。The hydrogen-fueled vehicle according to the present invention is provided with a heat exchanger, three or more heat-absorption tanks for storing metal hydrides, and a compressor for compressing hydrogen gas. A suction-side transfer pipe connecting the respective heat-absorbing / heating tanks and a suction port of the compressor via a valve so that hydrogen gas can be transferred; and each of the heat-absorbing / heating tanks and a discharge port of the compressor via a valve. A discharge-side transfer pipe connecting hydrogen gas to be able to transfer hydrogen gas; control means for sequentially opening and closing the valves to sequentially switch communication between each of the heat-absorbing / heating tanks and one of the two pipes; And a power source for generating power using pressurized hydrogen gas supplied from a transfer pipe via a valve as fuel.
【0008】動力源として、水素燃料電池や水素エンジ
ンを採用することができる。As a power source, a hydrogen fuel cell or a hydrogen engine can be employed.
【0009】[0009]
【作用】冷房運転時において、圧縮機が駆動され、圧縮
機は吸入側移送管路から吐出側移送管路へ水素ガスを圧
送する。一部の吸発熱槽は弁を通じて吸入側移送管路へ
水素ガスを放出し、この時生じる冷熱は熱交換器を通じ
て外部に輸送されて空調に供される。他の一部の吸発熱
槽は弁を通じて吐出側移送管路から水素ガスを吸蔵し、
この時生じる発熱は熱交換器を通じて外部に輸送され
る。In the cooling operation, the compressor is driven, and the compressor pumps hydrogen gas from the suction-side transfer pipe to the discharge-side transfer pipe. Some of the heat absorbing / heating tanks release hydrogen gas to a suction side transfer pipe through a valve, and the cold generated at this time is transported to the outside through a heat exchanger for air conditioning. Some other heat-absorbing and heat-absorbing tanks absorb hydrogen gas from the discharge-side transfer pipe through valves,
The heat generated at this time is transported outside through the heat exchanger.
【0010】制御手段は、各吸発熱槽を吸入側移送管路
及び吐出側移送管路に順次切り換える。動力源は、吐出
側移送管路から供給される水素ガスを燃料として動力を
発生する。冷房運転停止時の一例において、圧縮機が駆
動されて動力源へ水素ガスが供給される一方、水素ガス
を放出する吸発熱槽には外気又は動力源から熱が供給さ
れる。[0010] The control means sequentially switches each heat absorbing / heating tank to a suction side transfer pipeline and a discharge side transfer pipeline. The power source generates power using hydrogen gas supplied from the discharge-side transfer pipe as fuel. In an example when the cooling operation is stopped, the compressor is driven to supply hydrogen gas to the motive power source, while heat is supplied from the outside air or the motive power source to the heat absorbing and discharging tank that discharges the hydrogen gas.
【0011】冷房運転停止時の一例において、圧縮機も
停止され、動力源へ加圧水素ガスを供給する吸発熱槽に
は動力源から熱が供給される。In an example when the cooling operation is stopped, the compressor is also stopped, and heat is supplied from the power source to the heat absorbing / heating tank that supplies pressurized hydrogen gas to the power source.
【0012】[0012]
【発明の効果】以上説明したように本発明の水素燃料自
動車では、動力源が圧縮機加圧型水素吸蔵放出式空調装
置の吐出側移送管路から加圧水素ガスを供給される構成
を採用しているので、吸発熱槽からの水素ガス放出量が
燃料電池の排熱に依存する従来方式と比べて、以下の効
果を奏する。As described above, the hydrogen-fueled vehicle of the present invention employs a configuration in which the power source is supplied with pressurized hydrogen gas from the discharge-side transfer pipe of the compressor pressurized hydrogen storage / release type air conditioner. Therefore, the following effects are achieved as compared with the conventional method in which the amount of hydrogen gas released from the heat absorbing / heating tank depends on the exhaust heat of the fuel cell.
【0013】第一に、圧縮機により吸発熱槽から水素ガ
スを吸引するので、動力源の排熱温度による水素ガス放
出量の変動を抑止でき、更に、吸発熱槽の温度が低くて
も充分な量の水素ガスを放出することができ、動力源に
供給する水素ガス流量の安定制御を実現することができ
る。例えば、走行開始時において動力源として採用した
燃料電池が低温の場合においても、圧縮機駆動により充
分な水素ガス供給が実現できる。First, since the hydrogen gas is sucked from the heat absorbing / heating tank by the compressor, the fluctuation of the amount of hydrogen gas released due to the exhaust heat temperature of the power source can be suppressed, and even if the temperature of the heat absorbing / heating tank is low, it is sufficient. An appropriate amount of hydrogen gas can be released, and stable control of the flow rate of hydrogen gas supplied to the power source can be realized. For example, even when the fuel cell used as a power source at the start of traveling is at a low temperature, a sufficient supply of hydrogen gas can be realized by driving the compressor.
【0014】第二に、燃料供給圧縮機で、冷房装置など
の車両空調装置の圧縮機を共用することができる。第三
に、車両用空調装置としてふっ素化合物ガスを採用しな
いので、環境悪化を防止できる。第四に3個以上の吸発
熱槽を有するので燃料電池や水素エンジンの水素消費量
に関わらず吸発熱槽は安定して水素を放出することがで
き、冷房出力が安定化できる。Second, a compressor of a vehicle air conditioner such as a cooling device can be shared with a fuel supply compressor. Third, since a fluorine compound gas is not used as a vehicle air conditioner, environmental degradation can be prevented. Fourth, since there are three or more heat absorbing / heating tanks, the heat absorbing / heating tanks can stably release hydrogen regardless of the hydrogen consumption of the fuel cell or the hydrogen engine, and the cooling output can be stabilized.
【0015】[0015]
【実施例】本発明の装置の一実施例を図1に示すブロッ
ク図を参照して説明する。1は走行用のモータであり、
燃料電池(本発明でいう動力源)2の出力端から電源ラ
インLを通じて給電されている。燃料電池2の内部は多
数のセルが直列接続されて所要電圧が出力可能となって
いる。電源ラインLは補助バッテリ3の高位端及びモー
タM1、M2に接続されており、モータM1は空気圧縮
機4を駆動し、モータM2は水素ガス圧縮用の圧縮機7
を駆動する。空気圧縮機4は外気を所要圧力(数気圧)
に加圧して燃料電池2の酸素室(図示せず)に供給す
る。この酸素室中にて酸素含有率が減少した空気は所定
の流量調整手段(図示せず)を通じて外気に排出され
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the apparatus of the present invention will be described with reference to the block diagram shown in FIG. 1 is a running motor,
Power is supplied from an output terminal of a fuel cell (power source in the present invention) 2 through a power supply line L. A large number of cells are connected in series inside the fuel cell 2 so that a required voltage can be output. The power line L is connected to the high end of the auxiliary battery 3 and the motors M1 and M2. The motor M1 drives the air compressor 4, and the motor M2 is a compressor 7 for compressing hydrogen gas.
Drive. The air compressor 4 pressurizes the outside air to the required pressure (several atmospheric pressure)
And supplied to an oxygen chamber (not shown) of the fuel cell 2. The air having a reduced oxygen content in the oxygen chamber is discharged to the outside air through a predetermined flow rate adjusting means (not shown).
【0016】5は水素ガス輸送用の吸入側移送管路であ
り、6は水素ガス輸送用の吐出側移送管路であり、7は
吸入側移送管路5から吸入した水素ガスを約10気圧に
加圧して吐出側移送管路6に吐出する圧縮機である。4
0は流量調整弁又は圧力調整弁であり、その開度に応じ
て吐出側移送管路6から燃料電池2の水素室(図示せ
ず)に必要電力に応じた水素ガス流量が所要圧力(数気
圧)に減圧されて供給される。Reference numeral 5 denotes a suction-side transfer line for transporting hydrogen gas, 6 denotes a discharge-side transfer line for transporting hydrogen gas, and 7 denotes hydrogen gas sucked from the suction-side transfer line 5 at about 10 atm. And discharges it to the discharge-side transfer pipeline 6. 4
Numeral 0 denotes a flow rate control valve or a pressure control valve, and a hydrogen gas flow rate corresponding to a required electric power from the discharge side transfer pipe line 6 to a hydrogen chamber (not shown) of the fuel cell 2 according to the opening degree corresponds to a required pressure (number). (Atmospheric pressure).
【0017】8aは水素ガスを各吸発熱槽11〜18に
個別に導入制御する電磁開閉弁(本発明でいう弁)であ
り、各吸発熱槽11〜18毎に付設されている。そし
て、吐出側移送管路6の水素ガスは弁8a及び弁8aと
直列接続された逆止弁を通じて各吸発熱槽11〜18に
導入される。各吸発熱槽11〜18にはLaNi5 ・M
mNi5 (Mmはミツシュメタル)、FeTiなどの金
属水素化物が収蔵されている。これらの金属水素化物
は、脱水素化反応により吸熱し、水素化反応により発熱
するものとして周知である。弁8bは各吸発熱槽11〜
18から放出された水素ガスを吸入側移送管路5に個別
に導出制御する電磁開閉弁(本発明でいう弁)であり、
各吸発熱槽11〜18毎に付設されている。そして、各
吸発熱槽11〜18は弁8bを通じて吸入側移送管路5
に水素を放出する。Numeral 8a denotes an electromagnetic opening / closing valve (a valve in the present invention) for individually controlling the introduction and control of hydrogen gas into each of the heat absorbing / heating tanks 11 to 18, and is provided for each of the heat absorbing / heating tanks 11 to 18. Then, the hydrogen gas in the discharge-side transfer pipe 6 is introduced into each of the heat absorbing / heating tanks 11 to 18 through the valve 8a and a check valve connected in series with the valve 8a. Each endothermic and exothermic heat tank 11~18 LaNi 5 · M
Metal hydrides such as mNi 5 (Mm is a Mitsumi metal) and FeTi are stored. These metal hydrides are well known to absorb heat by a dehydrogenation reaction and generate heat by a hydrogenation reaction. The valve 8b is connected to each of the heat absorbing / heating tanks 11 to
An electromagnetic on-off valve (a valve in the present invention) for individually controlling the outflow of the hydrogen gas released from 18 to the suction-side transfer pipe line 5;
It is provided for each of the heat absorbing / heating tanks 11 to 18. Then, each of the heat absorbing / heating tanks 11 to 18 is connected to the suction side transfer pipe 5 through the valve 8b.
Releases hydrogen.
【0018】また、空調のために、冷却水ポンプP1と
冷水(又はブライン)ポンプP2とが配設されており、
冷却水ポンプP1は冷却水管路91から吸入した冷却水
をラジエータ92に送り、ラジエータ92で冷却された
冷却水は冷却水管路93に送られる。冷水ポンプP2は
冷水管路94から吸入した冷水を電磁三方弁95、蓄熱
槽96、電磁三方弁97を通じて冷却用空調器98に送
り、空調器98で加温された冷水は冷却水管路99に送
られる。A cooling water pump P1 and a cooling water (or brine) pump P2 are provided for air conditioning.
The cooling water pump P1 sends the cooling water sucked from the cooling water pipe 91 to the radiator 92, and the cooling water cooled by the radiator 92 is sent to the cooling water pipe 93. The chilled water pump P2 sends the chilled water sucked from the chilled water pipe 94 to the cooling air conditioner 98 through the electromagnetic three-way valve 95, the heat storage tank 96, and the electromagnetic three-way valve 97, and the chilled water heated by the air conditioner 98 is sent to the cooling water pipe 99. Sent.
【0019】9aは電磁三方弁であって、各吸発熱槽1
1〜18毎に付設されており、各電磁三方弁9aは管路
93、99の一方と各吸発熱槽11〜18に内蔵された
熱交換器11a〜18aの流入口とを接続する。9bも
電磁三方弁であって、各吸発熱槽11〜18毎に付設さ
れており、各電磁三方弁9bは管路91、94の一方と
各吸発熱槽11〜18に内蔵された熱交換器11a〜1
8aの流出口とを接続する。Reference numeral 9a denotes an electromagnetic three-way valve,
Each electromagnetic three-way valve 9a connects one of the pipes 93 and 99 to the inlet of the heat exchangers 11a to 18a incorporated in each of the heat absorbing and heating tanks 11 to 18. Reference numeral 9b denotes an electromagnetic three-way valve, which is provided for each of the heat absorbing / heating tanks 11 to 18. Each electromagnetic three-way valve 9b has a heat exchange built in one of the pipes 91 and 94 and each of the heat absorbing / heating tanks 11 to 18. Vessels 11a-1
8a is connected to the outlet.
【0020】2aは燃料電池2に内蔵された熱交換器で
あって、電磁三方弁9cを通じて管路93、99に接続
され、電磁三方弁9dを通じて管路91、94に接続さ
れている。コントローラ(本発明でいう制御手段)10
はマイコンを内蔵しており、走行モータ1、圧縮機7、
ポンプP1、P2などの回転機器の駆動制御、弁40の
開度制御、各弁8a、8b、9a、9b、9c,9dの
開閉制御を行う。Reference numeral 2a denotes a heat exchanger built in the fuel cell 2, which is connected to lines 93 and 99 through an electromagnetic three-way valve 9c and connected to lines 91 and 94 through an electromagnetic three-way valve 9d. Controller (control means in the present invention) 10
Has a built-in microcomputer, running motor 1, compressor 7,
Drive control of rotating devices such as the pumps P1 and P2, opening control of the valve 40, and opening / closing control of the valves 8a, 8b, 9a, 9b, 9c, 9d are performed.
【0021】以下、上記した空調−走行駆動系の各種動
作モードを以下に説明する。 (冷房−発電モード)ただし説明を簡単にするために、
コントローラ10は、定期的に弁8a〜9dを開閉する
ものとし、圧縮機4、7、ポンプP1、P2は所望回転
数で駆動されているものとする。Hereinafter, various operation modes of the air-conditioning-traveling drive system will be described. (Cooling-power generation mode) However, to simplify the explanation,
The controller 10 opens and closes the valves 8a to 9d periodically, and it is assumed that the compressors 4, 7 and the pumps P1, P2 are driven at a desired rotation speed.
【0022】まず、冷房動作を説明する。ここでは、吸
発熱槽11は水素吸蔵槽として作動し、吸発熱槽12が
水素放出槽として作動するものとする。吸発熱槽11に
付設の弁8aと吸発熱槽12に付設の弁8bが開弁さ
れ、他の各弁8a、8bは閉弁される。そして、吸発熱
槽12に付設の弁9a、9bは熱交換器12aと冷水管
路94、99とを連通し、残りの各弁9a、9bは他の
熱交換器11a、13a〜18aと冷却水管路91、9
3とを連通する。First, the cooling operation will be described. Here, it is assumed that the heat absorbing / heating tank 11 operates as a hydrogen storage tank, and the heat absorbing / heating tank 12 operates as a hydrogen releasing tank. The valve 8a attached to the heat absorbing / heating tank 11 and the valve 8b attached to the heat absorbing / heating tank 12 are opened, and the other valves 8a, 8b are closed. The valves 9a and 9b attached to the heat absorbing and heating tank 12 communicate the heat exchanger 12a and the cold water pipes 94 and 99, and the remaining valves 9a and 9b cool the other heat exchangers 11a and 13a to 18a. Water pipeline 91, 9
And 3 is communicated.
【0023】このようにすれば、吸発熱槽12から吸入
側移送管路5へ水素ガスが放出され、圧縮機7はそれを
加圧して吐出側移送管路6に吐出し、吐出側移送管路6
の水素ガスは吸発熱槽11に吸蔵される。吸発熱槽12
の冷熱はポンプP2により蓄熱槽96を通じて空調器9
8に送られて車室空気を冷却し、吸発熱槽11の発熱は
ポンプP1によりラジエータ92に送られて外気に放出
される。In this way, hydrogen gas is released from the heat absorbing / heating tank 12 to the suction side transfer line 5, and the compressor 7 pressurizes it and discharges it to the discharge side transfer line 6. Road 6
Hydrogen gas is stored in the heat absorbing / heating tank 11. Heat absorbing / heating tank 12
Of the air conditioner 9 through the heat storage tank 96 by the pump P2.
The heat generated in the heat absorbing / heating tank 11 is sent to the radiator 92 by the pump P1 and released to the outside air.
【0024】次に、発電動作について説明する。弁40
は高圧(約10気圧)の吐出側移送管路6から抽気し、
所望気圧まで減圧して燃料電池2に供給する。燃料電池
2は供給された水素ガス及び酸素ガスの電池反応により
発電した電力を走行モータ1に給電し、残余の電力を各
種車両用電気負荷及び補助バッテリ3に給電する。な
お、燃料電池2の負荷変動に伴う発電電力の制御は主と
して弁40の開度調節にて行う。また、熱交換器2aは
電磁三方弁9c,9dを通じて管路91、93に連通
し、燃料電池2の発熱熱量はラジエータ92に放熱され
る。Next, the power generation operation will be described. Valve 40
Is extracted from the high pressure (about 10 atm) discharge side transfer line 6,
The pressure is reduced to a desired pressure and supplied to the fuel cell 2. The fuel cell 2 supplies electric power generated by a cell reaction of the supplied hydrogen gas and oxygen gas to the traveling motor 1, and supplies the remaining electric power to various vehicle electric loads and the auxiliary battery 3. The control of the power generated by the load fluctuation of the fuel cell 2 is mainly performed by adjusting the opening of the valve 40. The heat exchanger 2 a communicates with the pipes 91 and 93 through the electromagnetic three-way valves 9 c and 9 d, and the heat generated by the fuel cell 2 is radiated to the radiator 92.
【0025】次に、吸発熱槽12が空になった場合、吸
発熱槽12に付設の弁8bが閉弁され、吸発熱槽13に
付設の弁8bが開弁される。また、吸発熱槽13付設の
弁9a、9bが熱交換器13aと冷水管路94、99と
を連通し、残りの各弁9a、9bは他の熱交換器11
a、12a、14a〜18aと冷却水管路91、93と
を連通する。これにより、吸発熱槽13が水素放出槽と
して作動する。なお、上記の空になったことの検出は槽
内温度又は圧力又は管路温度又は圧力又は水素ガス流量
の検出により実施できる。Next, when the heat absorbing / heating tank 12 becomes empty, the valve 8b attached to the heat absorbing / heating tank 12 is closed, and the valve 8b attached to the heat absorbing / heating tank 13 is opened. Further, valves 9a and 9b attached to the heat absorbing and heating tank 13 communicate the heat exchanger 13a with the cold water pipes 94 and 99, and the remaining valves 9a and 9b are connected to the other heat exchangers 11 and 9, respectively.
a, 12a, 14a to 18a and the cooling water pipes 91, 93 are communicated. As a result, the heat absorbing / heating tank 13 operates as a hydrogen releasing tank. The detection of the empty state can be performed by detecting the temperature or pressure in the tank, the pipe temperature or pressure, or the flow rate of hydrogen gas.
【0026】次に、吸発熱槽11へ水素ガスが満充填さ
れた場合、吸発熱槽11に付設の弁8aが閉弁され、吸
発熱槽12に付設の弁8aが開弁される。これにより、
吸発熱槽12が水素吸蔵槽として作動する。なお、上記
の満充填の検出は槽内温度又は圧力又は管路温度又は圧
力又は水素ガス流量の検出により実施できる。次に、吸
発熱槽12へ水素ガスが満充填された場合や、吸発熱槽
13が空になった場合にも、上記と同様の手順で吸発熱
槽13が水素吸蔵槽として作動し、吸発熱槽14が水素
放出槽として作動する。以下、順次、各吸発熱槽11〜
18が順次水素吸蔵、水素放出を順次実施して冷熱発生
を行う。Next, when the heat absorbing / heating tank 11 is fully filled with hydrogen gas, the valve 8a attached to the heat absorbing / heating tank 11 is closed, and the valve 8a attached to the heat absorbing / heating tank 12 is opened. This allows
The heat absorbing / heating tank 12 operates as a hydrogen storage tank. The detection of the full filling can be performed by detecting the temperature or pressure in the tank, the temperature or pressure of the pipeline, or the flow rate of hydrogen gas. Next, even when the heat absorbing and heating tank 12 is fully filled with hydrogen gas and when the heat absorbing and heating tank 13 is emptied, the heat absorbing and heating tank 13 operates as a hydrogen storage tank in the same procedure as described above. The heating tank 14 operates as a hydrogen releasing tank. Hereinafter, each of the heat absorbing / heating tanks 11 to 11 will be sequentially described.
18 sequentially performs hydrogen storage and hydrogen release to generate cold heat.
【0027】なお、蓄熱槽96は吸発熱槽11〜18に
よる冷熱発生量と空調器98の冷熱要求量との一時的な
不均衡を改善するために設けたものであるが、省略も可
能である。また、余剰冷熱の貯蔵又は不足冷熱の発生が
不要な場合は、電磁三方弁95、97の切替えにより蓄
熱槽96を迂回して冷水を循環してもよい。 (冷暖房−非発電モード)次に、例えば走行モータ1の
停止時など、燃料電池2の発電停止時には、弁40を閉
とし、圧縮機4を停止すればよい。The heat storage tank 96 is provided to improve the temporary imbalance between the amount of cold generated by the heat absorbing and heating tanks 11 to 18 and the required amount of cold from the air conditioner 98, but can be omitted. is there. When it is not necessary to store excess cold energy or generate insufficient cold energy, the cooling water may be circulated around the heat storage tank 96 by switching the electromagnetic three-way valves 95 and 97. (Cooling / heating-non-power generation mode) Next, when the power generation of the fuel cell 2 is stopped, for example, when the traveling motor 1 is stopped, the valve 40 may be closed and the compressor 4 may be stopped.
【0028】(冷暖房停止−発電モードの一例)次に、
冷暖房停止時における発電動作の一例について説明す
る。この場合には、原則的にはポンプP1,P2は停止
され、各吸発熱槽11〜18の内、空でない槽から放出
された水素ガスが圧縮機7、吐出側移送管路6及び弁4
0を通じて燃料電池2に送られる。(Example of cooling / heating stop-power generation mode)
An example of the power generation operation at the time of cooling / heating stop will be described. In this case, in principle, the pumps P1 and P2 are stopped, and the hydrogen gas discharged from the non-empty tank among the heat absorbing / heating tanks 11 to 18 is supplied to the compressor 7, the discharge side transfer line 6, and the valve 4
0 to the fuel cell 2.
【0029】このモードは燃料電池2が冷却状態の場合
などに好適である。 (冷暖房停止−発電モードの他例)次に、冷暖房停止時
における発電動作の他例について説明する。この場合に
は、ポンプP1を運転し、ポンプP2及び圧縮機7を停
止する。吸発熱槽11〜18のどれかから吐出側移送管
路6側に放出された水素ガスは弁40を通じて燃料電池
2に供給される。燃料電池2で生じた発熱は熱交換器2
aを通じてラジエータ92に循環される。この時、水素
ガスを放出している上記吸発熱槽に内蔵の熱交換器は弁
9a、9bの切替により管路91、93に接続され、こ
れにより熱交換器2aで受熱した熱量の一部は上記水素
放出槽に供給される。なお、この場合、ラジエータ92
にもバイパス管路を追加し、このバイパス管路の流量を
制御することにより、熱交換器2aで受熱した熱量をラ
ジエータ92で放熱せず、なるべく上記水素放出槽に供
給することが好ましい。This mode is suitable when the fuel cell 2 is in a cooling state. Next, another example of the power generation operation when the cooling / heating is stopped will be described. In this case, the pump P1 is operated, and the pump P2 and the compressor 7 are stopped. The hydrogen gas discharged from any of the heat absorbing / heating tanks 11 to 18 toward the discharge side transfer pipe 6 is supplied to the fuel cell 2 through the valve 40. The heat generated in the fuel cell 2 is
A is circulated to the radiator 92 through a. At this time, the heat exchanger built in the heat-absorbing / heating tank which is releasing hydrogen gas is connected to the pipelines 91 and 93 by switching the valves 9a and 9b, thereby a part of the heat received by the heat exchanger 2a. Is supplied to the hydrogen release tank. In this case, the radiator 92
It is preferable to add a bypass pipe to the apparatus and control the flow rate of the bypass pipe so that the heat received by the heat exchanger 2a is not radiated by the radiator 92 but is supplied to the hydrogen release tank as much as possible.
【0030】(暖房−発電モードの一例)この場合に
は、上記した冷暖房停止−発電モードの他例と同じく、
電磁三方弁9c,9dを冷水管路93、94側に切り換
える。そして、ポンプP1を停止し、ポンプP2を運転
する。このようにすれば、熱交換器2の受熱量を空調器
98及び水素放出槽に供給することができる。(Example of heating / power generation mode) In this case, as in the other examples of the cooling / heating stop / power generation mode described above,
The electromagnetic three-way valves 9c and 9d are switched to the cold water pipes 93 and 94. Then, the pump P1 is stopped, and the pump P2 is operated. In this way, the amount of heat received by the heat exchanger 2 can be supplied to the air conditioner 98 and the hydrogen discharge tank.
【0031】(暖房−発電モードの他例)この場合に
は、上記した冷暖房停止−発電モードの一例と同じく、
各電磁三方弁9a,9b,9c,9dの切替制御によ
り、熱交換器2の受熱量を空調器98及び水素放出槽に
供給するとともに、水素吸蔵槽の発熱熱量も空調器に供
給する。ただこの場合、ポンプP1を運転するとともに
水素放出槽付設の弁9a,9bを管路91、93側に切
り換えて、水素放出槽の必要吸熱量をラジエータ92を
通じて外気から吸熱できるようにする。なお、燃料電池
2及び水素吸蔵槽の発生熱量が余剰の場合はそれを利用
することもできる。(Other example of heating / power generation mode) In this case, as in the above-described example of the cooling / heating stop-power generation mode,
By controlling the switching of each of the electromagnetic three-way valves 9a, 9b, 9c, 9d, the amount of heat received by the heat exchanger 2 is supplied to the air conditioner 98 and the hydrogen discharge tank, and the amount of heat generated by the hydrogen storage tank is also supplied to the air conditioner. In this case, however, the pump P1 is operated and the valves 9a and 9b provided with the hydrogen release tank are switched to the pipe lines 91 and 93 so that the required heat absorption of the hydrogen discharge tank can be absorbed from the outside air through the radiator 92. If the amount of heat generated by the fuel cell 2 and the hydrogen storage tank is excessive, it can be used.
【0032】(暖房−発電停止モード)この場合には、
圧縮機7、ポンプP1、P2が運転され、各吸発熱槽1
1〜18が水素吸蔵槽、水素放出槽として上記と同様に
順次切替え制御される。そして、水素放出槽の吸熱熱量
はラジエータ92から供給され、水素吸蔵槽の発生熱量
は空調器98に供給される。(Heating-power generation stop mode) In this case,
The compressor 7, the pumps P1 and P2 are operated, and the heat absorbing /
1 to 18 are sequentially switched and controlled as a hydrogen storage tank and a hydrogen release tank in the same manner as described above. The amount of heat absorbed by the hydrogen release tank is supplied from the radiator 92, and the amount of heat generated by the hydrogen storage tank is supplied to the air conditioner 98.
【0033】以上説明したように本発明の水素燃料自動
車では、共通の装置構成で冷暖房システムと燃料電池発
電システムとを実現しているので、それらを別個に構成
した場合に比べて装置構成が簡単となり、しかも燃料電
池2への水素ガス供給量を安定制御することができ、ふ
っ素化合物ガスの使用を回避することもできる。As described above, in the hydrogen-fueled vehicle of the present invention, since the cooling and heating system and the fuel cell power generation system are realized with a common device configuration, the device configuration is simpler than when they are separately configured. In addition, the amount of hydrogen gas supplied to the fuel cell 2 can be stably controlled, and the use of a fluorine compound gas can be avoided.
【図1】本発明の装置の一実施例を示すブロック図であ
る。FIG. 1 is a block diagram showing one embodiment of the apparatus of the present invention.
【図2】従来の装置を示すブロック図である。FIG. 2 is a block diagram showing a conventional device.
2は燃料電池(本発明でいう動力源)、5は吸入側移送
管路、6は吐出側移送管路、7は圧縮機、8a、8bは
電磁開閉弁(本発明でいう弁)、9a,9bは電磁三方
弁、10はコントローラ(本発明でいう制御手段)、1
1〜18は吸発熱槽。2 is a fuel cell (power source in the present invention), 5 is a transfer pipe on the suction side, 6 is a transfer pipe on the discharge side, 7 is a compressor, 8a and 8b are solenoid on-off valves (valves in the present invention), 9a , 9b are electromagnetic three-way valves, 10 is a controller (control means in the present invention), 1
Numerals 1 to 18 are heat absorbing and heating tanks.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI H01M 8/06 H01M 8/06 R (72)発明者 三浦 正芳 愛知県刈谷市豊田町2丁目1番地 株式 会社豊田自動織機製作所内 (72)発明者 藤田 信雄 愛知県豊田市トヨタ町1番地 トヨタ自 動車株式会社内 (72)発明者 青木 博史 愛知県愛知郡長久手町大字長湫字横道41 番地の1 株式会社豊田中央研究所内 (72)発明者 三井 宏之 愛知県愛知郡長久手町大字長湫字横道41 番地の1 株式会社豊田中央研究所内 (58)調査した分野(Int.Cl.6,DB名) F02B 43/10 F02M 21/02 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification symbol FI H01M 8/06 H01M 8/06 R (72) Inventor Masayoshi Miura 2-1-1 Toyota-cho, Kariya-shi, Aichi Prefecture Toyota Industries Corporation (72) Inventor Nobuo Fujita 1 Toyota Town, Toyota City, Aichi Prefecture Inside Toyota Motor Co., Ltd. (72) Inventor Hiroshi Aoki 41 No. 41, Chukumi Yokomichi, Nagakute-cho, Aichi County, Aichi Prefecture 1 Toyota Central Research Institute, Inc. 72) Inventor Hiroyuki Mitsui 41 Toyoda Central Research Laboratories Co., Ltd., 41-cho, Yokomichi, Nagakute-cho, Aichi-gun, Aichi Prefecture (58) Field surveyed (Int. Cl. 6 , DB name) F02B 43/10 F02M 21/02
Claims (1)
物を収蔵する3個以上の吸発熱槽と、 水素ガスを圧縮する圧縮機と、 それぞれ弁を介して前記各吸発熱槽と前記圧縮機の吸入
口とを水素ガス移送可能に連結する吸入側移送管路と、 それぞれ弁を介して前記各吸発熱槽と前記圧縮機の吐出
口とを水素ガス移送可能に連結する吐出側移送管路と、 前記各弁を順次に開閉制御して前記各吸発熱槽と前記両
管路のどちらかとの連通を順次切替える制御手段と、 前記吐出側移送管路から弁を介して供給される加圧水素
ガスを燃料として動力を発生する動力源と、 を備えることを特徴とする水素燃料自動車。A heat exchanger is provided and three or more heat absorbing / heating tanks for storing metal hydrides, a compressor for compressing hydrogen gas, and each of said heat absorbing / heating tanks via a valve. A suction-side transfer pipe connecting the suction port of the compressor so as to transfer hydrogen gas, and a discharge-side transfer pipe connecting each of the heat-absorbing / heating tanks and the discharge port of the compressor via a valve so as to transfer hydrogen gas. Control means for sequentially controlling the opening and closing of each valve so as to sequentially switch the communication between each of the heat absorbing and heating tanks and one of the two pipe lines; and pressurized water supplied from the discharge side transfer pipe line via a valve. A hydrogen-fueled vehicle comprising: a power source that generates power using raw gas as fuel.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5196514A JP2883789B2 (en) | 1993-08-06 | 1993-08-06 | Hydrogen fueled vehicles |
| US08/286,191 US5678410A (en) | 1993-08-06 | 1994-08-05 | Combined system of fuel cell and air-conditioning apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5196514A JP2883789B2 (en) | 1993-08-06 | 1993-08-06 | Hydrogen fueled vehicles |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0749037A JPH0749037A (en) | 1995-02-21 |
| JP2883789B2 true JP2883789B2 (en) | 1999-04-19 |
Family
ID=16359016
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5196514A Expired - Fee Related JP2883789B2 (en) | 1993-08-06 | 1993-08-06 | Hydrogen fueled vehicles |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2883789B2 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4213267B2 (en) | 1998-09-25 | 2009-01-21 | 株式会社豊田自動織機 | Hydrogen storage tank device |
| AT407316B (en) * | 1999-03-23 | 2001-02-26 | Vaillant Gmbh | Compressor control for a fuel cell arrangement |
| JP3220438B2 (en) * | 1999-05-14 | 2001-10-22 | 株式会社日立製作所 | Fuel cell power generation system |
| KR100644263B1 (en) * | 2000-11-16 | 2006-11-10 | 한라공조주식회사 | Air-conditioning device for electric vehicle for hydrogen battery |
| KR100689335B1 (en) * | 2000-12-29 | 2007-03-08 | 주식회사 엘지이아이 | Heating and cooling system using fuel cell |
| CN114962993A (en) * | 2022-01-19 | 2022-08-30 | 北京未来氢能科技有限公司 | Hydrogen storage fuel cell air conditioning system and hydrogenation equipment |
-
1993
- 1993-08-06 JP JP5196514A patent/JP2883789B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0749037A (en) | 1995-02-21 |
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