JP2008254986A - Activation device and method for hydrogen storage alloy vessel - Google Patents
Activation device and method for hydrogen storage alloy vessel Download PDFInfo
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- 239000001257 hydrogen Substances 0.000 title claims abstract description 117
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 117
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 114
- 229910045601 alloy Inorganic materials 0.000 title claims abstract description 72
- 239000000956 alloy Substances 0.000 title claims abstract description 72
- 238000003860 storage Methods 0.000 title claims abstract description 57
- 230000004913 activation Effects 0.000 title claims abstract description 47
- 238000000034 method Methods 0.000 title abstract description 36
- 239000012530 fluid Substances 0.000 claims abstract description 36
- 150000002431 hydrogen Chemical class 0.000 claims abstract description 8
- 230000003213 activating effect Effects 0.000 claims description 12
- 230000001629 suppression Effects 0.000 abstract description 2
- 238000001994 activation Methods 0.000 description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000010521 absorption reaction Methods 0.000 description 6
- 238000007796 conventional method Methods 0.000 description 6
- 238000001816 cooling Methods 0.000 description 4
- 239000004033 plastic Substances 0.000 description 4
- 229920003023 plastic Polymers 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 230000006837 decompression Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000004904 shortening Methods 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 230000002528 anti-freeze Effects 0.000 description 1
- 238000009694 cold isostatic pressing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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- 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
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Abstract
Description
本発明は、水素吸蔵合金容器の活性化装置及び方法に関し、特に、水素吸蔵合金容器内部にかけられる水素圧力とほぼ同等の流体圧力を外部にかけることにより、水素吸蔵合金容器の変形の抑制と効率的な熱交換を両立させ、活性化時間の短縮を実現するための新規な改良に関する。 The present invention relates to an apparatus and method for activating a hydrogen storage alloy container, and in particular, by applying a fluid pressure substantially equal to the hydrogen pressure applied to the inside of the hydrogen storage alloy container to the outside, the deformation and efficiency of the hydrogen storage alloy container are suppressed. The present invention relates to a novel improvement for achieving both heat exchange and shortening the activation time.
従来、用いられていた水素吸蔵合金の活性化方法としては、例えば、粉末状の水素吸蔵合金を水素導入管を設けた密閉容器内に入れ、80℃以上の温度で数時間〜数十時間真空引きをした後、室温以下の温度で数気圧以上の水素を導入する方法が一般的である。ここで、前半部分の高温での真空引きを「減圧活性化」、後半部分の低温での高圧水素導入を「加圧活性化」と呼ぶ。BCC系水素吸蔵合金のような活性化しにくい水素吸蔵合金では、AB5系やAB2系の活性化しやすい合金に比べ、減圧活性化条件の高温化及び高真空化とともに、加圧活性化条件の低温化および高圧化が必要である。また、これらの活性化条件を強めるほど、一般的に活性化にかかる時間は短くなる。すなわち、減圧活性化工程では100℃よりも150℃の方が、加圧活性化工程では20℃よりも0℃、或いは1MPaよりも10MPaで行った方が活性化完了までの時間は短くなる。 Conventionally, as a method for activating a hydrogen storage alloy that has been used, for example, a powdered hydrogen storage alloy is placed in a sealed container provided with a hydrogen introduction tube, and is vacuumed at a temperature of 80 ° C. or more for several hours to several tens of hours. After pulling, a method of introducing hydrogen at several atmospheres or more at a temperature below room temperature is common. Here, evacuation at a high temperature in the first half is called “depressurization activation”, and high-pressure hydrogen introduction at a low temperature in the second half is called “pressurization activation”. Hydrogen-absorbing alloys that are difficult to activate, such as BCC-based hydrogen-absorbing alloys, have higher pressure activation conditions and higher vacuums, and lower pressure activation conditions than AB5- and AB2-based alloys that are easily activated. And high pressure is necessary. In addition, as the activation conditions are increased, the activation time is generally shortened. That is, the time until activation is completed is shorter when the pressure activation step is performed at 150 ° C. than 100 ° C., and when the pressure activation step is performed at 0 ° C. than 20 ° C. or 10 MPa rather than 1 MPa.
しかしながら、実用的な水素吸蔵合金容器を活性化する場合には、容器の設計温度、圧力に自ずと制限があるため、活性化条件を無制限に強めることはできない。金属容器であれば温度の許容幅は比較的広いものの、圧力の許容限度を超えることは容器の変形や破裂をもたらす可能性がある。さらに、活性化前後で水素吸蔵合金自身の体積も大きく変化するため、水素ガス圧力に加えて合金の膨張圧力も考慮に入れる必要がある。すなわち、加圧活性化時の導入水素圧は容器本来の設計圧力よりも低くせざるを得ない。このため、活性化速度の遅い水素吸蔵合金を内蔵した容器では、活性化に要する時間が長くなってしまう欠点があった。 However, when a practical hydrogen storage alloy container is activated, the design conditions and the pressure of the container are naturally limited, and thus the activation conditions cannot be increased without limit. A metal container has a relatively wide allowable temperature range, but exceeding the allowable pressure limit may cause deformation or rupture of the container. Furthermore, since the volume of the hydrogen storage alloy itself changes greatly before and after activation, it is necessary to take into account the expansion pressure of the alloy in addition to the hydrogen gas pressure. That is, the hydrogen pressure introduced during the pressure activation must be lower than the original design pressure of the container. For this reason, in a container containing a hydrogen storage alloy having a slow activation rate, there is a drawback that the time required for activation becomes long.
また、前述の従来方法を改良するために、次の特許文献1および2に記載の方法が提案されていた。
すなわち、特許文献1の方法の場合、水素吸蔵合金を水素とともにポリエチレン袋のような可塑性容器に封入し、袋ごと冷間静水圧プレスすることで活性化する方法が考案されている。しかしながら、水素吸蔵合金は自身の体積の1000倍近い水素を吸収することができることを考えると、例えば体積1Lの水素吸蔵合金(およそ6〜8kg)を活性化するためには、容積1m3の可塑性容器が必要になる。活性化する合金量に比例して可塑性容器体積は増えるため、大量処理には不向きな方法であった。
Further, in order to improve the above-described conventional method, methods described in the following
That is, in the method of
また、前述の特許文献2の方法の場合、水素ガス供給装置、不活性ガス供給装置、減圧装置を備えたベッセル内に、水素吸放出孔を開放した水素吸蔵合金容器を入れ、ベッセル内部ごと減圧および水素加圧することで、水素活性化する装置および方法が提案されている。この方法では、水素吸蔵合金容器の内外圧を均等にすることができるため、圧力差による容器の変形を考慮することなく、高圧で水素活性化することができる。しかしながら、この方法には、次のような欠点がある。(1)ベッセルごと減圧しなければならないため、水素吸蔵合金容器単体を減圧するときよりも減圧活性化時の真空度を上げることが困難である。(2)合金容器だけではなく、ベッセル内部すべてを高圧水素で満たさなくてはならないため、大量の水素が必要である。(3)熱交換用のジャケットは、減圧時の内圧および加圧時の外圧に共に耐えられる構造としなければならない。(4)活性化終了後、水素吸蔵合金容器を取り出す際は、水素を放出させた上で不活性ガスにてベッセル内部を置換し、さらに不活性ガスで置換したまま合金容器に蓋をしなければならず、装置および製造工程が複雑になっていた。
Moreover, in the case of the method of the above-mentioned
従来の水素吸蔵合金容器の活性方法は、以上のように構成されているため、次のような課題が存在していた。
すなわち、容器変形を防ぐため、加圧活性化時の水素圧力を一定以下に抑えているため、活性化に時間がかかっていた。そこで、容器に入れる前の水素吸蔵合金を水素ガスとともに可塑性容器に入れ、静水圧をかける事で活性化時間の短縮を図る方法が考案されたが、活性化前の容器体積が非常に大きくなるため、現実的な方法ではない。その他に、蓋を開放した水素吸蔵合金容器をべッセルに入れ、ベッセル内に水素を導入することで、合金容器内外圧を均圧させたまま、活性化する方法が考案されたが、活性化に必要な水素量が多くなることや、活性化終了後の合金容器の取り出しが難しいといった課題が存在していた。
Since the conventional method for activating a hydrogen storage alloy container is configured as described above, the following problems exist.
That is, in order to prevent deformation of the container, the hydrogen pressure during the pressurization activation is kept below a certain level, so that it takes time to activate. Therefore, a method has been devised to reduce the activation time by putting the hydrogen storage alloy before putting into the container together with hydrogen gas into a plastic container and applying hydrostatic pressure, but the container volume before activation becomes very large. Therefore, it is not a realistic method. In addition, a hydrogen storage alloy container with an open lid was placed in a vessel, and hydrogen was introduced into the vessel to devise a method for activation while keeping the pressure inside and outside the alloy container equalized. However, there are problems that the amount of hydrogen required for the process increases, and that it is difficult to take out the alloy container after the activation is completed.
本発明による水素吸蔵合金容器の活性化装置は、耐圧容器内に水素吸蔵合金容器が配置でき、前記耐圧容器の外部に配設された水素源に連通する水素配管が前記水素吸蔵合金容器に接続され、前記耐圧容器には前記耐圧容器に流入させる流体の流入口が設けられ、前記耐圧容器には前記流体の充填及び加圧ができる充填・加圧手段が接続されている構成であり、また、前記流体の熱を除去するための熱除去手段を有する構成であり、また、本発明による水素吸蔵合金容器の活性化方法は、請求項1又は2記載の水素吸蔵合金容器の活性化装置を用い、前記水素吸蔵合金容器に導入した水素の圧力と、前記流体の圧力とが平衡になるように調整しつつ前記水素吸蔵合金容器内の水素吸蔵合金を活性化する方法である。
The activation apparatus for a hydrogen storage alloy container according to the present invention can arrange a hydrogen storage alloy container in a pressure resistant container, and a hydrogen pipe communicating with a hydrogen source disposed outside the pressure resistant container is connected to the hydrogen storage alloy container. The pressure vessel is provided with an inlet for fluid flowing into the pressure vessel, and the pressure vessel is connected to a filling / pressurizing means capable of filling and pressurizing the fluid. The method for activating the hydrogen storage alloy container according to the present invention includes a heat storage means for removing heat from the fluid, and the activation method for the hydrogen storage alloy container according to
本発明による水素吸蔵合金容器の活性化装置及び方法は、以上のように構成されているため、次のような効果を得ることができる。
すなわち、水素吸蔵合金容器を耐圧容器に入れ、水素吸蔵合金容器外部を流体で満たした上で、水素圧力と流体圧力とを平衡させながら水素活性化させるように構成したので、水素吸蔵合金容器の変形を抑えながら高圧活性化ができると共に、流体によって水素吸収熱を除去できるため、水素活性化時間を短縮できる。
Since the apparatus and method for activating a hydrogen storage alloy container according to the present invention are configured as described above, the following effects can be obtained.
That is, since the hydrogen storage alloy container is placed in a pressure vessel, and the outside of the hydrogen storage alloy container is filled with a fluid, the hydrogen is activated while balancing the hydrogen pressure and the fluid pressure. The high pressure activation can be performed while suppressing deformation, and the heat of hydrogen absorption can be removed by the fluid, so that the hydrogen activation time can be shortened.
本発明は、水素吸蔵合金容器内部にかけられる水素圧力とほぼ同等の流体圧力を外部にかけることにより、水素吸蔵合金容器の変形の抑制と効率的な熱交換を両立させ、活性化時間の短縮を実現するようにし水素吸蔵合金容器の活性化装置及び方法を提供することを目的とする。 The present invention applies a fluid pressure substantially equal to the hydrogen pressure applied to the inside of the hydrogen storage alloy container to achieve both suppression of deformation of the hydrogen storage alloy container and efficient heat exchange, and shortening the activation time. An object of the present invention is to provide an apparatus and method for activating a hydrogen storage alloy container.
以下、図面と共に本発明による水素吸蔵合金容器の活性化装置及び方法の好適な実施の形態について説明する。
図1は本発明による水素活性化装置の一形態を示すもので、符号1で示される耐圧容器の蓋部2には、水素配管3、差圧計4及びエア抜き弁5が設けられている。
Hereinafter, preferred embodiments of an apparatus and method for activating a hydrogen storage alloy container according to the present invention will be described with reference to the drawings.
FIG. 1 shows an embodiment of a hydrogen activation apparatus according to the present invention, and a
前記耐圧容器1の本体部1Aには、流体6を貯蔵する流体タンク7が流体配管8を介して接続され、この流体配管8は前記本体部1Aの流入口9及び放出口10に接続されている。
前記流体配管8には、第1、第2、第3弁11,12,13が設けられていると共に、前記第1、第3弁11,13間には、この流体6を前記耐圧容器1内に充填・加圧するための充填・加圧ポンプ等からなる充填・加圧手段14が設けられている。
A fluid tank 7 for storing a fluid 6 is connected to the main body 1A of the
The fluid pipe 8 is provided with first, second, and
前記差圧計4及び充填・加圧手段14は、出力制御部15に接続され、前記差圧計4からの差圧4aに基づいて前記充填・加圧手段14の流体6の送り量を制御することができるように構成されている。
前記水素配管3には、圧力計16及びレギュレータ17を介して高圧水素源からなるタンク状の水素源18が接続されている。
The differential pressure gauge 4 and the filling / pressurizing means 14 are connected to an output control unit 15 and control the feed amount of the fluid 6 of the filling / pressurizing means 14 based on the
A tank-like hydrogen source 18 composed of a high-pressure hydrogen source is connected to the
次に、前述の構成において、水素活性化手順について述べる。まず、図1に示されるように、減圧活性化工程が終了した各水素吸蔵合金容器20を水素配管3に取り付け、図2に示されるように、蓋部2を閉める。前記蓋部2を閉めた状態で内部の工程のエアを抜きながら流体6を耐圧容器1内に充填し終わった後、水素18aを導入する。この水素18aと流体6との圧力の差圧が0になるように充填・加圧手段14で送り制御をしながら水素を徐々に加圧していき、目標圧力に達したら、圧力を一定に保ち、活性化終了まで待つ。水素活性化終了後は、流体の圧力と水素の圧力とを同時に抜き、水素吸蔵合金容器20の許容圧力以下まで水素圧力を下げる。最後に、前記耐圧容器1の蓋部2を開けて活性化済みの水素吸蔵合金容器20を取り外す。
Next, the hydrogen activation procedure in the above-described configuration will be described. First, as shown in FIG. 1, each hydrogen
尚、前記流体6としては、好ましくは水が用いられるが、活性化温度によっては、油や不凍液を用いても良い。また、水素圧力と流体圧力との差圧解消手段としては、図1に示したような差圧計4の出力に応じて送り出力を調整する方法の他、ダイアフラムやシリンダーを用いて機械的に水素圧力と流体との圧力バランスを取る方法も可能である。 The fluid 6 is preferably water, but oil or antifreeze may be used depending on the activation temperature. As a means for eliminating the differential pressure between the hydrogen pressure and the fluid pressure, in addition to the method of adjusting the feed output according to the output of the differential pressure gauge 4 as shown in FIG. A method of balancing the pressure and the fluid is also possible.
前述の水素吸蔵合金容器の活性化装置及び方法によって、水素吸蔵合金容器20の内外圧を平衡に保つことができるため、水素吸蔵合金容器20の変形を極力抑えながら高い水素圧力で活性化ができると共に、周囲の流体6への熱伝達によって発生した水素吸収熱を除去することができるので、活性化にかかる時間を短縮できる。また、図3のように冷媒を流入させた冷却コイル等からなる熱除去手段30を耐圧容器1に配置すると、水素吸収熱の除去効率は格段に向上し、活性化時間をさらに短くすることができる。ここで、流体6の熱除去手段30は、図3で例示した他に、耐圧容器1の外側に冷却コイルを巻いて耐圧容器1ごと冷却する方法や、流体配管の一部をコイル状にして冷却槽に浸け、流体を強制循環することで冷却する方法も可能である。
The internal and external pressures of the hydrogen
次に、本出願人が本発明による水素吸蔵合金容器の活性化方法について、従来方法と比較するため、定格水素容量50NLの水素吸蔵合金タンク(外寸φ50mm×H132mm、AB5合金330g内蔵)を用いて活性化速度比較の実験を行ったため、その結果について述べる。
従来方法による活性化手順は、次の通りである。(1)80℃の水槽に合金タンクを浸け、5時間真空引きをする。(2)15℃の水槽に合金タンクを浸けると共に、1MPaの水素を内部に導入する。合金タンクの水素吸収量は質量流量計で測定した。
本発明方法による活性化手順は、次の通りである。(1) 80℃の水槽に合金タンクを浸け、5時間真空引きをする。(2)15℃の水が循環するコイルを内部に設けた耐圧容器内に合金タンクを配置し、水素配管を接続して耐圧容器を閉める。(3)耐圧容器内部に水を充填し、水素圧力を徐々に上げていくとともに、平衡させて水圧もあげていく。(4)水素圧力、水圧がともに5MPaに達したら昇圧をやめ、水素吸収量を質量流量計で測定する。次に、水素充填を開始した時刻を0としたときのMHタンクの水素吸収量変化を図4に示す。従来方法では3.5時間かかった活性化が、本発明方法では2時間程度で完了することが判明した。
Next, in order to compare the activation method of the hydrogen storage alloy container according to the present invention with the conventional method, the present applicant uses a hydrogen storage alloy tank with a rated hydrogen capacity of 50 NL (external size φ50 mm × H132 mm, built-in AB5 alloy 330 g). The results of the activation rate comparison were described.
The activation procedure according to the conventional method is as follows. (1) Immerse the alloy tank in a water bath at 80 ° C and evacuate for 5 hours. (2) Immerse the alloy tank in a water bath at 15 ° C. and introduce 1 MPa of hydrogen into the interior. The amount of hydrogen absorbed in the alloy tank was measured with a mass flow meter.
The activation procedure according to the method of the present invention is as follows. (1) Immerse the alloy tank in a water bath at 80 ° C and vacuum for 5 hours. (2) An alloy tank is placed in a pressure vessel in which a coil in which water of 15 ° C. circulates is provided, and a hydrogen pipe is connected to close the pressure vessel. (3) Fill the pressure vessel with water, gradually increase the hydrogen pressure, and equilibrate to increase the water pressure. (4) When both the hydrogen pressure and water pressure reach 5 MPa, stop the pressure increase and measure the hydrogen absorption amount with a mass flow meter. Next, FIG. 4 shows a change in the hydrogen absorption amount of the MH tank when the time when the hydrogen filling is started is set to zero. It was found that the activation that took 3.5 hours in the conventional method was completed in about 2 hours in the method of the present invention.
1 耐圧容器
1A 本体部
2 蓋部
3 水素配管
4 差圧計
5 エア抜き弁
6 流体
7 流体タンク
8 流体配管
9 流入口
10 放出口
11〜13 第1〜第3弁
14 充填・加圧手段
15 出力制御部
16 圧力計
17 レギュレータ
18 水素源
18a 水素
20 水素吸蔵合金容器
30 熱除去手段
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CN102167285A (en) * | 2011-03-02 | 2011-08-31 | 上海师范大学 | Portable, safe and controllable hydrolysis hydrogen-producing device |
CN103253630A (en) * | 2013-05-16 | 2013-08-21 | 桂林电子科技大学 | Hydrolysis hydrogen production device with internal integrated feeding tank and layered heat conduction and drying architecture |
JP2016211646A (en) * | 2015-05-07 | 2016-12-15 | 株式会社日本製鋼所 | Hydrogen pressure rise storage system and boosting method of hydrogen pressure rise storage system |
CN114877241A (en) * | 2022-05-25 | 2022-08-09 | 武汉氢能与燃料电池产业技术研究院有限公司 | Activation hydrogen charging and discharging water bath device and method for hydrogen storage tank |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102167285A (en) * | 2011-03-02 | 2011-08-31 | 上海师范大学 | Portable, safe and controllable hydrolysis hydrogen-producing device |
CN103253630A (en) * | 2013-05-16 | 2013-08-21 | 桂林电子科技大学 | Hydrolysis hydrogen production device with internal integrated feeding tank and layered heat conduction and drying architecture |
JP2016211646A (en) * | 2015-05-07 | 2016-12-15 | 株式会社日本製鋼所 | Hydrogen pressure rise storage system and boosting method of hydrogen pressure rise storage system |
CN114877241A (en) * | 2022-05-25 | 2022-08-09 | 武汉氢能与燃料电池产业技术研究院有限公司 | Activation hydrogen charging and discharging water bath device and method for hydrogen storage tank |
CN114877241B (en) * | 2022-05-25 | 2024-05-17 | 武汉氢能与燃料电池产业技术研究院有限公司 | Hydrogen storage tank activation charging and discharging water bath device and method |
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