JP2009283425A - Oxidation reduction-type electricity storage device using circulatory regenerated pure water as electrolyte solution - Google Patents
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- 239000008151 electrolyte solution Substances 0.000 title claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 18
- 230000005611 electricity Effects 0.000 title abstract description 4
- 230000003647 oxidation Effects 0.000 title abstract description 3
- 238000007254 oxidation reaction Methods 0.000 title abstract description 3
- 150000003681 vanadium Chemical class 0.000 claims abstract description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 8
- 239000000843 powder Substances 0.000 claims abstract description 5
- 239000011347 resin Substances 0.000 claims abstract description 4
- 229920005989 resin Polymers 0.000 claims abstract description 4
- 239000003792 electrolyte Substances 0.000 claims description 56
- 230000033116 oxidation-reduction process Effects 0.000 claims description 10
- 239000003014 ion exchange membrane Substances 0.000 claims description 7
- 239000011230 binding agent Substances 0.000 claims description 3
- 230000005484 gravity Effects 0.000 claims description 3
- 238000004898 kneading Methods 0.000 claims description 3
- 238000005056 compaction Methods 0.000 claims description 2
- 229920000049 Carbon (fiber) Polymers 0.000 claims 1
- 239000004917 carbon fiber Substances 0.000 claims 1
- 239000000835 fiber Substances 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 abstract description 10
- 229910052739 hydrogen Inorganic materials 0.000 abstract description 10
- 238000005260 corrosion Methods 0.000 abstract description 5
- 230000007797 corrosion Effects 0.000 abstract description 5
- 229910052751 metal Inorganic materials 0.000 abstract description 5
- 239000002184 metal Substances 0.000 abstract description 5
- 230000008929 regeneration Effects 0.000 abstract description 5
- 238000011069 regeneration method Methods 0.000 abstract description 5
- 239000000243 solution Substances 0.000 abstract description 2
- 229910052720 vanadium Inorganic materials 0.000 description 11
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 11
- -1 tuffs Substances 0.000 description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 238000007599 discharging Methods 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 238000007710 freezing Methods 0.000 description 3
- 230000008014 freezing Effects 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 239000011435 rock Substances 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 229910001260 Pt alloy Inorganic materials 0.000 description 1
- 229910001069 Ti alloy Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000414 obstructive effect Effects 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000007670 refining 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
- Y02E60/10—Energy storage using batteries
Abstract
Description
本発明は、純水にイオン価数の変化する電解物質を溶解した電解液の酸化還元作用を利用した蓄電装置に関するものである。 The present invention relates to a power storage device using an oxidation-reduction action of an electrolytic solution in which an electrolytic substance whose ionic valence changes in pure water.
従来の電池は、電極の化学変化で充放電する方式で 耐久性や電気密度が小さいため大容量の装置化や廉価で伝導度の高い電極の実用化に問題あった。 Conventional batteries are charged and discharged by the chemical change of the electrodes, and have low durability and electrical density. Therefore, there are problems in realizing large capacity devices and practical use of inexpensive and high conductivity electrodes.
また希硫酸にバナジューム塩を溶解した電解液を使用した本発明装置と同様の酸化還元型蓄電装置も実用化されている。電解液に溶解したバナジュームのイオン価数の変化で充放電するため、電極の化学反応による寿命阻害要因がなく、長寿命で、大容量で、設置スペース自由度の大きい蓄電装置の実現が可能となったが、電解液の危険性や腐食性や硫化水素ガスの発生の問題で小型化や一般普及が困難とされている。 Also, a redox power storage device similar to the device of the present invention using an electrolytic solution in which vanadium salt is dissolved in dilute sulfuric acid has been put into practical use. Since charging and discharging are performed by changing the ionic valence of vanadium dissolved in the electrolyte, it is possible to realize a power storage device that has no long-lived, long-capacity, large-capacity, and large installation space freedom through no electrode chemical reaction. However, due to the risk of electrolyte solution, corrosiveness, and generation of hydrogen sulfide gas, miniaturization and general dissemination are difficult.
また上記の欠点を解決するため、イオン価数の異なるバナジュームを希硫酸で溶解した原液を純水で希釈溶解した電解液を使用した本発明装置と同様の酸化還元型蓄電装置も開発されているが、バナジューム塩の純水での溶解性に問題があり実用化に至っていない。 In addition, in order to solve the above-mentioned drawbacks, a redox type power storage device similar to the device of the present invention using an electrolytic solution obtained by diluting a stock solution obtained by dissolving vanadium having different ionic valence with dilute sulfuric acid with pure water has been developed. However, there is a problem with the solubility of vanadium salt in pure water, and it has not been put into practical use.
上述のように、イオン価数の異なるバナジューム電解液の酸化還元作用を利用した蓄電装置は、多くの長所を持っているが、その普及実用化については解決すべきいくつかの問題点もある。第一に、装置の効率を高め、小型化するために高濃度で、安定した、保守管理が容易で安全なバナジューム電解液が必要とされる。 As described above, the power storage device using the redox action of the vanadium electrolytes having different ionic valences has many advantages, but there are some problems to be solved for its practical use. First, there is a need for a highly concentrated, stable, easy to maintain and safe vanadium electrolyte to increase device efficiency and miniaturization.
また、電池セル内で電解液と接し電気を集めるため耐食性が高く、伝導性の優れた白金やチタン合金等の高価な電極板が使用されているが、価格が高いため汎用普及が難しい。耐食性が高く伝導性の優れた価格の安い電極板または電極装置が必要とされる。 In addition, expensive electrode plates such as platinum and titanium alloys having high corrosion resistance and excellent conductivity are used because they are in contact with the electrolytic solution in the battery cell and collect electricity, but their general use is difficult due to their high price. There is a need for an inexpensive electrode plate or electrode device that has high corrosion resistance and excellent conductivity.
また、電池の動作の発停時に、陰極側に、水素ガスが発生し、円滑な運転を阻害されるため、水素のガス化蓄積の防止が必要とされる。 In addition, since hydrogen gas is generated on the cathode side when the operation of the battery starts and stops and smooth operation is hindered, it is necessary to prevent hydrogen gasification and accumulation.
また、電解液貯蔵タンクを屋外に設置する場合、季節によって電解液の凍結や温度上昇が問題となる。 In addition, when the electrolytic solution storage tank is installed outdoors, freezing of the electrolytic solution and a rise in temperature become a problem depending on the season.
このような課題を解決するために本発明者は、天然深成岩や凝灰岩や金属やそれらの焼結体から放射される5〜10テラヘルツの遠赤外線領域の共鳴電磁波により、水の水素結合を分離し、水分子同士の結合しているクラスターを微細化し、水分子間の隙間の小さい純水にすることにより、バナジューム塩の微粉末が安定して溶解することを見出し、本発明をなすに至った。 In order to solve such problems, the present inventor separated hydrogen bonds of water by resonance electromagnetic waves in the far-infrared region of 5 to 10 terahertz emitted from natural plutonic rocks, tuffs, metals, and sintered bodies thereof. The present inventors have found that the fine powder of vanadium salt can be stably dissolved by refining a cluster in which water molecules are bonded to each other and making pure water with small gaps between water molecules, thereby achieving the present invention. .
すなわち、上記課題を解決するために、本発明の純水の電解液循環再生装置は、天然深成岩や凝灰岩や金属やそれらの焼結体から放射される5〜10テラヘルツの遠赤外線領域の共鳴電磁波で、遠赤外線領域のエネルギー領域の水素結合を励起し、切り離す。 That is, in order to solve the above-mentioned problems, the pure water electrolyte circulation regeneration device of the present invention is a resonance electromagnetic wave in the far-infrared region of 5 to 10 terahertz radiated from natural plutonic rock, tuff, metal, or a sintered body thereof. Thus, the hydrogen bond in the energy region of the far infrared region is excited and separated.
電解液循環再生装置が純水の水素結合を切り離し、クラスターを小さくしていることは、この電解循環再生装置を通過する水に空気を送り込むことで、小さくなった隙にナノバブル化された酸素が安定して溶存され、溶存酸素量が1.5〜2.5倍増加することや、水のPHが、通常の純水より1.5〜3倍上昇することで証明される。 The fact that the electrolyte circulation regenerator cuts off the hydrogen bonds of pure water and made the clusters smaller is that the air bubbled into the water that passes through this electrolysis circulation regenerator allows oxygen that has been nanobubbled into the gap It is proved by the fact that it is dissolved stably and the dissolved oxygen amount increases 1.5 to 2.5 times, and the pH of water rises 1.5 to 3 times that of ordinary pure water.
また本発明の第2の酸化還元型蓄電装置において、カーボン微粉末を90〜95%程度の重量比で樹脂バインダーと混練して圧密を繰り返すことにより、嵩比重を高め、伝導度を高めた電極補助板を、電極に圧接し、電解液に直接接する側に使用することにより、電解液の酸化還元により生ずる起電力、または充放電のための電力を、高効率で電解液を介して集電供給することにより電池セルの小型が図れるとともに、電極の腐食を防止する。 Further, in the second oxidation-reduction type power storage device of the present invention, an electrode having increased bulk specific gravity and increased conductivity by kneading carbon fine powder with a resin binder at a weight ratio of about 90 to 95% and repeating compaction. By using the auxiliary plate on the side in direct contact with the electrode and in direct contact with the electrolyte, the electromotive force generated by the oxidation / reduction of the electrolyte or the power for charging / discharging is collected through the electrolyte with high efficiency. By supplying, the battery cell can be reduced in size and the corrosion of the electrode can be prevented.
また本発明の第3の酸化還元型蓄電装置において、電池セルの電解液室内に充填され電解液内の電荷を効率良く集電するためのスポンジ状カーボンの粗密度を陰極電解液室側で、正極電解液室側よりも微細にすることにより、電池動作の発停時の円滑な動作を阻害する水素ガスが、陰極で蓄積されないようにする。 In the third oxidation-reduction type power storage device of the present invention, the coarse density of the sponge-like carbon charged in the electrolytic solution chamber of the battery cell for efficiently collecting the electric charge in the electrolytic solution on the cathode electrolytic solution chamber side, By making it finer than the cathode electrolyte chamber side, hydrogen gas that hinders smooth operation during battery operation is prevented from accumulating at the cathode.
また本発明の第4の酸化還元型蓄電装置において、電解液貯蔵タンクの外表面に、輻射熱を遮蔽するフィルムを貼り付けることにより、電解液貯蔵タンクを屋外に設置した場合の紫外線等の輻射熱による電解液の温度上昇や放射冷却による電解液の凍結を防止するとともに、有害電磁波ノイズの電解液への影響を防止する。 Further, in the fourth oxidation-reduction type power storage device of the present invention, by attaching a film that shields radiant heat on the outer surface of the electrolyte storage tank, the electrolyte storage tank is caused by radiant heat such as ultraviolet rays when the electrolyte storage tank is installed outdoors. It prevents the electrolyte from freezing due to temperature rise and radiation cooling of the electrolyte, and also prevents harmful electromagnetic noise from affecting the electrolyte.
本発明によれば、バナジューム塩を高濃度で安定して溶解でき、炭素含有率の高い電極補助板により高効率で集電し、陰極側の水素ガス蓄積を防ぐように電解液室に充填するスポンジカーボンの密度を高めることにより、小型で高効率の電解液酸化還元型蓄電装置を廉価で生産することができる。 According to the present invention, the vanadium salt can be stably dissolved at a high concentration, and the electrode chamber is filled with high efficiency by the electrode auxiliary plate having a high carbon content so as to prevent hydrogen gas accumulation on the cathode side. By increasing the density of the sponge carbon, a small and highly efficient electrolytic redox power storage device can be produced at low cost.
以下、本発明の実施形態について図面を参照しながら詳細に説明する。
図1は、本発明の概念を示すフロー図である。この蓄電装置は、電池セル内でイオン交換膜11をはさんで、イオン価数の異なる正極電解液室9と陰極電解液室10が接していて、充電時には水素イオンが、イオン交換膜11を介して陰極電解液室から陽極電解液室へ移動し、放電時には、陽極電解液室9から陰極電解液室10に水素イオンが移動するように構成され、電力は陽極電極板7及び陰極電極板8を介して取り出されるようになっている。Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
FIG. 1 is a flowchart showing the concept of the present invention. In this power storage device, the
正極及び陰極の電解液は、それぞれ正極液電解液貯蔵タンク1および陰極電解液貯蔵タンク2に貯蔵され、正極電解液循環ポンプ3および陰極電解液循環ポンプ4により電池セルを介して循環され、電池セル内でイオン交換膜11を介して、水素イオンを正極および陰極電解液室9及び10の間で移動することにより充放電を行なう。従って充放電能力は電池セル能力により決定されるが、蓄電量は電解液貯蔵タンク1及び2の容量で決定される。 The positive and negative electrode electrolytes are respectively stored in the positive electrode
装置全体を小型高効率化するためには、電気密度を高濃度にする必要があり、そのためにバナジューム塩を安定して均一に溶解する方法として、本発明では、天然深成岩や凝灰岩や金属やそれらの焼結体による5〜10テラヘルツの遠赤外線領域の共鳴電磁波発生体51及び61を充填した電解液循環再生装置5及び6を電極液循環系統の電解液循環ポンプ3および4の出口側設けていて、電解液の水分子間の水素結合を分離し、バナジューム塩を高濃度で安定して溶解する。 In order to make the entire device small and highly efficient, it is necessary to increase the electric density. Therefore, as a method for stably and uniformly dissolving the vanadium salt, in the present invention, natural plutonic rock, tuff, metal, and the like are used.
図2は、本発明の電池セルの模式図で、イオン交換膜11をはさんで正極電解液室9と陰極電解液室10があり、イオン価数の異なるバナジューム水溶液が循環ポンプ3及び4により電解液貯蔵タンク1及び2から移送され、陽極電解液室9では、充電時に、4価のバナジュームが5価のバナジュームとなり、放電時には5価の4価のバナジュームになる。また陰極電解液室10では、充電時に3価のバナジュームが2価のバナジュームになり、放電時には2価のバナジュームが3価になる。イオンの移動は水素イオンで行なわれる。 FIG. 2 is a schematic diagram of a battery cell according to the present invention, which has a positive
正極及び陰極電解液室内9及び10には、電解液の正極及び陰極電極補助板71及び81で効率良く電荷の移動による集電を行なうために、純綿を炭化したカーボンスポンジが充填され、陰極電極液室10には、正極電解液室9よりも微細で、空隙のサイズの細かい材料を使用することにより、電池動作停止時に水素ガスが陰極電解液室10に蓄積されることで、次の円滑な運転の阻害を防止する。 The positive electrode and
充放電動作で、正極及び陰極電解液室9及び10を、イオン交換膜11を介して移動する電荷を、効率良く集電し、金属電極の腐食を防止するため、カーボン微粉末を90〜95%程度の重量比で樹脂バインダーと混練して圧密を繰り返すことにより、嵩比重を高め、伝導度を高めた正極及び陰極電極補助板71及び81を、正極電極板7および陰極電極板8と圧接して構成している。 In the charge / discharge operation, 90 to 95 carbon fine powder is used to efficiently collect the charges moving through the
電解液貯蔵タンク1及び2を電池セルと分離して屋外に設置する場合、紫外線等の輻射熱による電解液の温度上昇や放射冷却による電解液の凍結を防止したり、有害電磁波ノイズの電解液への影響を防止するため、電解液貯蔵タンク1及び2の外表面に、輻射熱を遮蔽するフィルムを貼り付ける。 When the electrolytic
本発明によれば、保守点検が容易な、長寿命で、比較的容量の大きい電解液酸化還元型蓄電装置を、低価格で提供できるため、太陽光発電や風力発電のような不安定な起電力の自然エネルギーの蓄積が可能となり、温室効果ガスの排出削減にも貢献できる。また夜間の廉価な電気を蓄電、需要の多い昼間の電力として使用することにより、電力の平準化と節電が可能となる。 According to the present invention, it is possible to provide an electrolyte redox power storage device that is easy to perform maintenance and has a long life and a relatively large capacity at a low price. Accumulation of natural energy from electric power is possible, which can contribute to reducing greenhouse gas emissions. In addition, low-cost electricity at night can be stored and used as daytime power, which is in high demand, so that power leveling and power saving can be achieved.
1. 正極電解液貯蔵槽
2. 陰極電解液貯蔵槽
3. 正極電解液循環ポンプ
4. 陰極電解液循環ポンプ
5. 正極電解液循環再生装置
6. 陰極電解液循環再生装置
7. 正極電極板
8. 陰極電極板
9. 正極電解液室
10.陰極電解液室
11.イオン交換膜
20.正極電解液入り口配管
21.正極電解液出口配管
30.陰極電解液入り口配管
31.陰極電解液出口配管
51.共鳴電磁波発生体
61.共鳴電磁波発生体
71.正極補助電極板
81.陰極補助電極板1. 1. Positive electrode
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2014531721A (en) * | 2011-09-28 | 2014-11-27 | ユナイテッド テクノロジーズ コーポレイションUnited Technologies Corporation | Flow battery with two-phase storage |
US11056698B2 (en) | 2018-08-02 | 2021-07-06 | Raytheon Technologies Corporation | Redox flow battery with electrolyte balancing and compatibility enabling features |
US11271226B1 (en) | 2020-12-11 | 2022-03-08 | Raytheon Technologies Corporation | Redox flow battery with improved efficiency |
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2008
- 2008-05-19 JP JP2008154610A patent/JP2009283425A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014531721A (en) * | 2011-09-28 | 2014-11-27 | ユナイテッド テクノロジーズ コーポレイションUnited Technologies Corporation | Flow battery with two-phase storage |
US9350039B2 (en) | 2011-09-28 | 2016-05-24 | United Technologies Corporation | Flow battery with two-phase storage |
US11056698B2 (en) | 2018-08-02 | 2021-07-06 | Raytheon Technologies Corporation | Redox flow battery with electrolyte balancing and compatibility enabling features |
US11637298B2 (en) | 2018-08-02 | 2023-04-25 | Raytheon Technologies Corporation | Redox flow battery with electrolyte balancing and compatibility enabling features |
US11271226B1 (en) | 2020-12-11 | 2022-03-08 | Raytheon Technologies Corporation | Redox flow battery with improved efficiency |
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