JPH02287289A - Energy generation device - Google Patents
Energy generation deviceInfo
- Publication number
- JPH02287289A JPH02287289A JP1110973A JP11097389A JPH02287289A JP H02287289 A JPH02287289 A JP H02287289A JP 1110973 A JP1110973 A JP 1110973A JP 11097389 A JP11097389 A JP 11097389A JP H02287289 A JPH02287289 A JP H02287289A
- Authority
- JP
- Japan
- Prior art keywords
- heavy water
- oxygen
- cathode
- palladium
- deuterium
- 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.)
- Pending
Links
- XLYOFNOQVPJJNP-ZSJDYOACSA-N Heavy water Chemical compound [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 claims abstract description 122
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 25
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 25
- 239000001301 oxygen Substances 0.000 claims abstract description 25
- YZCKVEUIGOORGS-OUBTZVSYSA-N Deuterium Chemical compound [2H] YZCKVEUIGOORGS-OUBTZVSYSA-N 0.000 claims abstract description 17
- 229910052805 deuterium Inorganic materials 0.000 claims abstract description 17
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 15
- 238000002485 combustion reaction Methods 0.000 claims abstract description 8
- 239000000463 material Substances 0.000 claims description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 abstract description 63
- 229910052763 palladium Inorganic materials 0.000 abstract description 32
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 abstract description 16
- 239000007789 gas Substances 0.000 abstract description 14
- 229910052697 platinum Inorganic materials 0.000 abstract description 8
- 239000002994 raw material Substances 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- 239000000470 constituent Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000006096 absorbing agent Substances 0.000 description 4
- 230000004927 fusion Effects 0.000 description 4
- 239000003463 adsorbent Substances 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 3
- 241000580924 Turbinella Species 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 150000002940 palladium Chemical class 0.000 description 1
- -1 palladium Chemical compound 0.000 description 1
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 description 1
- 150000003057 platinum Chemical class 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
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
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/10—Nuclear fusion reactors
Landscapes
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
Description
【発明の詳細な説明】
［産業上の利用分野］
この発明は、重水素を吸着する材質からなる陰極を、陽
極とともに、電解槽内の重水の中に入れ、電流を流すこ
とによりエネルギを発生させる装置間するものである。[Detailed Description of the Invention] [Industrial Application Field] This invention generates energy by placing a cathode made of a material that adsorbs deuterium together with an anode into heavy water in an electrolytic cell and passing an electric current through it. This is a device that can be used to
［従来の技術および発明が解決しようとする課８］最近
、英国のサラサンプトン大学のフライシュタイン教授、
および米国のユタ大学のポンス教授らにより、室温で核
融合反応を起こすことに成功したとする報告がなされ注
目を浴びている。これらの報告では、パラジウムなどの
重水素を吸着しやすい材質からなる陰極と、白金などの
安定な陽極とを重水の中に入れ、両極間に電流を流すこ
とにより、核融合反応であると推測される陰極上での反
応を起こさせ、エネルギを発生させている。[Lesson 8 to be solved by conventional techniques and inventions] Recently, Professor Freistein of the University of Sarathampton in the UK,
Professor Pons and his colleagues at the University of Utah in the United States have reported that they have succeeded in causing a nuclear fusion reaction at room temperature, which has attracted attention. In these reports, it is speculated that a nuclear fusion reaction is produced by placing a cathode made of a material that easily adsorbs deuterium, such as palladium, and a stable anode, such as platinum, in heavy water and passing an electric current between the two electrodes. A reaction occurs on the cathode, generating energy.
これらの反応は核融合反応であるか否かは定かではない
が、このようなエネルギ発生反応を将来的に実用化可能
にすることが望まれる。Although it is not certain whether these reactions are nuclear fusion reactions, it is hoped that such energy-generating reactions will become practical in the future.
上記の反応は、重水中に入れた陽極および陰極間に電流
を流すことにより生じる反応であるため、上記の反応と
は別に、副反応的に電気分解反応が生じる。この電気分
解反応により消費される重水の量は、実際にはかなりの
量であり、この電気分解によって消費された重水を補う
ように、新たに重水を加えていく必要が生じ、エネルギ
発生のために必要なコストを高める結果となる。Since the above reaction is caused by passing an electric current between an anode and a cathode placed in heavy water, an electrolysis reaction occurs as a side reaction in addition to the above reaction. The amount of heavy water consumed by this electrolysis reaction is actually quite large, and it becomes necessary to add new heavy water to compensate for the heavy water consumed by this electrolysis, and in order to generate energy. This results in an increase in the necessary costs.
この発明の目的は、このような電気分解による重水の消
費に伴なう問題点を解消し、より低いコストでエネルギ
を発生させることの可能な装置を提供することにある。An object of the present invention is to provide an apparatus that can solve the problems associated with the consumption of heavy water by electrolysis and generate energy at a lower cost.
［課題を解決するための手段］
この発明のエネルギ発生装置では、電気分解反応により
発生した重水素および酸素を捕集して、燃焼反応させる
ことにより重水とし、この回収された重水を差び電解槽
内に戻し、再びエネルギ発生のための反応に使用するこ
とを特徴としている。[Means for Solving the Problems] In the energy generation device of the present invention, deuterium and oxygen generated by an electrolysis reaction are collected and subjected to a combustion reaction to produce heavy water, and the recovered heavy water is used for electrolysis. It is characterized by being returned to the tank and used again for reactions to generate energy.
［作用］
この発明のエネルギ発生装置では、電気分解反応により
発生した重水素および酸素を捕集し、これを重水として
再び使用するものであるため、原料である重水の消費量
を大幅に削減させることができ、発生させるエネルギを
より低コストで得ることが可能になる。[Function] The energy generation device of the present invention captures deuterium and oxygen generated by electrolysis reaction and reuses it as heavy water, thereby significantly reducing the consumption of heavy water, which is a raw material. This makes it possible to obtain the generated energy at a lower cost.
［実施例］
第１図は、この発明の一実施例を示す概略構成図である
。第１図を参照して、密閉容器１内には陰極の一部とな
るパラジウム容器３が設けられており、このパラジウム
容器３内に重水６が入れられている。密閉容器１のまわ
りには、密閉容器１内を冷却するための冷却水が通され
る冷却水バイブ２が設けられている。[Embodiment] FIG. 1 is a schematic diagram showing an embodiment of the present invention. Referring to FIG. 1, a palladium container 3 which becomes a part of a cathode is provided in a closed container 1, and heavy water 6 is placed in this palladium container 3. A cooling water vibrator 2 is provided around the closed container 1, through which cooling water is passed for cooling the inside of the closed container 1.
パラジウム容器３内には、円筒状のパラジウム陰極４が
設けられている。パラジウム陰極４の一方端には、循環
系配管８の一端が密閉して取付けられており、この循環
系配管８は熱交換器９を通り冷却器１０ｂを通して、パ
ラジウム陰極４の他方端に密閉して取付けられている。Inside the palladium container 3, a cylindrical palladium cathode 4 is provided. One end of a circulation system piping 8 is attached to one end of the palladium cathode 4 in a sealed manner. installed.
パラジウム陰極４内および循環系配管８内には加圧され
た状態の軽水が入れられている。Pressurized light water is contained in the palladium cathode 4 and the circulation system piping 8.
パラジウム陰極のまわりには、コイル状の白金陽極５が
設けられている。この白金陽極５は電源７の陽極と接続
されている。電源７の陰極はパラジウム陰極４およびパ
ラジウム容器３に接続されている。A coiled platinum anode 5 is provided around the palladium cathode. This platinum anode 5 is connected to the anode of a power source 7. The cathode of the power source 7 is connected to the palladium cathode 4 and the palladium container 3.
熱交換器９内には、循環系配管８内を通る加熱された軽
水からの熱によって加熱される水が通された配管１６が
設置されており、配管１６にはタービンｌｌａおよび冷
却器１０ａが取付けられている。Inside the heat exchanger 9, a pipe 16 is installed, through which water heated by the heat from the heated light water passing through the circulation system pipe 8 passes, and in the pipe 16, a turbine lla and a cooler 10a are installed. installed.
密閉容器１の上部には、密閉容器１内で発生したガスを
捕集するためのガス捕集管１７が設けられており、この
ガス捕集管１７にはタービン１１ｂおよび冷却器１０ｃ
が取付けられている。冷却器１０からの配管は重水溜め
１５およびエアドライヤ１２に接続されている。エアド
ライヤ１２は、ガス中に含まれる重水を分離するための
ものであり、分離された重水は、重水溜め１５に送られ
、重水素ガスおよび酸素は酸素吸着器１３に送られる。A gas collection pipe 17 for collecting gas generated within the closed container 1 is provided at the upper part of the closed container 1, and the gas collection pipe 17 is equipped with a turbine 11b and a cooler 10c.
is installed. Piping from the cooler 10 is connected to a heavy water reservoir 15 and an air dryer 12. The air dryer 12 is for separating heavy water contained in the gas. The separated heavy water is sent to a heavy water reservoir 15, and deuterium gas and oxygen are sent to an oxygen absorber 13.
酸素吸着器内には酸素を吸着する吸着材が設けられてお
り、この酸素吸着器１３には、燃焼器１４が接続されて
おり、さらに燃焼器１４は重水溜め１５に接続されてい
る。重水溜め１５で溜められた重水は、再び、パラジウ
ム容器３内に送られ再使用される。An adsorbent for adsorbing oxygen is provided in the oxygen adsorber 13 , and a combustor 14 is connected to the oxygen adsorber 13 , and the combustor 14 is further connected to a heavy water reservoir 15 . The heavy water stored in the heavy water reservoir 15 is sent to the palladium container 3 again and reused.
白金陽極５と、パラジウム陰極４およびパラジウム容器
３との間で、電源７からの電流が流れると、パラジウム
陰極４およびパラジウム容器３上で現在のところ核融合
反応と推測されている反応が起こり、エネルギが発生す
る。このエネルギにより、パラジウム陰極４が加熱され
、内部に入れられている軽水が加熱される。内部の軽水
は１００℃以上になっても蒸気とならないように加圧さ
れており、１００℃以上に加熱された軽水が循環系配管
８を通り熱交換器９に送られる。熱交換器９では、配管
１６内を循環する水が１００℃以上に加熱されて蒸気と
なり、この蒸気がタービン１１ａ内に送られて電気エネ
ルギに変換される。タービンｌｌａからの蒸気および冷
却された水は、冷却器１０ａにより冷却され、再び配管
１６を通り熱交換器９内で加熱され蒸気となる。When a current from the power source 7 flows between the platinum anode 5, the palladium cathode 4, and the palladium container 3, a reaction that is currently assumed to be a nuclear fusion reaction occurs on the palladium cathode 4 and the palladium container 3. Energy is generated. This energy heats the palladium cathode 4 and heats the light water contained inside. The light water inside is pressurized so that it does not turn into steam even if the temperature reaches 100°C or higher, and the light water heated to 100°C or higher is sent to the heat exchanger 9 through the circulation system piping 8. In the heat exchanger 9, water circulating in the piping 16 is heated to 100° C. or higher to become steam, and this steam is sent into the turbine 11a and converted into electrical energy. The steam and cooled water from the turbine lla are cooled by the cooler 10a, pass through the pipe 16 again, and are heated in the heat exchanger 9 to become steam.
熱交換器９を通り冷却された軽水は、冷却器１０ｂによ
り冷却されて、再びパラジウム陰極４の他方端からパラ
ジウム陰極４内に入り再び加熱される。The light water that has been cooled through the heat exchanger 9 is cooled by the cooler 10b, enters the palladium cathode 4 from the other end of the palladium cathode 4, and is heated again.
このようなエネルギ発生反応とともに、パラジラム容器
３内では、電気分解反応が生じる。電気分解反応により
発生した重水素および酸素は、密閉容器１の上部に集ま
り、ガス捕集管１７によりタービン１１ｂへ送られる。Along with such an energy generation reaction, an electrolysis reaction occurs within the palladium container 3. Deuterium and oxygen generated by the electrolysis reaction collect in the upper part of the closed container 1, and are sent to the turbine 11b through the gas collection pipe 17.
このようにして発生した重水素および酸素とともに、密
閉容器１内では、パラジウム容器３やパラジウム陰極４
の加熱により、重水６が蒸気となり、この蒸気となった
重水がガス捕集管１７により捕集されてタービン１１ｂ
に送られる。Along with the deuterium and oxygen generated in this way, the palladium container 3 and the palladium cathode 4 are
Due to heating, the heavy water 6 becomes steam, and this steamed heavy water is collected by the gas collection pipe 17 and is sent to the turbine 11b.
sent to.
タービンｌｌｂでは、この重水の蒸気を用いてタービン
を回転させ電気エネルギを取出す。このタービン１１ｂ
から排出されたガスは、冷却器１０Ｃを通り冷却され、
液化した重水は重水溜め１５に送られる。ガス成分はエ
アドライヤ１２に送られ、ここでさらに重水を吸着材に
よって分離し、分離した重水は重水溜め１５に送られる
。ガスは、さらに酸素吸着器１３に送られ、ここで酸素
が吸着材によって吸着されて取除かれる。重水素は燃焼
器１４に送られ、酸素吸着器１３で分離された酸素も燃
焼器１４に別のルートで送られる。燃焼器１４では、分
離した重水素および酸素を再び混合して燃焼反応を起こ
させ、この燃焼反応により重水を製造し、製造した重水
を重水溜め１５に送る。重水溜め１５に集められた重水
は、再びパラジウム容器３内の重水に加えられて再使用
される。In the turbine llb, this heavy water steam is used to rotate the turbine and extract electrical energy. This turbine 11b
The gas discharged from the is cooled through a cooler 10C,
The liquefied heavy water is sent to the heavy water reservoir 15. The gas component is sent to an air dryer 12, where heavy water is further separated by an adsorbent, and the separated heavy water is sent to a heavy water reservoir 15. The gas is further sent to an oxygen absorber 13 where oxygen is adsorbed and removed by an adsorbent. Deuterium is sent to the combustor 14, and oxygen separated by the oxygen absorber 13 is also sent to the combustor 14 via a different route. In the combustor 14, the separated deuterium and oxygen are mixed again to cause a combustion reaction, heavy water is produced by this combustion reaction, and the produced heavy water is sent to the heavy water reservoir 15. The heavy water collected in the heavy water reservoir 15 is reused by being added to the heavy water in the palladium container 3 again.
以上説明したように、この実施例のエネルギ発生装置で
は、重水の電気分解により発生した重水素および酸素を
捕集して、これを燃焼反応させることにより重水とし、
この回収した重水を再びエネルギ発生用の重水として再
使用している。このため、従来の装置のように電気分解
により重水が消費されることがなく、低コストでエネル
ギを発生させることができる。As explained above, in the energy generation device of this embodiment, deuterium and oxygen generated by electrolysis of heavy water are collected and converted into heavy water by a combustion reaction.
This recovered heavy water is reused as heavy water for energy generation. Therefore, unlike conventional devices, heavy water is not consumed by electrolysis, and energy can be generated at low cost.
第１図に示すような装置を用いてエネルギ発生の実験を
行なった。内径６０ｍｍのパラジウム容器３内に重水２
００ｃｃを入れ、これに塩化リチウムおよび塩化パラジ
ウムを合計で０．３ｇ溶解させた。パラジウム陰極４と
しては、外径２０ｍｍの円筒状の電極を用い、このパラ
ジウム陰極４のまわりには、白金線を直径４０ｍｍで１
０ターン巻いたコイル状の白金陽極５を設置した。パラ
ジウム陰極内には、軽水を２ｃｃ／分の流量で流し、熱
交換器９との間を循環させた。白金陽極５とパラジウム
容器３およびパラジウム陰極４との間には、２０Ｖ、５
００ｍＡで電流を流した。これによりタービンｌｌａお
よびタービン１１ｂに接続された発電機から発生したエ
ネルギは合計で１５Ｗであった。An experiment on energy generation was conducted using a device as shown in FIG. Heavy water 2 is placed in a palladium container 3 with an inner diameter of 60 mm.
00 cc was added, and a total of 0.3 g of lithium chloride and palladium chloride were dissolved therein. A cylindrical electrode with an outer diameter of 20 mm is used as the palladium cathode 4, and a platinum wire with a diameter of 40 mm is placed around the palladium cathode 4.
A coiled platinum anode 5 wound with 0 turns was installed. Light water was flowed into the palladium cathode at a flow rate of 2 cc/min and circulated between it and the heat exchanger 9. Between the platinum anode 5, the palladium container 3, and the palladium cathode 4, a voltage of 20 V, 5
A current of 00 mA was applied. As a result, a total of 15 W of energy was generated from the generators connected to turbine 11a and turbine 11b.
このようなエネルギ発生を１０時間行なった後、燃焼器
１４内を確認したところ、重水の水滴が約１ｇ確認でき
、電気分解によって発生した重水素および酸素から重水
が回収されたことが確認された。After generating energy in this way for 10 hours, we checked the inside of the combustor 14 and found approximately 1 g of heavy water droplets, confirming that heavy water was recovered from deuterium and oxygen generated by electrolysis. .
［発明の効果］
以上説明したように、この発明のエネルギ発生装置では
、電気分解反応により発生した重水素および酸素を捕集
してこれを燃焼反応させて重水とし、この重水を回収し
て用いている。このため、従来は電気分解により消費さ
れていた重水を、エネルギ発生の原料の重水として再使
用でき、より低コストでエネルギを発生させることがで
きる。[Effects of the Invention] As explained above, in the energy generation device of the present invention, deuterium and oxygen generated by an electrolysis reaction are collected and subjected to a combustion reaction to produce heavy water, and this heavy water is recovered and used. ing. Therefore, the heavy water conventionally consumed by electrolysis can be reused as heavy water as a raw material for energy generation, and energy can be generated at a lower cost.
第１図は、この発明の一実施例を示す概略構成図である
。
図において、１は密閉容器、２は冷却水パイプ、３はパ
ラジウム容器、４は円筒状のパラジウム陰極、５はコイ
ル状の白金陽極、６は重水、７は電源、８は循環系配管
、９は熱交換器、１０ａ、１０ｂ、１０ｃは冷却器、ｌ
ｌａ、ｌｌｂはタービン、１２はエアドライヤ、１３は
酸素吸着器、１４は燃焼器、１５は重水溜め、１６は配
管、１７はガス捕集管を示す。
特許出願人 住友電気工業株式会社FIG. 1 is a schematic diagram showing an embodiment of the present invention. In the figure, 1 is a closed container, 2 is a cooling water pipe, 3 is a palladium container, 4 is a cylindrical palladium cathode, 5 is a coiled platinum anode, 6 is heavy water, 7 is a power source, 8 is a circulation system piping, 9 is a heat exchanger, 10a, 10b, 10c are coolers, l
la and llb are turbines, 12 is an air dryer, 13 is an oxygen absorber, 14 is a combustor, 15 is a heavy water reservoir, 16 is a pipe, and 17 is a gas collection pipe. Patent applicant: Sumitomo Electric Industries, Ltd.
Claims (1)
もに、電解槽内の重水の中に入れ、前記陰極および陽極
間に電流を流すことにより前記陰極上で反応を起こさせ
エネルギを発生させる装置において、 前記陰極上の反応とは別に生じる電気分解反応により発
生した重水素および酸素を捕集して燃焼反応させること
により重水とし、この回収された重水を再び前記電解槽
内に戻すことを特徴とする、エネルギ発生装置。(1) A cathode made of a material that adsorbs deuterium is placed in heavy water in an electrolytic cell together with an anode, and a current is passed between the cathode and anode to cause a reaction on the cathode and generate energy. In the apparatus, deuterium and oxygen generated by an electrolysis reaction that occurs separately from the reaction on the cathode are collected and subjected to a combustion reaction to produce heavy water, and the recovered heavy water is returned to the electrolytic cell. Features: Energy generation device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1110973A JPH02287289A (en) | 1989-04-28 | 1989-04-28 | Energy generation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1110973A JPH02287289A (en) | 1989-04-28 | 1989-04-28 | Energy generation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02287289A true JPH02287289A (en) | 1990-11-27 |
Family
ID=14549188
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1110973A Pending JPH02287289A (en) | 1989-04-28 | 1989-04-28 | Energy generation device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02287289A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1994006123A1 (en) * | 1992-08-28 | 1994-03-17 | Arthur D. Little, Inc. | Material symmetry breaking for reversible energy storage |
| JPH07140277A (en) * | 1993-09-27 | 1995-06-02 | Toichi Chikuma | Cold nuclear fusion device |
-
1989
- 1989-04-28 JP JP1110973A patent/JPH02287289A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1994006123A1 (en) * | 1992-08-28 | 1994-03-17 | Arthur D. Little, Inc. | Material symmetry breaking for reversible energy storage |
| JPH07140277A (en) * | 1993-09-27 | 1995-06-02 | Toichi Chikuma | Cold nuclear fusion device |
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