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JP4885641B2 - Marine electrolysis factory - Google Patents
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JP4885641B2 - Marine electrolysis factory - Google Patents

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JP4885641B2
JP4885641B2 JP2006211566A JP2006211566A JP4885641B2 JP 4885641 B2 JP4885641 B2 JP 4885641B2 JP 2006211566 A JP2006211566 A JP 2006211566A JP 2006211566 A JP2006211566 A JP 2006211566A JP 4885641 B2 JP4885641 B2 JP 4885641B2
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electrolysis
water
turbine
power generation
magnesium
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JP2008038673A (en
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村原正隆
和市 関
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SIGMAKOKI Co Ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/138Water desalination using renewable energy
    • Y02A20/141Wind power
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/70Wind energy
    • Y02E10/72Wind turbines with rotation axis in wind direction
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/70Wind energy
    • Y02E10/74Wind turbines with rotation axis perpendicular to the wind direction
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/133Renewable energy sources, e.g. sunlight
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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  • Wind Motors (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Electrolytic Production Of Metals (AREA)

Description

浮体船甲板上に設置した風車や甲板下の表層海水中に船首が鋭角を成す単胴船を複数艇並べて形成した流路に列並みした水車などから得られる電力により海水の淡水化過程で得られる食塩を電気分解して苛性ソーダや船積みされたアルミナの溶融塩電気分解よりアルミニウム新地金を生産・貯蔵・輸送システムに関する。 Obtained in the process of seawater desalination by electric power obtained from windmills installed on a floating ship deck or water turbines lined up in a flow path formed by arranging a number of single-hull boats with sharp bows in the surface seawater beneath the deck. This is related to a system for producing, storing and transporting new ingots of aluminum by electrolyzing the salt produced and electrolyzing the molten salt of caustic soda and the loaded alumina.

ソーダ工業は、硫酸工業と共に化学工業の基礎工業で、化学工業はこの両者を出発点とする。2005年の統計によると我が国の生産量は455万トンと順調に推移している。しかし我が国のソーダ工業は原料塩の全てを輸入塩に頼っているため、その輸入価格の半分以上が輸送費である。さらにこの塩から苛性ソーダを生産するには電気分解のための大電力が欠かせず、現在以上のコスト上昇は我が国の苛性ソーダ・塩素工業の国際競争力を失わせることになる。その対策として、電力の深夜電力への移行、自家発電設備の新設や増設、あるいは輸送船舶の大型化などを促進することが緊急課題となっている。 The soda industry is the basic industry of the chemical industry together with the sulfuric acid industry, and the chemical industry starts from both. According to 2005 statistics, Japan's production volume is steady at 45.5 million tons. However, because soda industry in Japan relies on imported salt for all raw material salt, more than half of its imported price is transportation costs. Furthermore, high power for electrolysis is indispensable for producing caustic soda from this salt, and an increase in cost beyond the present level will cause the international competitiveness of our caustic soda / chlorine industry to be lost. As countermeasures, it has become an urgent issue to promote the transition of electric power to midnight power, the establishment or expansion of private power generation facilities, or the enlargement of transport vessels.

2004年度の統計によると我が国の新地金アルミの消費量は世界の7%の200万トンであり99%以上を輸入に頼っている。軽金属の代表格アルミニウムの精錬には大量の電力が必要であるため、発電コストが低い国が有利で、非特許文献1によると大規模な水力発電所を有するロシア、カナダ、アメリカ、ブラジルなどが上位を占めている。一方、石油などの海外依存度が高く電力料金が高い我が国は圧倒的に不利で、現在ボーキサイトから新地金の精錬を行っているのは、自家水力発電所を持つ日本軽金属・蒲原工場のみである。アルミニウム生産高世界第一位の中国ですら、非特許文献2に開示するように「中国アルミ産業発展政策」(2005年10月7日)では、電解アルミ及びアルミナ生産は発電コストの高い東部地域の工場は閉鎖して、水力資源や石炭資源が豊富な西部地域に生産拠点をシフトすることが盛り込まれ、さらに電解アルミメーカーのアルミナ輸入を奨励し、アルミナの輸入関税を3〜5%引き下げることを検討している。 According to the 2004 statistics, Japan's consumption of new bullion aluminum is 2 million tons, 7% of the world, and more than 99% depends on imports. The refining of light metal representative aluminum requires a large amount of power, so countries with low power generation costs are advantageous. According to Non-Patent Document 1, Russia, Canada, the United States, Brazil, etc., which have large-scale hydropower plants Occupies the top. On the other hand, Japan, which is highly dependent on foreign countries such as oil and has high electricity charges, is overwhelmingly unfavorable, and only the Nippon Light Metal and Ebara Plant, which has its own hydroelectric power plant, is currently refining new bullion from bauxite. . Even in China, the world's top producer of aluminum, as disclosed in Non-Patent Document 2, according to the “China Aluminum Industry Development Policy” (October 7, 2005), electrolytic aluminum and alumina production are in the eastern region where power generation costs are high. Will be closed and the production base will be shifted to the western region where hydropower and coal resources are abundant. In addition, electrolytic aluminum manufacturers will be encouraged to import alumina and reduce import duties on alumina by 3-5%. Are considering.

エネルギー、ソーダ、軽金属など国力を左右する産業の建て直しが急がれる。とくに食塩の電気分解による苛性ソーダの製造あるいはアルミニウムの精錬などには大電力が必要である。昨今のサンクトペテルブルクで開催されたロシアサミット、世界の原油生産シェアで12%とサウジアラビアに次ぐ2位、天然ガスでは22%と首位。「エネルギー安全保障」で世界に対する自国の影響力を誇示するロシア、豊富な天然資源を武器に国際的発言力を行使し始めた中国、こうした中で各国首脳の発言は原油消費の抑制策に重点を置いたが、脱石油の早急の対策として原子力、天然ガス、太陽などを挙げている。このように化石燃料を用いない自然エネルギーに頼ろうとする気運が大いに高まっている。自然エネルギー発電には風力、水力(潮力)、波力、太陽電池、太陽熱などがあるが、この中でも風力は地表に対して垂直に設置できるため他の自然エネルギー発電設置に比べて設置面積が少なく、しかも昼夜問わず利用できる。この風力発電を利用して未処理水や海水を逆浸透プラントで処理するための圧力ポンプの電力に利用することが特許文献1,2に開示されている。同様に海水の淡水化を目的として海水の汲み上げポンプの電力に風力発電を使用することが特許文献3に開示されている。また海水の淡水化装置から得られた淡水を電気分解して水素を生産する電力として風力発電を利用することが特許文献4に開示されている。 There is an urgent need to rebuild industries that influence national power, such as energy, soda, and light metals. In particular, high power is required for the production of caustic soda by electrolysis of salt or the refining of aluminum. Russia's summit held in St. Petersburg these days, the world's crude oil production share is 12%, second only after Saudi Arabia, and natural gas is 22%. Russia, which shows off its own influence on the world in “energy security”, China, which has begun to use international remarks with its abundant natural resources as a weapon, and the remarks of the leaders of each country focus on measures to curb crude oil consumption However, nuclear, natural gas, the sun, etc. are cited as urgent measures against oil removal. In this way, there is a great increase in the mood to rely on natural energy that does not use fossil fuels. Natural energy power generation includes wind power, hydropower (tidal power), wave power, solar cells, solar heat, etc. Among them, wind power can be installed perpendicular to the ground surface, so the installation area is smaller than other natural energy power generation installations It can be used both day and night. Patent Documents 1 and 2 disclose that this wind power generation is used for power of a pressure pump for treating untreated water and seawater in a reverse osmosis plant. Similarly, Patent Document 3 discloses the use of wind power generation for the power of a seawater pump for the purpose of desalination of seawater. Patent Document 4 discloses that wind power generation is used as electric power for electrolyzing fresh water obtained from a seawater desalination apparatus to produce hydrogen.

風力を直接動力源として用い海水の淡水化を行う試みもある。特許文献5には風車軸に空気圧縮機を連結し、圧縮空気タンクからの圧縮空気を海水に作用させて海水から真水を製造する浸透圧式海水淡水化装置が開示されている。また特許文献6には海水淡水化プラント用蒸発管に海水を送る手段として風力駆動式海水淡水化プラントが開示されている。 There are also attempts to desalinate seawater using wind power as a direct power source. Patent Document 5 discloses an osmotic seawater desalination apparatus in which an air compressor is connected to a wind turbine shaft, and fresh air is produced from seawater by causing compressed air from a compressed air tank to act on seawater. Patent Document 6 discloses a wind-driven seawater desalination plant as means for sending seawater to an evaporation pipe for a seawater desalination plant.

風力発電で得られるエネルギー(W)は、受風面積(A)、空気密度(ρ)、風速(V)とすると W=AρV/2 で与えられる。ここで空気の密度は1.2kg/m3に対し水の密度は1025kg/m3である。 このため風の流を水の流に換えれば854倍のエネルギーを得ることが出来る。日本周辺には黒潮(日本海流)と対馬海流があり、トカラ海峡、足摺岬、室戸岬、潮岬、三宅島・御蔵島を流れる黒潮は幅250km、水深1000m、流速0.3〜2m/秒であり格好の水流発電源である。 Energy obtained by wind power (W) is swept area (A), air density ([rho), is given by When the wind speed (V) W = AρV 3/ 2. Here, the density of air is 1.2 kg / m3 and the density of water is 1025 kg / m3. For this reason, if the wind flow is changed to the water flow, 854 times as much energy can be obtained. There are Kuroshio Current (Japan Current) and Tsushima Current around Japan. The Kuroshio Current flowing through Tokara Strait, Cape Ashizuri, Cape Muroto, Cape Shio, Miyakejima and Mikurajima is 250km wide, 1000m deep, and 0.3 to 2m / s in velocity. It is a water stream power source.

このように水車の出力は水流の3乗に比例するので水車の回転面を通過する水流速度を増大させれば効果絶大である。幸いにも単胴船を複数艇平行に並べて構成した流路は夫々の船首が鋭角であるため海流は必然的に舷に進むに連れて狭められるため流速は増速する。ここで船首が鋭角とは、水切り角が鋭い凸形を指し、V字型やU字型など船首から徐々に広がっていく形状を意味する。さらに船首を球状船首にすることにより単同船の造波抵抗は軽減する。このため流路中の水車からは高出力が得られる。このため流路に沿って垂直軸型水車あるいはプロペラ形水平軸水車を複数基列並みする。ただし1本の流路中に水車を縦に並べると後方すなわち下流の水車の速度は減衰する。このため各水車の前方に海水の流入速度を増大させるためにノズルフロー型増速装置を設備する。これにより、例えば流速を1.5倍に増速すると水車出力は3.38倍に増加する。このノズルフロー型増速装置は曲面壁を両舷あるいは水車の上下面、あるいはその両方に一体物として設備するもので、水車が垂直軸型の場合は角型拡声器形状であり、プロペラ形水平軸の場合はラッパ形状である。 As described above, the output of the water turbine is proportional to the cube of the water flow. Therefore, if the water flow velocity passing through the rotating surface of the water wheel is increased, the effect is great. Fortunately, the flow path composed of single hulls arranged in parallel with each other has an acute angle at the bow, so the ocean current inevitably narrows as it goes to the ridge, so the flow velocity increases. Here, the sharp angle of the bow means a convex shape with a sharp water drainage angle, and means a shape that gradually spreads from the bow, such as a V-shape or U-shape. Furthermore, the wave resistance of a single ship is reduced by making the bow a spherical bow. For this reason, high output is obtained from the water wheel in the flow path. For this reason, a plurality of vertical axis type turbines or propeller type horizontal axis turbines are arranged along the flow path. However, if the turbines are arranged vertically in one flow path, the speed of the downstream or downstream turbine is attenuated. For this reason, a nozzle flow type speed increasing device is installed in front of each turbine to increase the inflow speed of seawater. Thus, for example, when the flow velocity is increased by 1.5 times, the turbine output increases by 3.38 times. This nozzle flow type speed increasing device is equipped with curved walls as a single unit on both sides and / or the upper and lower surfaces of the water turbine. When the water wheel is a vertical shaft type, it is a square loudspeaker shape, and a propeller type horizontal In the case of a shaft, it is a trumpet shape.

上述した風力、流水力などの自然エネルギーは地球環境に優しく、かつ、資源の枯渇も起こさない格好なエネルギー源であるように思われがちで在るが、しかしこれらは全て自然的・地理的条件に制約され、気象条件や場所によっては所望の発電電力を得ることは困難である。そこで風力エネルギーあるいは潮流や海流など自然エネルギーが豊富に存在する洋上でそれらを利用する方法が提案されている。特許文献7では海上に浮遊設置されたプールに海洋深層水を汲み上げるために風力発電で得られた電力を使用することが開示されている。特許文献8には海水の電気分解による淡水化に風力発電を用いることが開示されている。特許文献9には海上に設置する大型浮体構造物に風力発電、波力発電、海洋温度差発電など自然エネルギーを利用する発電設備が開示されている。移動可能な海上浮体上で太陽熱による蒸気タービン発電や波力発電、風力発電などで得られた電力により淡水化された水を電気分解して水素や酸素ガスを生産することが特許文献10,11に開示されている。洋上の浮遊あるいは浮体船の甲板に設置する風車は風向に関係ない無指向性が望ましい。本願発明者は風力や水力の両エネルギーから電力を取り出す垂直軸風水車を特許文献12,13に開示している。 Natural energy such as wind power and hydropower mentioned above tends to seem to be a good energy source that is friendly to the global environment and does not cause resource depletion, but these are all natural and geographical conditions. It is difficult to obtain a desired generated power depending on weather conditions and places. Therefore, a method of using wind energy or offshore where there is abundant natural energy such as tidal current and ocean current has been proposed. Patent Document 7 discloses that electric power obtained by wind power generation is used to draw deep ocean water into a pool suspended on the sea. Patent Document 8 discloses that wind power generation is used for desalination by electrolysis of seawater. Patent Document 9 discloses a power generation facility that uses natural energy such as wind power generation, wave power generation, and ocean temperature difference power generation for a large floating structure installed on the sea. Patent Documents 10 and 11 include producing hydrogen and oxygen gas by electrolyzing water desalinated by electric power obtained by steam turbine power generation, wave power generation, wind power generation, etc. by solar heat on a movable floating body. Is disclosed. Wind turbines installed on the surface of floating or floating ship decks are preferably omnidirectional regardless of the wind direction. The inventor of the present application discloses vertical axis wind turbines that extract electric power from both wind energy and hydraulic energy in Patent Documents 12 and 13.

上述した参考文献を統括すると本発明は自然的・地理的条件あるいは気象条件や場所に制約されない手法として洋上で所望の発電電力と原料を得る構成により、食塩の輸入に頼らない苛性ソーダの生産やアルミニウム新地金の99%輸入から脱却し、原料のみの輸入に止め、自国精錬に切り替えるアルミ工業の育成を可能としている。 By integrating the above-mentioned references, the present invention can be used to produce caustic soda that does not rely on salt import or aluminum by using a configuration that obtains desired generated power and raw materials on the ocean as a method that is not restricted by natural / geographical conditions or weather conditions and locations. It has made it possible to nurture the aluminum industry by moving away from 99% imports of new bullion, stopping only imports of raw materials, and switching to domestic refining.

特公平2004−537668号Japanese Patent Publication No. 2004-537668 特開平2000−202441号公報Japanese Unexamined Patent Publication No. 2000-202441 特開平2004−290945号公報Japanese Patent Laid-Open No. 2004-290945 特開平2005−069125号公報Japanese Patent Application Laid-Open No. 2005-069125 特開平2003−083230号公報Japanese Patent Laid-Open No. 2003-083230 特公平2005−521557号Japanese Patent Publication No. 2005-521557 特開平2002−059893号公報Japanese Unexamined Patent Publication No. 2002-059893 特開平2001−213388号公報Japanese Patent Laid-Open No. 2001-213388 特開平2002−255091号公報Japanese Patent Laid-Open No. 2002-255091 特開平2002−303454号公報Japanese Patent Laid-Open No. 2002-303454 特開平2005−145218号公報Japanese Patent Laid-Open No. 2005-145218 特開平2003−206848号公報Japanese Patent Laid-Open No. 2003-206848 特開平2003−206849号公報Japanese Patent Application Laid-Open No. 2003-206849 特願2006−168275号Japanese Patent Application No. 2006-168275 日本国勢図会、財団法人矢野恒太記念会発行2006年6月1日 発行Issued on June 1, 2006 香港・経済通ニュース(2005年10月7日)Hong Kong Economic News (October 7, 2005) 電気化学概論・高橋武彦著、槇書店、1991年2月20日新版4刷Introduction to Electrochemistry, Takehiko Takahashi, Sakai Shoten, 4th edition, February 20, 1991 最新 商品の科学、株式会社 国勢社、79頁、昭和48年12月20日発行Latest product science, Kokuseisha, p. 79, published on December 20, 1973

従来のエネルギー資源の調達は経済性の観点から資源の豊富な場所に限られ、それを消費地に如何に経済的に運搬するかが課題であった。しかし近代産業は度重なる資源の乱獲をもたらし、これに起因する資源の世界的枯渇は、資源高をもたらし、これによる資源供給国の台頭は国際社会で影響力を拡大し、しいては我が国など需要国を脅かすような資源大国が台頭して来ている。まさに資源ウオーズの始まりである。幸いにも我が国は4面を海に囲まれ、200海里の大陸棚の外周を考えると豊富な資源国に成り得る可能性を持っている。海水に溶存する鉱物資源、海流・潮汐・海水の温度差などのエネルギー源、飲み水や工業用水も海洋資源である。これら無尽蔵にある海洋資源を化石燃料を使わず経済的に製造する事が本発明が解決しようとする課題である。 Conventional procurement of energy resources is limited to places where resources are abundant from the viewpoint of economy, and how to economically transport them to consumption areas has been a problem. However, modern industry has caused repeated over-exploitation of resources, and the resulting global depletion of resources has resulted in high resources, and the rise of resource-providing countries has increased its influence in the international community. Resource powers that threaten demanding countries are emerging. This is the very beginning of resource use. Fortunately, our country is surrounded by the sea, and considering the circumference of the continental shelf of 200 nautical miles, we have the potential to become an abundant resource country. Mineral resources dissolved in seawater, energy sources such as ocean currents, tides, seawater temperature differences, drinking water and industrial water are also marine resources. The problem to be solved by the present invention is to economically manufacture these inexhaustible marine resources without using fossil fuels.

風力発電に比べ黒潮などによる海流発電は、流量、流速が一定で、海流の幅が広く、かつ流水が止まる事がない。さらに水は風に比べて密度が高いため風の流を水の流に換えれば854倍のエネルギーを得ることができる。例えば、風の年平均風速6メートルに比べ黒潮の流速は高々2メートルである。そこで単胴船を複数艇平行に並べて構成した流路は夫々の船首が鋭角であるため海流は必然的に舷に進むに連れて狭められ、流速は速くなる。さらに船首を球状船首にすることにより単同船の造波抵抗は軽減する。この流路に沿って垂直軸型水車あるいはプロペラ形水平軸水車を列並みし、さらに海流の速度を速めるため各水車の前方に流入速度を増大するためのノズルフロー型海流増速装置を設備することにより、水車の羽根車やプロペラの直径を小さくでき、かつ1基の水車から得られる電力を増大させることが本発明の課題である。 Compared to wind power generation, ocean current power generation such as the Kuroshio Current has a constant flow rate and velocity, wide ocean current width, and flowing water never stops. Furthermore, since water has a higher density than the wind, 854 times more energy can be obtained by replacing the wind flow with the water flow. For example, compared to the annual average wind speed of 6 meters, the Kuroshio current flow rate is at most 2 meters. Therefore, the flow path constructed by arranging a plurality of monohulls in parallel with each other has an acute angle at the bow, so the ocean current is inevitably narrowed as it goes to the ridge, and the flow velocity increases. Furthermore, the wave resistance of a single ship is reduced by making the bow a spherical bow. In line with this flow path, vertical axis type turbines or propeller type horizontal axis turbines are lined up, and in order to increase the speed of the ocean current, a nozzle flow type ocean current speed increasing device for increasing the inflow velocity is installed in front of each turbine. Accordingly, it is an object of the present invention to reduce the diameter of the impeller and the propeller of the water wheel and increase the electric power obtained from one water wheel.

これまで海水の淡水化やマグネシウムなどの海水溶存金属の生産施設などは沿岸地域の火力発電所周辺に限られ、これら海水溶存金属はアルミニウム同様電力の化石と言われてきた。アルミニウム生産にいたっては非特許文献1に開示されている如く、我が国では新地金の99%を輸入に頼り、新地金の精錬を行っているのは、自家発電所を持つ日本軽金属・蒲原(静岡県)のみである。金属ナトリウムも同様で、日本曹達・二本木工場(新潟県)1か所のみである。一方、ソーダ工業の主要品苛性ソーダは電気分解による電力消費が多いため、苛性ソーダ事業部門の平成11年度収益は5億円の経営赤字であり、このままでは、我が国の苛性ソーダ・塩素工業の国際競争力を失わせることになる。これは製品1トン当たりの使用電力は非特許文献3に示してある如く、約2500kWhと多く、かつ原料塩は100%輸入である。とくに海水から原料塩が採取できる苛性ソーダ生産は本発明によって全て解決する。我が国では、昭和30年代までは水銀法が食塩電解法の主流であったが、昭和61年6月までに隔膜法やイオン交換膜法に全面転換が完了した。しかし非特許文献4に開示してあるように、製造の簡便さや高純度苛性ソーダ製造が可能な水銀法は捨てがたく、非特許文献3に示してあるように、世界の動静はいまだに水銀法が主流を占めている。 So far, seawater desalination and production facilities for water-soluble metals such as magnesium have been limited to the vicinity of thermal power plants in coastal areas, and these water-soluble metals have been said to be fossil powers like aluminum. As disclosed in Non-Patent Document 1, in Japan, 99% of new bullion is relied on for imports, and the refinement of new bullion is done by Nippon Light Metal with a private power plant, Sugawara ( Shizuoka Prefecture) only. The same applies to metallic sodium, and there is only one location at Nippon Soda and Nihongi Plant (Niigata Prefecture). On the other hand, because caustic soda, the main product of soda industry, consumes a lot of electricity due to electrolysis, the fiscal 2011 revenue of the caustic soda business is 500 million yen in deficit. It will be lost. As shown in Non-Patent Document 3, the power used per ton of product is as large as about 2500 kWh, and the raw material salt is 100% imported. In particular, the present invention solves all caustic soda production from which raw material salt can be collected from seawater. In Japan, the mercury method was the mainstream of the salt electrolysis method until the Showa 30s, but by June 1986, the full conversion to the diaphragm method and the ion exchange membrane method was completed. However, as disclosed in Non-Patent Document 4, the mercury method that is easy to manufacture and capable of producing high-purity caustic soda is difficult to throw away. Occupies the mainstream.

洋上構造物としては石油掘削井戸のようにプラットホームを建設するが、その開発に供給される莫大なエネルギーは石油に依存していた。ところが最近、洋上に豊富に在る太陽エネルギーや風力エネルギーを用いようとする提案がなされている。特許文献9には海上に設置する大型浮体構造物の発電設備として風力発電、波力発電、海洋温度差発電などの自然エネルギー利用が開示されている。特許文献10、11では太陽熱による蒸気タービン発電、波力発電、風力発電などで得られた電力により海水を淡水化した真水を電気分解して水素や酸素ガスを生産している。特許文献7では風力発電で得られた電力で海洋深層水を汲み上げている。風力発電を用いて海水の電気分解による淡水化が特許文献8に開示されている。しかし殆どが海水の淡水化止りでかん水の回収・濃縮・溶融塩電気分解による金属の製造は試みられず、まして、それら製造物を船倉に貯蔵・陸に寄港し、出航の際船積みしたアルミナや使用済み酸化マグネシウムを洋上で溶融塩電気分解して、新地金アルミニウムや金属マグネシウムを生産する海洋電気分解工場システムについては皆無である。 As an offshore structure, a platform was constructed like an oil drilling well, but the enormous energy supplied to the development depended on oil. Recently, however, proposals have been made to use solar and wind energy abundant on the ocean. Patent Document 9 discloses the use of natural energy such as wind power generation, wave power generation, and ocean temperature difference power generation as a power generation facility for a large floating structure installed on the sea. In patent documents 10 and 11, hydrogen and oxygen gas are produced by electrolyzing fresh water obtained by desalinating seawater with electric power obtained by steam turbine power generation, wave power generation, wind power generation, etc. by solar heat. In patent document 7, the deep sea water is pumped up with the electric power obtained by wind power generation. Patent Document 8 discloses desalination by electrolysis of seawater using wind power generation. But little is produced of metal by recovery, concentration, molten salt electrolysis of cans water desalination blind seawater attempts, let alone, their product calling at storage and land to hold and shipping time of departure alumina There is no marine electrolysis factory system that produces new bullion aluminum and metallic magnesium by electrolyzing molten magnesium at sea and using molten salt.

本発明は上述した問題点に鑑みて創案されたものである。すなわち、本発明の目的は、海流、風力などの流体エネルギーによるクリーンで再生可能なエネルギーで発生させた大電力を効果的に用い、電力生産現場にある海水を淡水化し真水を製造し、同時にその廃液の濃縮かん水から苛性ソーダ、金属ナトリウム、金属マグネシウム、塩素、水素ガスなどを生産し、それら生産物を寄港先で陸揚げし、陸地からはアルミナや使用済み酸化マグネシウムなどを船積みし、海流発電や風力発電から得られる豊富な電力を用いて港から船積みされた原料を溶融塩電気分解して金属アルミやマグネシウムを製造する。これらの全ての仕事を行う海洋工場・貨物船として、あるいは現場に留まって生産を続ける母船として、生産・貯蔵・輸送時におけるエネルギーロスを低減し、かつ、システム全体の効率を向上させることができる海洋電気分解工場を提供することにある。 The present invention has been made in view of the above-described problems. That is, the object of the present invention is to effectively use high power generated by clean and renewable energy by fluid energy such as ocean currents and wind power, and desalinate seawater at the power production site to produce fresh water, and at the same time caustic soda from the concentrated cans water waste, metallic sodium, metallic magnesium, producing chlorine, such as hydrogen gas, landed them product at ports of call destination, and shipping the alumina or spent magnesium oxide from land, Ya marine current power Using abundant electric power obtained from wind power generation, raw materials loaded from the port are electrolyzed with molten salt to produce metal aluminum and magnesium. As an offshore factory / cargo ship that performs all these tasks, or as a mother ship that continues production on the spot, it can reduce energy loss during production, storage, and transportation, and improve the efficiency of the entire system. To provide a marine electrolysis factory.

上記目的を達成するため、本発明の海洋電気分解工場は、本願発明者らが特許文献23に開示したごとく、大型双胴船や複胴船または単胴船あるいは潜水艦やメガよりフロートよりなり、洋上の資源採取場所で大量の電力を流体エネルギーから得るために甲板上下に無指向性垂直軸風水車やプロペラ形水平軸水車を複数台備え、生産しながら洋上を航行したり、資源摂取現場で浮遊したり、係留したりすることが出来る。とくに黒潮などの海流の流れを利用した海流発電を行う際には船を係留する。また海流発電を行う為には単胴船よりも複胴船が望ましく、2つ以上の船体を結合した甲板上部に無指向性垂直軸風車を複数其備え、甲板下部の表層海面下には海流発電用垂直軸水車やプロペラ形水平水車を複数其備する。 In order to achieve the above object, the marine electrolysis factory of the present invention, as disclosed in the patent document 23 by the present inventors, is composed of a large catamaran, a double-hull, a single-hull, a submarine, or a mega than a float, In order to obtain a large amount of power from fluid energy at offshore resource collection sites, it is equipped with multiple omnidirectional vertical axis wind turbines and propeller type horizontal axis turbines above and below the deck. Can float or moor. The ship is moored especially when performing ocean current power generation using ocean currents such as the Kuroshio Current. In order to generate ocean currents, a double hull is desirable rather than a single hull, and two or more omnidirectional vertical axis wind turbines are provided on the upper deck where two or more hulls are combined. Several vertical axis turbines and propeller-type horizontal turbines for power generation are provided.

単胴船を複数艇平行に並べて構成した流路は夫々の船首が鋭角であるため海流が舷に進むに連れて狭められ、必然的に流速は速くなる。さらに船首を球状船首にすることにより単同船の造波抵抗は軽減する。この単胴船を平行に複数艇並べて作った流路に垂直軸型水車あるいはプロペラ形水平軸水車をある間隔をおいて列並し、かつこれを各水路に設備する。さらに各水車の前面に上流の開口面積が広く水車タービン部が狭くなっているノズルフロー型海流増速装置を設置する。このノズルフロー型海流増速装置は垂直軸型水車の場合は角型拡声器状であり、プロペラ形水平軸水車の場合はラッパ状であり、これにより水車の発電効率をさらに高くすることができる。 The flow path composed of single hulls arranged side by side in parallel is narrowed as the ocean current advances to the dredging because each bow has an acute angle, and the flow velocity inevitably increases. Furthermore, the wave resistance of a single ship is reduced by making the bow a spherical bow. A vertical axis type turbine or a propeller type horizontal axis turbine is arranged in a line at a certain interval in a channel formed by arranging a plurality of boats in parallel, and this is installed in each channel. Furthermore, a nozzle flow type ocean current speed increasing device having a large upstream opening area and a narrow turbine turbine part is installed in front of each turbine. This nozzle flow type ocean current speed increasing device is in the form of a square loudspeaker in the case of a vertical axis type water turbine, and in the form of a trumpet in the case of a propeller type horizontal axis water turbine, which can further increase the power generation efficiency of the water turbine. .

海洋で生産した電力を用いて海水を逆浸透法により淡水化して真水を製造し、廃液として出るかん水を電気透析法により約30%に濃縮し、さらに煎ごうして食塩結晶を析出させ、濾液として残る苦汁と分離する。この苦汁から得られた塩化マグネシウムを溶融塩電気分解して金属マグネシウムを製造し、他方の食塩結晶は淡水化によって得られた真水で濃度約30%の食塩水を生成した後、水溶液電気分解を行い苛性ソーダを製造する。 To produce fresh water by desalination by reverse osmosis sea water by using the electric power produced at sea, the cans water exiting the waste is concentrated by electrodialysis to about 30%, and further decoction combined and precipitated with sodium chloride crystals, the filtrate Separate from the remaining bitter juice. Magnesium chloride obtained from this bitter juice is electrolyzed with molten salt to produce magnesium metal, and the other salt crystals are made from fresh water obtained by desalination to produce a salt solution having a concentration of about 30%. To produce caustic soda.

苛性ソーダ製造には、純粋な食塩水が得られれば、わざわざ食塩を製造する代わりに海水をイオン交換膜透析により約30%まで濃縮後、洋上工場で生産した苛性ソーダを少量入れて濃縮海水中の塩化マグネシウムなどの不純物を沈殿させ、その濾液を洋上工場で生産した塩化水素を真水と反応させて生産した塩酸で中和した電解液を電気分解することにより苛性ソーダを製造する。この苛性ソーダ製造工程で生成する水素は塩化水素や塩酸を作る原料として用い、残りはボンベに詰めて陸上に搬送する。塩素は苛性ソーダ製造工程およびナトリウムやマグネシウムの溶融塩電気分解で生産されるため塩化水素や塩酸を生産した残りはボンベに詰めて陸上に搬送する。 For the production of caustic soda, if pure saline is obtained, instead of producing salt, the seawater is concentrated to about 30% by ion-exchange membrane dialysis, and then a small amount of caustic soda produced at the offshore plant is added to salify the concentrated seawater. Caustic soda is produced by precipitating impurities such as magnesium and electrolyzing the electrolyte neutralized with hydrochloric acid produced by reacting hydrogen chloride produced at the offshore factory with fresh water. The hydrogen produced in the caustic soda manufacturing process is used as a raw material for producing hydrogen chloride and hydrochloric acid, and the remainder is packed in a cylinder and transported to the land. Chlorine is produced in the caustic soda manufacturing process and sodium and magnesium molten salt electrolysis, so the remainder of the hydrogen chloride and hydrochloric acid production is packed in a cylinder and transported to land.

アルミニウム新地金は非特許文献3に開示してあるように、輸入されたボーキサイト鉱石を粗砕し、付着水、結晶水、有機物などを除去するために回転炉で400〜600℃でばい焼する。これを20メッシュ以下に粉砕し、苛性ソーダを加え、オートクレーブ中140〜170℃、4〜5気圧で抽出するとアルミン酸ナトリウムとなって溶解する。これを水で希釈した後、不溶解分を沈殿または濾過により分離する。この溶液を冷却し、水で比重1.2に調節すると自然に加水分解されて水酸化アルミニウムが析出する。これに別に作った水酸化アルミ結晶を種結晶として加え、ゆっくり撹拌して反応を促進させると3〜5日で50〜60%の水酸化アルミが析出する。これをオリバーろ過機でろ過洗浄した後、高温で焼成して高純度アルミナを生産する。一般にアルミナ1トン製造するのにボーキサイト2トンと残渣が等倍出ることと高温でのばい焼および養生時間がかかるため、アルミナ製造は陸地あるいは輸入に頼ることが望ましいが、輸入ボーキサイトを洋上で生産した苛性ソーダおよび電力を用いて洋上生産することも可能である。このアルミナ約1トンに氷晶石を加え融点を935℃まで下げ、少量の蛍石を加え溶融塩電気分解により新地金アルミニウム約0.5トンを製造する。 As disclosed in Non-Patent Document 3, aluminum new bullion crushes imported bauxite ore and roasts it at 400-600 ° C in a rotary furnace to remove adhering water, crystal water, organic matter, etc. . When this is pulverized to 20 mesh or less, caustic soda is added, and extraction is performed at 140 to 170 ° C. and 4 to 5 atm in an autoclave, it becomes sodium aluminate and dissolves. After dilution with water, the insoluble matter is separated by precipitation or filtration. When this solution is cooled and adjusted to a specific gravity of 1.2 with water, it is naturally hydrolyzed to precipitate aluminum hydroxide. When aluminum hydroxide crystals prepared separately are added as seed crystals and the reaction is promoted by stirring slowly, 50 to 60% aluminum hydroxide precipitates in 3 to 5 days. This is filtered and washed with an Oliver filter and then fired at a high temperature to produce high purity alumina. Generally, to produce 1 ton of alumina, 2 tons of bauxite and a residue are produced at the same rate, and high temperature roasting and curing time are required. Therefore, it is desirable that alumina production depend on land or import, but import bauxite is produced offshore. It is also possible to produce offshore using caustic soda and electricity. Cryolite is added to about 1 ton of alumina to lower the melting point to 935 ° C., and a small amount of fluorite is added to produce about 0.5 ton of new metal aluminum by molten salt electrolysis.

上記したように、本発明によれば、海水採取現場で洋上の海流や風力などから得られた電力を効果的に使い、苛性ソーダ、真水、食塩、水素、塩素、塩酸、塩化水素、マグネシウム、ナトリウム等を製造し、同時に船積みしたアルミナや氷晶石および蛍石より新地金アルミニウムを製造し、生産品の貯蔵・輸送時のエネルギーロスをも低減することができ、かつシステム全体の効率を向上させることができる等の優れた効果が得られる。 As described above, according to the present invention, the power obtained from offshore currents and wind power is effectively used at the seawater collection site, caustic soda, fresh water, salt, hydrogen, chlorine, hydrochloric acid, hydrogen chloride, magnesium, sodium. At the same time, new bullion aluminum is manufactured from the loaded alumina, cryolite, and fluorite, reducing energy loss during storage and transportation of the product, and improving the efficiency of the entire system. An excellent effect is obtained.

以下、本発明の効果的な実施の形態を図1〜5に基づいて詳細に説明する。 Hereinafter, an effective embodiment of the present invention will be described in detail with reference to FIGS.

図1は、本発明の実施形態の概略構成図である。この図に示すように、本願発明の海洋電気分解工場は、海洋に浮かぶ浮体船・潜水体船1に、海流や風などの流体エネルギー資源2を利用して海流発電3や風力発電4を行う手段と、海水すなわち海水溶存鉱物資源5から汲み上げた海水6にポンプで圧力をかけ逆浸透法7により真水8を製造する海水の淡水化手段と、同時に排出される食塩濃度約5%のかん水をさらにイオン交換膜透析法9によりあるいは汲み上げた海水6を直接イオン交換膜透析法9により濃度約30%の濃縮かん水10を、海流や風などの流体エネルギー資源2から得られた電力あるいは溶融塩電気分解11,12,13で発生する熱を利用して煎ごう14を行うと、かん水の沸点108℃以上で食塩の微結晶が析出し始め、約160℃で粗結晶の食塩15が製造される。ここで同時に抽出する苦汁を取り出して煮詰め塩化マグネシウム16を海流発電3や風力発電4で得られた電力により溶融塩電気分解11して金属マグネシウム17を製造する。この工程で得られた食塩15を海水6の淡水化によって得られた真水8で溶解して電解質とした濃度約30%の食塩水18を水溶液電気分解19して苛性ソーダ20を製造する。この苛性ソーダ20製造には高純度苛性ソーダが簡便な方法で得られる水銀法の採用が望ましいが、我が国では水銀法は全廃されているため隔膜法やイオン交換膜法を用いる。海水から直接苛性ソーダ20を製造する方法として、イオン交換透析膜法9により生成した濃度約30%の濃縮かん水10を本発明で製造した苛性ソーダ20を少量注ぎ、苛性ソーダ処理21を行い、濃縮かん水10に含まれる塩化マグネシウムを沈殿させる。ここで沈殿した塩化マグネシウム16は金属マグネシウム17の原料として使われ、他方の母液は塩酸で中和処理22した後、電解質としての食塩水18を水溶液電気分解19して苛性ソーダ20を製造する。ここで中和に使われる塩酸は苛性ソーダ20を製造するための水溶液電気分解19の副産物として陽極から得られる塩素23と陰極から得られる水素24を反応させて生成した塩化水素25に真水8を加えて製造する。ここで苛性ソーダの製造工程に水銀法を採用すれば、水銀はきわめて高い水素過電圧のためナトリウムアマルガムを生成し、これに水を注げば簡単に苛性ソーダ20と水素24が高純度で取り出すことが出来る。ここで生産される残りの水素ガス24はボンベに詰めて港26から消費地に運ばれる。塩素ガス23は溶融塩電気分解11,12でも排ガスとして得られるため、これらを含めてボンベに詰めて港26から消費地に運ばれる。またここで製造された苛性ソーダ20の一部を溶融塩電気分解12により、金属ナトリウム27を製造し石油の中に貯蔵し港26から陸揚げする。他方陸地から船積みされた船積鉱物資源28の内使用済み酸化マグネシウム29は塩化工程30で塩化水素25と反応させて塩化マグネシウム16とした後、溶融塩電気分解11により金属マグネシウム17に再生される。一方の陸積鉱物資源28の内アルミの精錬原料であるアルミナ・氷晶石・蛍石31は溶融塩電気分解13により新地金アルミニウム32を製造する。 FIG. 1 is a schematic configuration diagram of an embodiment of the present invention. As shown in this figure, the marine electrolysis factory of the present invention performs ocean current power generation 3 and wind power generation 4 on a floating ship / submarine ship 1 floating in the ocean using fluid energy resources 2 such as ocean current and wind. means a seawater i.e. sea water by reverse osmosis 7 under pressure by a pump from the dissolved mineral resources 5 in seawater 6 pumped and desalination means seawater to produce fresh water 8, cans water salt concentration of about 5% of the discharged simultaneously further ion exchange membrane dialysis method 9 or by pumped concentrated cans water 10 at a concentration of about 30% by the seawater 6 directly ion-exchange membrane dialysis method 9, power or melt obtained from a fluid energy resources 2, such as ocean currents and wind Doing infusible rigid 14 by utilizing the heat generated by the salt electrolysis 11,12,13, microcrystalline sodium chloride at boiling point 108 ° C. or more cans water begins to precipitate, the brine 15 in the crude crystals at about 160 ° C. Manufactured . Here, the bitter juice extracted at the same time is taken out and boiled and the magnesium chloride 16 is subjected to molten salt electrolysis 11 with the electric power obtained by the ocean current power generation 3 and the wind power generation 4 to produce the metal magnesium 17. Sodium chloride 15 obtained in this step is dissolved in fresh water 8 obtained by desalination of seawater 6 to form an electrolyte, and an aqueous solution electrolyzed 19 of a salt solution 18 having a concentration of about 30% produces caustic soda 20. For the production of the caustic soda 20, it is desirable to adopt a mercury method by which a high-purity caustic soda can be obtained by a simple method. However, in Japan, the mercury method is completely abolished, and therefore a diaphragm method or an ion exchange membrane method is used. As a method for producing a directly caustic soda 20 from seawater poured a small amount of caustic soda 20 produced by the present invention a concentration of about 30% concentration cans water 10 produced by the ion-exchange dialysis membrane method 9 performs caustic soda process 21, concentrated cans water 10 is precipitated. The magnesium chloride 16 thus precipitated is used as a raw material for the metallic magnesium 17, and the other mother liquor is neutralized 22 with hydrochloric acid, and then electrolyzed 19 with an aqueous solution 18 of an electrolyte to produce caustic soda 20. Hydrochloric acid used for neutralization is added fresh water 8 to hydrogen chloride 25 produced by reacting chlorine 23 obtained from the anode and hydrogen 24 obtained from the cathode as a by-product of aqueous electrolysis 19 for producing caustic soda 20. Manufactured. Here, if the mercury method is adopted in the caustic soda production process, mercury produces sodium amalgam due to extremely high hydrogen overvoltage, and by pouring water into this, the caustic soda 20 and hydrogen 24 can be easily taken out with high purity. The remaining hydrogen gas 24 produced here is packed in a cylinder and transported from the port 26 to a consumption area. Since the chlorine gas 23 is also obtained as an exhaust gas in the molten salt electrolysis 11 and 12, it is packed in a cylinder including these and transported from the port 26 to the consumption area. A part of the caustic soda 20 produced here is produced by molten salt electrolysis 12 to produce metallic sodium 27, which is stored in petroleum and unloaded from the port 26. On the other hand, spent magnesium oxide 29 of the loaded mineral resources 28 loaded from the land is reacted with hydrogen chloride 25 in the chlorination step 30 to form magnesium chloride 16, and then regenerated to metal magnesium 17 by molten salt electrolysis 11. On the other hand, alumina, cryolite, and fluorite 31, which are raw materials for refining aluminum in land mineral resources 28, produce new bullion aluminum 32 by molten salt electrolysis 13.

本発明の海洋電気分解工場は、図1の浮体船・潜水体船1はタンカーなどの単胴船や複胴船あるいはメガフロートや潜水艦状の海中構造物を意味し、航行や浮遊しながら、あるいは係留して、苛性ソーダ、真水、食塩、水素、塩素、塩酸、塩化水素、マグネシウム、ナトリウム等を製造することが出来る。苛性ソーダを1トン製造するに必要な電力は約2500Kwh、アルミニウムは約13000kWh/トン、ナトリウムは約10500kWh/トン、マグネシウムは約10000kWh/トンと見込まれる。これらの電気分解に使用する電力を黒潮による海流発電や風力発電で賄おうとするのが本発明である。水車や風車1基当たりの発電量を5000kWに見込めば、これを200〜300基設備すれば100〜150万kWが得られる。浮体船・潜水体船1の大きさを幅1km、長さ2kmとし、この中に20〜30基の水車や風車を設備し、水車と風車の割合を3:1あるいは1:1とし、これを10〜20艇建造する。 In the marine electrolysis factory of the present invention, the floating ship / submarine ship 1 in FIG. 1 means a tanker or other monohull or double hull or a mega float or submarine underwater structure, Alternatively, it can be moored to produce caustic soda, fresh water, salt, hydrogen, chlorine, hydrochloric acid, hydrogen chloride, magnesium, sodium and the like. The electric power required to produce 1 ton of caustic soda is expected to be about 2500 Kwh, aluminum about 13000 kWh / ton, sodium about 10500 kWh / ton, and magnesium about 10,000 kWh / ton. It is the present invention that the electric power used for these electrolysis is covered by ocean current power generation or wind power generation by the Kuroshio Current. If the power generation amount per turbine or windmill is expected to be 5000 kW, 200 to 300 facilities can be obtained to obtain 1 to 1.5 million kW. The size of the floating ship / submarine ship 1 is 1 km wide and 2 km long, and 20 to 30 turbines and windmills are installed therein, and the ratio of the turbines and windmills is 3: 1 or 1: 1. Build 10-20 boats.

図2は海流から効果的に電力を得るための概略構成図である。この図に示すように、海流33中に係留した複胴浮体船1は、複数の単胴船35で流路を作り、この流路に沿って垂直軸型水車34をある間隔を隔てて複数基設備した模式図である。単胴船35は鋭角な船首36と舷38と鈍角な船尾37からなり所謂流線型構造を成し、造波抵抗を軽減し、かつ流路を構成する2艇の船首36の流路入り口の面積が舷38で構成される流路の面積より大であるため、海流は必然的に舷38に進むに連れて狭められ、流速は速くなる。このため流路中の水車34からは高出力が得られる。本発明では同様の水路を複数本作り電気分解用大電力を供給する。図3は図2の浮体船1を船首側から見た断面図である。複数の単胴船35によって作られた水路には、上甲板40と下甲板41および単胴船35の船底の竜骨近くには水車34の回転軸を固定するための固定板(翼)42を設備し、喫水線39より下部に水車34を設備する。尚この固定板42の断面は水路中の流速が速く成り、かつ船体を浮かす様に翼状に成っている。さらに船首を球状船首43にすることにより単同船の造波抵抗は軽減する。 FIG. 2 is a schematic configuration diagram for effectively obtaining power from the ocean current. As shown in this figure, a multihull floating ship 1 moored in an ocean current 33 forms a flow path by a plurality of single hulls 35, and a plurality of vertical axis type turbines 34 are spaced along the flow path at a certain interval. It is the schematic diagram which carried out the basic equipment. The monohull 35 is composed of an acute bow 36, an anchor 38 and an obtuse stern 37 to form a so-called streamlined structure, reduce the wave resistance, and the area of the flow path entrance of the bow 36 of the two boats constituting the flow path. Is larger than the area of the channel constituted by the ridge 38, the ocean current is inevitably narrowed as it proceeds to the ridge 38, and the flow velocity increases. For this reason, high output is obtained from the water wheel 34 in the flow path. In the present invention, a plurality of similar water channels are made to supply high power for electrolysis. FIG. 3 is a sectional view of the floating ship 1 of FIG. 2 as seen from the bow side. In the water channel formed by a plurality of single hulls 35, there are an upper deck 40 and a lower deck 41, and a fixing plate (wing) 42 for fixing the rotating shaft of the turbine 34 near the keel on the bottom of the single hull 35. Install a water turbine 34 below the water line 39. The cross section of the fixed plate 42 has a wing shape so that the flow velocity in the water channel is high and the hull is floated. Further, by making the bow a spherical bow 43, the wave resistance of the single ship is reduced.

図4は海流からさらに高電力を得るための概略構成図である。この図に示すように、海流33中に係留した複胴浮体船1は、複数の単胴船35で流路を作り、この流路に沿って垂直軸型水車34とそれよりも水車羽根車の直径が小さい水車45がある間隔を隔てて複数基設備した模式図である。単胴船35は鋭角な船首36と舷38と鈍角な船尾37からなり所謂流線型構造を成し、造波抵抗を軽減し、かつ流路を構成する2艇の船首36の流路入り口の面積が舷38で構成される流路の面積よりも大であるため、海流は必然的に舷38に進むに連れて狭められ、流速は速くなる。このため流路中の水車34からは高出力が得られる。ただし1本の流路中に水車を縦に並べると後方すなわち下流の水車の速度は減衰する。このため各水車の前方に海水の流入速度を増大させるために角型拡声器状のノズルフロー型増速装置44を設備する。このノズルフロー型増速装置44の概略を図5に示す。角型拡声器状のノズルフロー型増速装置44は浮体船1の喫水線39の下に設備され、複数の単胴船35の舷38に付けられた2枚一組の流体増速のための曲面板44と水車45の回転軸を固定する2枚の板兼増速のための曲面板46から成る角型拡声器状の増速装置43は水車45の前の海水流入口47から入った海流33は海水流出口48に進むにつれて断面積が小さくなり、流速が増大し、水車45の回転速度が増加する。このため浮体船1の船首36近くの水車34の羽根車直径よりも角型拡声器状の増速装置44の中の水車45の羽根車直径は小さくすることができ、かつ出力も大きい。本発明では同様の水路を複数本作り電気分解用大電力を供給する。 FIG. 4 is a schematic configuration diagram for obtaining higher power from the ocean current. As shown in this figure, a multihull floating ship 1 moored in an ocean current 33 forms a flow path by a plurality of single hulls 35, and a vertical axis type water wheel 34 and a water wheel impeller rather than that are formed along this flow path. It is the schematic diagram which installed two or more facilities at intervals with the water wheel 45 with a small diameter. The monohull 35 is composed of an acute bow 36, an anchor 38 and an obtuse stern 37 to form a so-called streamlined structure, reduce the wave resistance, and the area of the flow path entrance of the bow 36 of the two boats constituting the flow path. Is larger than the area of the channel formed by the ridge 38, the ocean current is inevitably narrowed toward the ridge 38, and the flow velocity is increased. For this reason, high output is obtained from the water wheel 34 in the flow path. However, if the turbines are arranged vertically in one flow path, the speed of the downstream or downstream turbine is attenuated. For this reason, in order to increase the inflow speed of seawater in front of each turbine, a nozzle flow type speed increasing device 44 in the form of a square loudspeaker is provided. An outline of the nozzle flow type speed increasing device 44 is shown in FIG. A square loudspeaker-like nozzle flow type speed increasing device 44 is installed under the waterline 39 of the floating ship 1 and is used for speeding up a set of two fluids attached to the anchor 38 of a plurality of monohulls 35. A rectangular loudspeaker speed increasing device 43 comprising a curved surface plate 44 and a curved surface plate 46 for speeding up to fix the rotating shaft of the water wheel 45 enters the seawater inlet 47 in front of the water wheel 45. As the ocean current 33 proceeds to the ocean outlet 48, the cross-sectional area decreases, the flow velocity increases, and the rotational speed of the water turbine 45 increases. Therefore, the impeller diameter of the water wheel 45 in the speed increasing device 44 in the form of a square loudspeaker can be made smaller than the impeller diameter of the water wheel 34 near the bow 36 of the floating ship 1, and the output is also large. In the present invention, a plurality of similar water channels are made to supply high power for electrolysis.

以上説明したように、本発明によれば、上記したように、海洋の海流や風力などの自然エネルギーから大電力を効果的に製造し、海水採取現場で苛性ソーダ、真水、食塩、水素、塩素、塩酸、塩化水素、マグネシウム、ナトリウム等を製造し、同時に港から船積みしたアルミナや氷晶石および蛍石より新地金アルミニウムを製造し、生産品の貯蔵・輸送時のエネルギーロスを低減することが出来ることは勿論のこと、システム全体のエネルギー効率の向上をも図ることができる。 As described above, according to the present invention, as described above, large power is effectively produced from natural energy such as ocean currents and wind power, and caustic soda, fresh water, salt, hydrogen, chlorine, Produces hydrochloric acid, hydrogen chloride, magnesium, sodium, etc., and at the same time produces new bullion aluminum from alumina, cryolite and fluorite loaded from the port, reducing energy loss during storage and transportation of products. Of course, the energy efficiency of the entire system can also be improved.

本願発明によれば、黒潮が流れる海域に係留した複胴船あるいはメガフロートで、その場生産した海流発電や風力発電から得た豊富な電力から、苛性ソーダや新地金アルミニウなどを製造し、副産物として、真水、食塩、水素、塩素、塩酸、塩化水素、マグネシウム、ナトリウム等を製造し、それら生産物を寄港先で陸揚げし、陸地からはアルミナや使用済み酸化マグネシウムなどを船積みし、新地金アルミニウムや金属マグネシウムを製造する。これらの全ての仕事を行う海洋工場・貨物船として、あるいは現場に留まって生産を続ける母船として、生産・貯蔵・輸送時におけるエネルギーロスを低減し、かつ、システム全体の効率を向上させることができる海洋電気分解工場である。このことは資源の世界的枯渇と資源高をもたらし、これに伴う資源供給国の台頭が国際社会に影響力を拡大させている現況を沈静化するに留まらず、無尽蔵にあるクリーンで再生可能な海洋資源を化石燃料を使わず経済的に製造する事は、4面を海に囲まれる我が国の産業に取って重要な手段である。 According to the present invention, a complex ship or mega float moored in the sea area where the Kuroshio Current flows, and from the abundant electric power obtained from ocean current power generation and wind power generation produced in situ, caustic soda, new bullion aluminum, etc. are manufactured as by-products Manufacture fresh water, salt, hydrogen, chlorine, hydrochloric acid, hydrogen chloride, magnesium, sodium, etc., land these products at the port of call, and load alumina, spent magnesium oxide, etc. Produces magnesium metal. As an offshore factory / cargo ship that performs all these tasks, or as a mother ship that continues production on the spot, it can reduce energy loss during production, storage, and transportation, and improve the efficiency of the entire system. It is a marine electrolysis factory. This has led to a global depletion of resources and high resources, and the rise of resource-providing countries that accompanies this has not only calmed down the current situation that is expanding its influence on the international community, but also an inexhaustible clean and renewable resource. Producing marine resources economically without using fossil fuels is an important means for Japanese industries surrounded by the sea.

本発明の実施の形態を示す概略構成図である。図中の2重枠はエネルギー源や原料であり、白抜き文字は生産物を示す。It is a schematic block diagram which shows embodiment of this invention. Double frames in the figure are energy sources and raw materials, and white letters indicate products. 本発明の複胴船を水路として用いる流体エネルギー発電用水車の配置を説明するための平面図である。It is a top view for demonstrating arrangement | positioning of the turbine for fluid energy power generation which uses the compound boat of this invention as a water channel. 本発明の複胴船を水路として用いる流体エネルギー発電用水車の配置を説明するための船首から見た断面図である。It is sectional drawing seen from the bow for demonstrating arrangement | positioning of the turbine for fluid energy power generation which uses the compound boat of this invention as a water channel. 本発明の複胴船を水路として用い、その水路中に流速増速装置を増設し、流体エネルギー発電用水車の配置を説明するための平面図である。It is a top view for demonstrating arrangement | positioning of the water turbine for fluid energy power generation using the double hull ship of this invention as a water channel, adding a flow-speed speed-increase apparatus in the water channel. 角型拡声器状ノズルフロー海流増速概略構成図である。It is a square loudspeaker-like nozzle flow ocean current speed-up schematic block diagram.

符号の説明Explanation of symbols

1 浮体船・潜水体船
2 流体エネルギー資源
3 海流発電手段
4 風力発電手段
5 海水溶存鉱物資源
6 海水
7 逆浸透法
8 真水
9 イオン交換膜透析法
10 濃縮かん
11 溶融塩電気分解装置(マグネシウム用)
12 溶融塩電気分解装置(ナトリウム用)
13 溶融塩電気分解装置(アルミニウム用)
14 煎ごう
15 食塩
16 塩化マグネシウム
17 マグネシウム
18 食塩水
19 水溶液電気分解(苛性ソーダ用)
20 苛性ソーダ
21 苛性ソーダ処理
22 塩素中和処理
23 塩素ガス
24 水素ガス
25 塩化水素ガス
26 港
27 ナトリウム
28 船積み鉱物資源
29 使用済み酸化マグネシウム
30 塩化処理
31 アルミナ・氷晶石・蛍石
32 アルミニウム
33 海流
34 垂直軸型水車(直径大)
35 単胴船
36 船首
37 船尾
38 舷
39 喫水線(海面)
40 甲板上部
41 甲板下部
42 水車固定翼
43 球状船首
44 増速曲面板(舷の左右)
45 垂直軸型水車(直径小)
46 増速曲面板(水車軸の上下)
47 海流入口
48 海流出口
1 Floating ship / submersible ship 2 Fluid energy resources
3 marine current power means 4 wind power unit 5 seawater dissolved minerals 6 sea 7 reverse osmosis 8 freshwater 9 ion exchange membrane dialysis method 10 concentrated cans water 11 molten salt electrolysis apparatus (for magnesium)
12 Molten salt electrolyzer (for sodium)
13 Molten salt electrolyzer (for aluminum)
14 Sengo 15 Salt 16 Magnesium chloride 17 Magnesium 18 Salt solution 19 Aqueous solution electrolysis (for caustic soda)
20 Caustic Soda 21 Caustic Soda Treatment 22 Chlorine Neutralization Treatment 23 Chlorine Gas 24 Hydrogen Gas 25 Hydrogen Chloride Gas 26 Port 27 Sodium 28 Shipping Mineral Resources 29 Used Magnesium Oxide 30 Chlorination Treatment 31 Alumina, Cryolite, Fluorite 32 Aluminum 33 Ocean Current 34 Vertical shaft type water wheel (large diameter)
35 Monohull 36 Bow 37 Stern 38 舷 39 Water Line (Sea Level)
40 Upper deck 41 Lower deck 42 Turbine fixed wing 43 Spherical bow 44 Accelerated curved surface plate
45 Vertical shaft type water wheel (small diameter)
46 Speed-up curved plate (up and down the water wheel shaft)
47 ocean current inlet 48 ocean current outlet

Claims (3)

海洋に浮かぶ複胴又は単胴あるいはメガフロートからなる浮体船または浮遊船、あるいは潜水艦状の海中構造物において、
海流や風などの流体エネルギーを利用して水車や風車による発電を行う手段と、
海水を淡水化させて真水を製造する手段と、
前記淡水化工程で排出されるかん水をさらに濃縮して得られた食塩を真水で希釈した食塩水、又はイオン交換透析膜により生成した濃縮塩水を苛性ソーダ処理した後の食塩水を電気分解して苛性ソーダを製造する手段と、
船積みしたアルミナと氷晶石と蛍石を溶融塩電気分解してアルミニウム新地金を製造する手段と、
食塩の製造工程で苦汁として得られた塩化マグネシウムを溶融塩電気分解して金属マグネシウムを製造する手段と、
前記食塩水の電気分解により陰極で発生した水素と陽極で発生した塩素を反応させて生成した塩化水素を船積みした使用済み酸化マグネシウムと反応させて生成した塩化マグネシウムを溶融塩電気分解により金属マグネシウムを製造する手段と、
苛性ソーダの溶融塩電気分解により金属ナトリウムを製造する手段と、
前記塩化水素を真水と反応させて塩酸を製造する手段と、
前記食塩水の電気分解で得られた副産物の水素ガスや塩素ガスあるいは溶融塩電気分解で得られた塩素ガスをボンベに貯蔵する手段とを具備したことを特徴とする海洋(洋上)電気分解工場。
In floating bodies or floating ships composed of double or single bodies or mega floats floating in the ocean, or submarine-like underwater structures,
Means for generating electricity by a water wheel or wind turbine using fluid energy such as ocean current or wind;
Means for producing fresh water by desalinating seawater;
Caustic soda is obtained by electrolyzing the sodium chloride solution obtained by further diluting the brine discharged in the desalination step with salt water obtained by diluting the salt water with fresh water or the sodium chloride solution produced by the ion-exchange dialysis membrane, and then subjecting the saline solution to electrolysis. Means for manufacturing,
Means for producing aluminum new bullion by electrolyzing molten alumina, cryolite, and fluorite,
Means for producing magnesium metal by electrolyzing molten salt electrolysis of magnesium chloride obtained as bitter in the salt production process;
The magnesium chloride produced by reacting the hydrogen produced at the cathode by the electrolysis of the brine and the chlorine produced at the anode by reacting with the used magnesium oxide loaded with the magnesium chloride is converted into the magnesium metal by the molten salt electrolysis. Means for manufacturing;
Means for producing sodium metal by molten salt electrolysis of caustic soda;
Means for reacting the hydrogen chloride with fresh water to produce hydrochloric acid;
A marine (offshore) electrolysis plant comprising means for storing hydrogen gas, chlorine gas, or by-product chlorine gas obtained by molten salt electrolysis obtained by electrolysis of the brine in a cylinder .
前記海洋(洋上)電気分解工場は、船首が鋭角な単胴船を複数艇平行に並べて形成された浮体船または浮遊船からなり、
該複数単胴船の互いに対向した舷により形成される夫々の流路に沿って垂直軸型水車あるいはプロペラ型水平軸水車を列並みに配置させ、該水車による発電を行うことを特徴とする請求項1記載による海洋(洋上)電気分解工場における発電方法。
The marine (offshore) electrolysis factory is composed of a floating ship or a floating ship formed by arranging a plurality of monohull boats with sharp bows in parallel,
A vertical axis type turbine or a propeller type horizontal axis turbine is arranged in a line along each flow path formed by the mutually opposite dredgers of the plurality of single hulls, and power generation by the turbine is performed. Item 1. A power generation method in an ocean (offshore) electrolysis factory according to item 1.
前記垂直軸型水車または前記プロペラ型水平軸水車の作動領域でノズルフローを起こさせる機能を持たせるために該単胴船の両舷(左右)に曲面壁を設備または前記流路に曲面壁からなる角型拡声器形状あるいはラッパ形状のホーン状構造体を設備し
船首方向が拡開させた開口部から流入した海流が曲面壁により船尾方向に絞り込まれる通路形状により海流を増速させ、絞り込まれた最狭部には、該水車を配備し、水車の回転運動を増幅させることにより発電させることを特徴とする請求項記載による海洋(洋上)電気分解工場における発電方法。
In order to impart functions to cause nozzle flow at the operating region of the vertical axis type hydraulic turbine or the propeller type horizontal axis water turbine, the curved wall and equipment on both side of the ship of the single hulls (right and left), or the flow path Equipped with a square loudspeaker shape or trumpet-shaped horn-like structure consisting of curved walls ,
The ocean current that has flowed in through the opening that has been widened in the bow direction is accelerated by the shape of the passage that is narrowed in the stern direction by the curved wall. The power generation method in the marine (offshore) electrolysis factory according to claim 2, wherein power is generated by amplifying the power.
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