JPH0530995B2 - - Google Patents
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- Publication number
- JPH0530995B2 JPH0530995B2 JP62077115A JP7711587A JPH0530995B2 JP H0530995 B2 JPH0530995 B2 JP H0530995B2 JP 62077115 A JP62077115 A JP 62077115A JP 7711587 A JP7711587 A JP 7711587A JP H0530995 B2 JPH0530995 B2 JP H0530995B2
- Authority
- JP
- Japan
- Prior art keywords
- heat
- steam
- generator
- hydrogen
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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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
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/46—Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、無公害で、かつ無限の太陽エネル
ギーを電気エネルギーに変換する太陽熱発電に係
るもので、特に高い稼働率と高い効率とを有する
発電装置に関するものである。[Detailed Description of the Invention] [Field of Industrial Application] This invention relates to solar thermal power generation that is pollution-free and converts infinite solar energy into electrical energy, and has particularly high operating rate and high efficiency. This relates to power generation equipment.
第6図a〜cは従来の太陽熱発電装置の各種例
を示すもので、第6図aは側面図、第6図b,c
は斜視図である。
Figures 6a to 6c show various examples of conventional solar power generation devices, with Figure 6a being a side view and Figures 6b and c.
is a perspective view.
第6図aはタワー方式を示し、入射する太陽光
14を追尾する多数の太陽追尾平面鏡27で反射
された太陽光14をタワー上部の塔上型集熱器3
0に集光して蒸気を発生し、タービン発電機5を
回して発電していた。第6図bは樋型放物面鏡2
8の焦線に線型集熱管31を置き、蒸気を発生
し、上記と同様に発電していた。第6図cは回転
放物面鏡29の焦点に高温集熱器32を置き、集
熱し発電を行つていた。 FIG. 6a shows a tower system, in which sunlight 14 reflected by a large number of solar tracking plane mirrors 27 that track incident sunlight 14 is transferred to a tower-top type heat collector 3 at the top of the tower.
The light was focused at zero to generate steam, which turned the turbine generator 5 to generate electricity. Figure 6b shows the gutter-shaped parabolic mirror 2.
A linear heat collecting tube 31 was placed on the focal line of 8 to generate steam and generate electricity in the same manner as above. In FIG. 6c, a high-temperature heat collector 32 is placed at the focal point of a rotating parabolic mirror 29 to collect heat and generate electricity.
しかしながら、上記従来の太陽熱発電装置のい
ずれにおいても、各集熱器30,32あるいは線
型集熱管31で集めた熱を断熱した高温水配管3
3によつて一箇所に集め発電用に提供している。
また、このようにして集められた熱を発電負荷の
変動に対処するため、断熱した蓄熱槽34に蓄え
て発電用に提供している。したがつて配管途中や
蓄熱時の熱損失は無視することができず、このた
めプラントの熱効率と稼働率とを下げるので経済
的に劣るという大きな問題点があつた。
However, in any of the above-mentioned conventional solar thermal power generation devices, the high temperature water pipe 3 is insulated from the heat collected by the heat collectors 30, 32 or the linear heat collection pipes 31.
3, they are collected in one place and provided for power generation.
In addition, in order to cope with fluctuations in the power generation load, the heat thus collected is stored in an insulated heat storage tank 34 and provided for power generation. Therefore, heat loss during piping and heat storage cannot be ignored, and this causes a major problem in that it lowers the thermal efficiency and operating rate of the plant, making it economically inferior.
この発明は、上記問題点を解決するためになさ
れたもので、太陽光の熱エネルギーを化学エネル
ギーに変換することにより、集熱途中および蓄熱
時の熱損失を原理的に無くすることができる発電
装置を得ることを目的とする。 This invention was made in order to solve the above problems, and by converting the thermal energy of sunlight into chemical energy, it is possible to generate electricity that can theoretically eliminate heat loss during heat collection and heat storage. The purpose is to obtain equipment.
反応物質が液体であり太陽光を受けて分解する
と液体と気体に分解する可逆反応を用い化学的に
集熱する反応型集熱器と、この反応型集熱器から
供給される前記分解により発生した液体と気体と
の反応を利用して熱を発生する熱発生器とからな
る循環型ヒートポンプと、水素吸蔵合金の発熱反
応を利用して冷水を加熱し、前記循環型ヒートポ
ンプの熱発生器からの受熱により水素を発生・放
出し回復過程を行う高温、高圧の蒸気を発生する
ため交互に作動し、それぞれ水素吸蔵合金を用い
た一組の蒸気発生器をもつバツチ型ヒートポンプ
と、前記蒸気発生器で発生した蒸気により駆動さ
れるタービン発電機とを備えたものである。
A reactive heat collector chemically collects heat using a reversible reaction in which the reactant is a liquid and decomposes into liquid and gas when exposed to sunlight, and the heat generated by the decomposition is supplied from this reactive heat collector. A circulating heat pump consists of a heat generator that generates heat by utilizing a reaction between a liquid and a gas, and a heat generator that heats cold water using the exothermic reaction of a hydrogen storage alloy. A batch-type heat pump that operates alternately to generate high-temperature, high-pressure steam that generates and releases hydrogen by receiving heat from the heat pump, and has a set of steam generators each using a hydrogen storage alloy; It is equipped with a turbine generator that is driven by the steam generated by the generator.
この発明においては、液体の反応物質が太陽光
により加熱され分解して液体と気体に分解し、こ
れが受熱側に集められ、触媒のもとで逆反応によ
り発熱する。一方、水素が吸蔵されると金属水素
化物が生成され、このときの反応熱により冷水を
加熱して高温、高圧の蒸気を得る。その後、水素
を十分吸蔵した金属水素化物は、上記有機物等の
分解生成物の逆反応による発熱により加熱され、
水素を放出し、再び水素を吸蔵する動作を一組の
蒸気発生器が交互に行つて、冷水を加熱すること
が可能となる。
In this invention, a liquid reactant is heated by sunlight and decomposed into a liquid and a gas, which are collected on the heat receiving side and generate heat through a reverse reaction under a catalyst. On the other hand, when hydrogen is occluded, metal hydrides are produced, and the heat of reaction at this time heats cold water to produce high-temperature, high-pressure steam. Thereafter, the metal hydride that has sufficiently absorbed hydrogen is heated by the heat generated by the reverse reaction of the decomposition products of the organic substances, etc.
A set of steam generators alternates between releasing hydrogen and storing hydrogen again, making it possible to heat cold water.
第1図a,bはこの発明の一実施例の構成を示
す概略系統図で、第1図aは昼間の運転方式を示
し、第1図bは夜間の運転方式を示す。これらの
図において、第6図と同一符号は同一部分を示
し、1は前記太陽光14を集光し、有機物等の可
逆反応を用い化学的に集熱する反応型集熱器、2
は熱発生器で、両者で循環型ヒートポンプが構成
される。3は蓄熱槽に相当する蓄液槽の全体を示
し、3A,3B,3Cは前記蓄液槽3を構成する
各貯蔵タンクを示す。4は蒸気発生器、6は復水
器、7は回復過程の蒸気発生器で、水素H2を発
生放出し、蒸気発生器4に水素H2を供給する。
蒸気発生器4,7によりバツチ型ヒートポンプが
構成されている。8は分解反応物質配管、9は被
熱分解物質配管、10は高圧蒸気配管、11は低
圧蒸気配管、12は水素ガス配管、13は高温水
配管である。
FIGS. 1a and 1b are schematic system diagrams showing the configuration of an embodiment of the present invention. FIG. 1a shows a daytime driving method, and FIG. 1b shows a nighttime driving method. In these figures, the same reference numerals as in FIG. 6 indicate the same parts, and 1 is a reactive heat collector that collects the sunlight 14 and chemically collects heat using a reversible reaction of organic matter, etc., 2
is a heat generator, and together they form a circulating heat pump. Reference numeral 3 indicates the entire liquid storage tank corresponding to the heat storage tank, and 3A, 3B, and 3C indicate each storage tank that constitutes the liquid storage tank 3. 4 is a steam generator, 6 is a condenser, and 7 is a steam generator in the recovery process, which generates and releases hydrogen H 2 and supplies hydrogen H 2 to the steam generator 4.
The steam generators 4 and 7 constitute a batch type heat pump. 8 is a decomposition reactant pipe, 9 is a thermally decomposed substance pipe, 10 is a high pressure steam pipe, 11 is a low pressure steam pipe, 12 is a hydrogen gas pipe, and 13 is a high temperature water pipe.
このように、この発明の発電装置は第1図aに
示したように、太陽光14を広い面積から集熱す
る循環型ヒートポンプの部分と、水素吸蔵合金の
発熱反応を利用して冷水を加熱し、上記循環型ヒ
ートポンプからの受熱により水素H2を発生、放
出し、回復過程を行う高温、高圧の蒸気を発生す
る一組の蒸気発生器4,7とを備えたバツチ型ヒ
ートポンプにより発電する部分とから構成されて
いる。 As shown in Figure 1a, the power generation device of the present invention heats cold water by utilizing the circulating heat pump part that collects sunlight 14 from a wide area and the exothermic reaction of the hydrogen storage alloy. Electricity is generated by a batch-type heat pump equipped with a set of steam generators 4 and 7 that generate and release hydrogen H 2 by receiving heat from the circulation-type heat pump, and generate high-temperature, high-pressure steam for the recovery process. It is composed of parts.
前者の部分は第2図に示すように、太陽光14
を受けて反応型集熱器1の有機物に中で吸熱反応
が起こり、上記有機物が触媒(例えば金属ニツケ
ル)により分解する。この有機物の一例としてイ
ソプロパノール(CH3)2CHOHの場合にはアセ
トンCH3COCH3と水素H2とに分解する。 The former part is exposed to sunlight 14 as shown in Figure 2.
As a result, an endothermic reaction occurs in the organic matter in the reactive heat collector 1, and the organic matter is decomposed by a catalyst (for example, nickel metal). As an example of this organic substance, isopropanol (CH 3 ) 2 CHOH is decomposed into acetone CH 3 COCH 3 and hydrogen H 2 .
ただし、Qsは前記太陽光14によつて加えら
れる熱量である。 However, Q s is the amount of heat added by the sunlight 14.
これが熱発生器2に送られ、熱発生器2で触媒
(金属ニツケル)により逆反応が起こり、発熱、
加熱する。 This is sent to the heat generator 2, where a reverse reaction occurs with a catalyst (nickel metal), generating heat and
Heat.
この太陽光集熱の循環型ヒートポンプとなる部
分を具体的に示すと第3図の斜視図のようにな
る。なお、第3図において、15は熱交換器であ
る。 The perspective view of FIG. 3 specifically shows the part that becomes the circulating heat pump for solar heat collection. In addition, in FIG. 3, 15 is a heat exchanger.
後者の部分は金属吸蔵合金として金属チタン等
の金属Mが水素H2を吸蔵して金属水素化物MHo
となるときの反応熱によつて発熱する熱量Qを利
用して蒸気を発生させるもので、この具体的構成
を第4図に示す。 The latter part is a metal occlusion alloy in which metal M such as titanium absorbs hydrogen H 2 and forms metal hydride MH o.
Steam is generated using the amount of heat Q generated by the heat of reaction when .
MHo+Q=M+n/2H2
この反応は極めて速く、チタンのような金属を
選ぶことにより、500〜600℃の高温が得られる。
ここで発生した高圧の蒸気は高圧蒸気配管10を
通つてタービン発電機5に送られて発電する。タ
ービン発電機5から出た低圧の蒸気は第1図の低
圧蒸気配管11を通り、復水器6を経て回復過程
にある蒸気発生器7に熱を供給する。この金属水
素化物MHoを用いた各蒸気発生器4,7は第5
図に示すような蒸熱体モジユールが多数個並べら
れ、あたかも原子炉のような構造をもち蒸気を発
生する。 MH o +Q=M+n/2H 2 This reaction is extremely fast, and by choosing a metal such as titanium, high temperatures of 500-600°C can be obtained.
The high pressure steam generated here is sent to the turbine generator 5 through the high pressure steam pipe 10 to generate electricity. The low-pressure steam output from the turbine generator 5 passes through the low-pressure steam pipe 11 shown in FIG. 1, passes through the condenser 6, and supplies heat to the steam generator 7 which is in the recovery process. Each steam generator 4, 7 using this metal hydride MHO is the fifth
As shown in the figure, a large number of steam heating modules are arranged side by side, creating a structure similar to a nuclear reactor and generating steam.
第5図は蒸気発生器4,7の形状を示す側断面
図で、第1図と同一符号は同一部分を示し、16
は発熱体で、水素ガスH2を吸蔵して発熱する金
属Mが入つている。17は前記発熱体16で発生
した熱により加熱される冷水で、多数の発熱体1
6が浸漬されている。18は前記発熱体16に水
素ガスH2を供給、回収するための水素導入管、
19は前記冷水17を均一に流すための整流板、
20は蒸気溜、21は前記冷水17の取出口、2
2は前記多数の発熱体16や水素導入管18を設
置したり、交換したりする場合の着脱可能な上
板、23は前記冷水17の水面、24は前記冷水
17を収容する蒸気発生器容器、25は前記蒸気
発生器容器24の外周を覆う断熱壁、26は給水
バルブである。 FIG. 5 is a side sectional view showing the shape of the steam generators 4 and 7, where the same reference numerals as in FIG. 1 indicate the same parts, and 16
is a heating element and contains a metal M that absorbs hydrogen gas H 2 and generates heat. Reference numeral 17 denotes cold water that is heated by the heat generated by the heating element 16, and includes a large number of heating elements 1.
6 is immersed. 18 is a hydrogen introduction pipe for supplying and recovering hydrogen gas H 2 to the heating element 16;
19 is a current plate for uniformly flowing the cold water 17;
20 is a steam reservoir, 21 is an outlet for the cold water 17, 2
2 is a removable upper plate for installing or replacing the large number of heating elements 16 and hydrogen introduction pipes 18; 23 is the water surface of the cold water 17; 24 is a steam generator container that accommodates the cold water 17; , 25 is a heat insulating wall covering the outer periphery of the steam generator container 24, and 26 is a water supply valve.
金属Mは水素H2を吸い飽和すると、もはや吸
わなくなり発熱しなくなるので、水素H2を放出
させる逆の回復過程が必要である。 Once the metal M absorbs hydrogen H 2 and becomes saturated, it no longer absorbs hydrogen H 2 and generates no heat, so a reverse recovery process is required to release hydrogen H 2 .
M+n/2H2=MHo+Q
これには、上記の反応式からわかるように、等
量の熱が必要である。ただし、温度は低くともよ
い。このために、熱発生器2から不足の熱を補給
し、蒸気発生器7が吸蔵していた水素H2を放出
させる。この水素H2はポンプによりただちに運
転中の蒸気発生器4に送られる。 M+n/2H 2 =MH o +Q This requires an equal amount of heat, as seen from the reaction equation above. However, the temperature may be low. For this purpose, the insufficient heat is supplied from the heat generator 2, and the hydrogen H 2 stored in the steam generator 7 is released. This hydrogen H 2 is immediately sent by a pump to the steam generator 4 in operation.
このような運転中の蒸気発生器4と回復過程の
蒸気発生器7とが一組となり、この数対の蒸気発
生器4,7が発電装置を構成することにより、連
続運転が可能となる。 The steam generator 4 in operation and the steam generator 7 in the recovery process form a set, and the several pairs of steam generators 4 and 7 constitute a power generation device, thereby enabling continuous operation.
また、集熱部において、第1図に示すように、
熱発生器2の前段階にそれぞれの反応物質を個別
に蓄える貯蔵タンク3A,3B,3Cを設けるこ
とにより、太陽光14の日射の変動を吸収するこ
とができると同時に第1図bに示すような夜間運
転も可能である。 In addition, in the heat collecting part, as shown in Figure 1,
By providing storage tanks 3A, 3B, and 3C for storing each reactant separately before the heat generator 2, it is possible to absorb fluctuations in the solar radiation of the sunlight 14, and at the same time, as shown in FIG. 1b, It is also possible to drive at night.
このように、この発明の発電装置は、従来の装
置の問題点を解決したのみならず、次のような特
徴をもつ。 As described above, the power generation device of the present invention not only solves the problems of conventional devices, but also has the following features.
1 直達日射量のみならず、散乱日射量も含めた
全天日射量を利用することができる。1. It is possible to utilize not only direct solar radiation but also total solar radiation, including scattered solar radiation.
2 固定集光型の比較的安価な集熱器でよい。2. A relatively inexpensive fixed condensing type heat collector may be sufficient.
3 反応型集熱器であるので、途中配管での損失
はない。3. Since it is a reactive heat collector, there is no loss in intermediate piping.
4 化学反応を用いるので、蓄熱は容易で、かつ
損失はない。4. Because it uses a chemical reaction, heat storage is easy and there is no loss.
5 集熱部の反応物質は石油生成物(インプロパ
ノール)のような有機物を利用することがで
き、安価である。5. An organic substance such as a petroleum product (impropanol) can be used as the reactant in the heat collecting section and is inexpensive.
6 蒸気発生器の化学ヒートポンプとして金属水
素化反応を用いているので反応が極めて速い。
しかも水素の出入れのみの運転で、機械的可動
部分がない。6. The chemical heat pump of the steam generator uses a metal hydrogenation reaction, so the reaction is extremely fast.
Moreover, it only operates to take in and out hydrogen, and there are no mechanically moving parts.
7 金属チタンのような金属を水素化物として選
択することにより500℃〜600℃の高温を得るこ
とができ、プラントの効率を向上させることが
できる。7. By selecting metals such as metallic titanium as hydrides, high temperatures of 500°C to 600°C can be obtained and the efficiency of the plant can be improved.
8 数対の蒸気発生器を用いることにより、プラ
ントの連続運転が可能である。8 By using several pairs of steam generators, continuous operation of the plant is possible.
9 数対の蒸気発生器をサイクリツクに運転する
ことにより、比較的高価な金属水素化物の量を
減らすことができ、プラントの建設費を押し上
げることはない。9. By operating several pairs of steam generators cyclically, the amount of relatively expensive metal hydride can be reduced without increasing the cost of building the plant.
10 完全な閉サイクル系であるので、化学的な公
害問題はない。10 Since it is a completely closed cycle system, there are no chemical pollution problems.
11 化学ヒートポンプを適用しているので、排熱
も十分利用しており、熱公害の問題もない。11 Since a chemical heat pump is used, exhaust heat is fully utilized and there is no problem of thermal pollution.
以上説明したように、反応物質が液体であり太
陽光を受けて分解すると液体と気体に分解する可
逆反応を用い化学的に集熱する反応型集熱器と、
この反応型集熱器から供給される前記分解により
発生した液体と気体との反応を利用して熱を発生
する熱発生器とからなる循環型ヒートポンプと、
水素吸蔵合金の発熱反応を利用して冷水を加熱
し、前記循環型ヒートポンプの熱発生器からの受
熱により水素を発生・放出し回復過程を行う高
温、高圧の蒸気を発生するため交互に作動し、そ
れぞれ水素吸蔵合金を用いた一組の蒸気発生器を
もつバツチ型ヒートポンプと、前記蒸気発生器で
発生した蒸気により駆動されるタービン発電機と
を備えたものであるので、反応物質が太陽熱を受
けて分解すると液体と気体とに分解するので、熱
伝達が極めて良好であり、集熱過程時の熱損失を
なくし、ヒートポンプ作用により高温の蒸気を得
ることが可能となり、しかも一組の蒸気発生器を
交互に動作させるため連続した蒸気供給が可能で
あり、したがつてプラントの稼動率の飛躍的向上
と、高効率が実現できる等の利点を有する。
As explained above, a reactive heat collector chemically collects heat using a reversible reaction in which the reactant is a liquid and decomposes into liquid and gas when exposed to sunlight.
a circulating heat pump comprising a heat generator that generates heat by utilizing the reaction between the liquid generated by the decomposition and the gas supplied from the reactive heat collector;
It heats cold water using the exothermic reaction of the hydrogen storage alloy, generates and releases hydrogen by receiving heat from the heat generator of the circulating heat pump, and operates alternately to generate high-temperature, high-pressure steam that performs the recovery process. , a batch-type heat pump with a set of steam generators each using a hydrogen storage alloy, and a turbine generator driven by the steam generated by the steam generator, so that the reactant can absorb solar heat. Since it decomposes into liquid and gas when it is decomposed, heat transfer is extremely good, eliminating heat loss during the heat collection process, and making it possible to obtain high-temperature steam through heat pump action. Since the steam generators are operated alternately, it is possible to supply steam continuously, which has the advantage of dramatically increasing the plant's operating rate and achieving high efficiency.
第1図a,bはこの発明の一実施例を示す概略
系統図で、第1図aは昼間運転方式を示す図、第
1図bは夜間運転方式を示す図、第2図は集熱部
のヒートポンプの原理を示す図、第3図は集熱部
を具体的に示した斜視図、第4図は蒸気発生部の
金属水素化物によつて蒸気が発生する場合を示す
原理図、第5図は金属水素化物を用いた蒸気発生
器を示す側断面図、第6図a〜cは従来の太陽熱
発電装置の各種の例を示すもので、第6図aは側
面図、第6図b,cは斜視図である。
図中、1は反応型集熱器、2は熱発生器、3は
蓄液槽、3A,3B,3Cは貯蔵タンク、4,7
は蒸気発生器、5はタービン発電機、6は復水
器、8は分解反応物質配管、9は被熱分解物質配
管、10は高圧蒸気配管、11は低圧蒸気配管、
12は水素ガス配管、13は高温水配管、14は
太陽光、17は冷水である。
Figures 1a and 1b are schematic system diagrams showing an embodiment of the present invention. Figure 1a is a diagram showing a daytime operation system, Figure 1b is a diagram showing a nighttime operation system, and Figure 2 is a diagram showing a heat collection system. Fig. 3 is a perspective view specifically showing the heat collecting part, Fig. 4 is a principle diagram showing the case where steam is generated by metal hydride in the steam generating part, Fig. Figure 5 is a side sectional view showing a steam generator using metal hydride, Figures 6 a to c show various examples of conventional solar thermal power generation devices, Figure 6 a is a side view, Figure 6 b and c are perspective views. In the figure, 1 is a reactive heat collector, 2 is a heat generator, 3 is a liquid storage tank, 3A, 3B, 3C are storage tanks, 4, 7
is a steam generator, 5 is a turbine generator, 6 is a condenser, 8 is a decomposition reactant pipe, 9 is a thermally decomposed substance pipe, 10 is a high pressure steam pipe, 11 is a low pressure steam pipe,
12 is a hydrogen gas pipe, 13 is a high temperature water pipe, 14 is sunlight, and 17 is cold water.
Claims (1)
ると液体と気体に分解する可逆反応を用い化学的
に集熱する反応型集熱器と、この反応型集熱器か
ら供給される前記分解により発生した液体と基体
との反応を利用して熱を発生する熱発生器とから
なる循環型ヒートポンプと、水素吸蔵合金の発熱
反応を利用して冷水を加熱し、前記循環型ヒート
ポンプの熱発生器からの受熱により水素を発生・
放出し回復過程を行う高温、高圧の蒸気を発生す
るため交互に作動しそれぞれ水素吸蔵合金を用い
た一組の蒸気発生器をもつバツチ型ヒートポンプ
と、前記蒸気発生器で発生した蒸気により駆動さ
れるタービン発電機とを備えたことを特徴とする
発電装置。1. A reactive heat collector that chemically collects heat using a reversible reaction in which the reactant is a liquid and decomposes into liquid and gas when exposed to sunlight, and the decomposition that is supplied from this reactive heat collector A circulating heat pump consisting of a heat generator that generates heat by using the reaction between the generated liquid and a substrate, and a heat generator of the circulating heat pump that heats cold water using the exothermic reaction of a hydrogen storage alloy. Generates hydrogen by receiving heat from
A batch-type heat pump has a set of steam generators, each using a hydrogen storage alloy, which operates alternately to generate high-temperature, high-pressure steam for the release and recovery process; What is claimed is: 1. A power generation device comprising: a turbine generator;
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62077115A JPS63243463A (en) | 1987-03-30 | 1987-03-30 | Electric power generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62077115A JPS63243463A (en) | 1987-03-30 | 1987-03-30 | Electric power generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63243463A JPS63243463A (en) | 1988-10-11 |
| JPH0530995B2 true JPH0530995B2 (en) | 1993-05-11 |
Family
ID=13624787
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62077115A Granted JPS63243463A (en) | 1987-03-30 | 1987-03-30 | Electric power generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63243463A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4777452B2 (en) * | 2009-08-24 | 2011-09-21 | 三井造船株式会社 | Sunlight collection system |
| JP5308275B2 (en) * | 2009-08-24 | 2013-10-09 | 国立大学法人東京工業大学 | Sunlight collection system |
| EP2470788A4 (en) * | 2009-08-27 | 2017-04-05 | McAlister Technologies, LLC | Increasing the efficiency of supplemented ocean thermal energy conversion (sotec) systems |
| JP5404374B2 (en) * | 2009-12-24 | 2014-01-29 | 三菱重工業株式会社 | Solar receiver and solar condensing heat receiving system |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5429311A (en) * | 1977-08-10 | 1979-03-05 | Tokyo Shibaura Electric Co | Method of making ceramic sintered body |
| JPS5554394A (en) * | 1978-10-18 | 1980-04-21 | Mitsubishi Heavy Ind Ltd | Energy storage equipment |
-
1987
- 1987-03-30 JP JP62077115A patent/JPS63243463A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63243463A (en) | 1988-10-11 |
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