JPS58129193A - Heat accumulating member - Google Patents
Heat accumulating memberInfo
- Publication number
- JPS58129193A JPS58129193A JP57011133A JP1113382A JPS58129193A JP S58129193 A JPS58129193 A JP S58129193A JP 57011133 A JP57011133 A JP 57011133A JP 1113382 A JP1113382 A JP 1113382A JP S58129193 A JPS58129193 A JP S58129193A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- heat storage
- methanol
- heat accumulating
- filled
- 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
- 239000002775 capsule Substances 0.000 claims abstract description 15
- 229910017053 inorganic salt Inorganic materials 0.000 claims abstract description 3
- 238000005338 heat storage Methods 0.000 claims description 43
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims 1
- 229910052802 copper Inorganic materials 0.000 claims 1
- 239000010949 copper Substances 0.000 claims 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 49
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 abstract description 11
- 229910001628 calcium chloride Inorganic materials 0.000 abstract description 11
- 239000001110 calcium chloride Substances 0.000 abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 10
- 238000010438 heat treatment Methods 0.000 abstract description 4
- 238000001179 sorption measurement Methods 0.000 abstract description 2
- 238000009825 accumulation Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 150000003839 salts Chemical class 0.000 description 21
- 239000007789 gas Substances 0.000 description 8
- 239000011232 storage material Substances 0.000 description 6
- 239000002156 adsorbate Substances 0.000 description 3
- 239000003463 adsorbent Substances 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 241000270708 Testudinidae Species 0.000 description 1
- -1 calcium nonachloride Chemical compound 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/003—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using thermochemical reactions
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は熱エネルギーO回収、有用に有効な蓄熱体に関
し、特に蓄熱材の充填構造を改良したものである。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a heat storage material that is useful for recovering thermal energy O, and particularly relates to an improved filling structure of the heat storage material.
従来、蓄熱装置の蓄熱材としては水1石、無機塩類尋が
一般に利用されているが、水1石などを蓄熱材として用
いる一熱利用型の蓄熱装置においては、熱エネルギー保
存時における熱の放散を避ける丸め断熱する必畳がTo
9、長時間に凰りて熱エネルギーを蓄熱することは困−
である。Conventionally, one stone of water and inorganic salts are generally used as the heat storage material for heat storage devices, but in one-heat type heat storage devices that use one stone of water as the heat storage material, the amount of heat during storage of thermal energy is To avoid radiation, it is necessary to round and insulate the mat.
9. It is difficult to store thermal energy for a long time.
It is.
一方、fJまたは蒸気を吸着して、そのM合エネルイー
により発熱あるいは吸熱する無機塩類による蓄熱材の熱
エネルイーの貯蔵は、無機塩類と、吸着質のガスまたは
蒸″気との接at遁断することにより、熱エネルギーを
半永久的に保存することができるという利点がある。On the other hand, storage of thermal energy in a heat storage material by inorganic salts that adsorb fJ or vapor and generate heat or absorb heat due to the combined energy of the inorganic salts is achieved by disconnecting the inorganic salts from the adsorbate gas or vapor. This has the advantage that thermal energy can be stored semi-permanently.
しかしながら無機塩類は熱伝導率が低いため、蓄熱装置
への入熱時あるいは蓄熱装置からの出熱時における熱の
移動速度が遅く、熱エネル←を効率嵐く利用することが
できない、また無機塩類は熱交換手段を儂え友蓄熱槽内
に充填して使用されるが、充填量が多くなると吸着質の
Iスヤ蒸気が無機塩類内を拡散する速度が遅くなると共
に、無機塩類との接触面積が少なくなって、充填され九
無機塩類が有効に利用されず、蓄熱効率が低下するなど
の欠点があつた。However, since inorganic salts have low thermal conductivity, the speed of heat transfer when heat is input to or output from the heat storage device is slow, and thermal energy cannot be used efficiently. is used by filling a thermal storage tank with a heat exchanger, but as the amount of filling increases, the speed at which adsorbent I-Sya vapor diffuses within the inorganic salts slows down, and the contact area with the inorganic salts decreases. There were drawbacks such as the inorganic salts being filled were not being utilized effectively and the heat storage efficiency was decreasing.
本発明は上記従来の欠点に鑑みなされえもので、金mW
のメック、からなるカプセル内に、無機塩類を充填して
、無機塩類内の熱の移動速度を萬めると共に、吸着質の
ガス中蒸気の拡敏速f#を高めて、熱の出入りを均一に
且つ速やかに行なりて蓄熱効率を向上させた蓄熱体を提
供することを目的とするものである。The present invention has been made in view of the above-mentioned conventional drawbacks, and is based on gold mW.
Inorganic salts are filled into a capsule made of MEC to increase the transfer speed of heat within the inorganic salts, and to increase the diffusion speed f# of vapor in the adsorbate gas to uniformly transfer heat in and out. It is an object of the present invention to provide a heat storage body whose heat storage efficiency can be improved quickly and efficiently.
本発明の蓄熱体は金属製のメック、からなる力!セル内
に無機塩類を充填したものである。The heat storage body of the present invention is made of metal MEC! The cell is filled with inorganic salts.
前記カプセルを形成する金属製のメ、り、とじては、例
えば鋼、アルミニウム、ステンレススチール等、熱伝導
率の大きいものが挙げられるが、特に鋼およびステンレ
ススチールカ最モ通している。また金属製メッ7.の大
きさは、無機塩類がメック、の網目を通過しないような
メツシュを選択する必要があるが、メック、の値が大き
く細かすぎると、吸着質のガス中蒸気O過過を妨げるこ
とになるため100メツシ。The metal mesh forming the capsule may be made of materials with high thermal conductivity such as steel, aluminum, and stainless steel, but steel and stainless steel are particularly preferred. Also, metal mesh 7. It is necessary to select a mesh that does not allow inorganic salts to pass through the mesh of MEC, but if the value of MEC is too large and too fine, it will prevent the vapor O from passing through the adsorbate gas. 100 metsushi.
以下が適轟である。ま九カグ竜ル0大亀さ扛、カプセル
中に充填した無機塩類内ta着質のガス中1気が拡散し
て無機塩!l1lK@着する際の妨げとならず、しかも
充填する無機塩類の量と、これを支持するカプセルの機
械的強度とから決められる。[に力!セルの形状は、方
形あるいは球形など偏れでも良い。The following is Suitoku. The inorganic salts are dispersed in the gas deposited in the inorganic salts filled in the capsule! l1lK@ does not interfere with the loading and is determined based on the amount of inorganic salts to be filled and the mechanical strength of the capsule that supports it. [Power to the power! The shape of the cell may be irregular, such as rectangular or spherical.
力f(ル内に蓄熱材として充填される無機塩類としては
、水蒸気やメタノール蒸気など吸着質のガスや蒸気¥t
eL着して発熱または吸熱する塩化マダネシウム(Mg
(’42人塩化カルシウム(CaCjz)等が挙げられ
る。またこれら無機塩類O選択にあ九りては、それぞれ
の熱利用系に適する温度で相変異点を持ち、そのliの
熱量が火車いもの會選択するのが好ましい。The force f (inorganic salts filled in the chamber as a heat storage material include adsorbent gases and steam such as water vapor and methanol vapor)
Madanesium chloride (Mg
('42 Calcium chloride (CaCjz), etc.) In addition, when selecting these inorganic salts, O has a phase change point at a temperature suitable for each heat utilization system, and the calorific value of Li It is preferable to choose the meeting.
このように構成された蓄熱体は金属製のメ。The heat storage body configured in this way is made of metal.
シ、で形成された力!セル内に無機塩類會充填しである
ので、熱伝導性に優れ九カグセルによ)、無機塩類との
熱交換が促進される。*にカブセル関およびカプセルを
形成する金属製メVシ、の網目間がガスや蒸気の通路と
なる丸め拡散が速く、無機塩類の全体に亘りてむもなく
均一に、且つ迅速にガス中蒸気の吸着、脱離作用が行な
われる。The power formed by shi! Since the cells are filled with inorganic salts, they have excellent thermal conductivity and promote heat exchange with the inorganic salts. *The mesh of the metal shell that forms the capsule and the capsule is rounded and forms a passageway for gas and steam, and diffusion is fast, allowing the vapor in the gas to flow uniformly and quickly over the entire inorganic salt. adsorption and desorption effects are carried out.
第1図および第2図は本尭明〇一実施例を示すもので蓄
熱体1はステンレススチールll050メツシ、からな
る1辺20■の立方体力!セル2内に塩化カルシウム1
を充填しえ40である。Figures 1 and 2 show the embodiment of the present invention, in which the heat storage body 1 is a cube of 20 cm on each side made of stainless steel 11050 mesh! Calcium chloride 1 in cell 2
40.
この蓄熱体1を第2図に示す蓄熱装置の蓄熱槽4内に塩
化カルシウム1の総量が1−となるように充填する。前
記蓄熱装置は、蓄熱体1を充填し、外部から引込まれ友
伝熱管1を儂え九番熱槽4と、外部から引込まれ九加熱
管6を備え、内部にメタノール1を貯ええ貯蔵槽1と、
これら両槽間に般けられ、凝縮器tを中間に取付けた連
通管1−とから構成されて込る。This heat storage body 1 is filled into a heat storage tank 4 of a heat storage device shown in FIG. 2 so that the total amount of calcium chloride 1 becomes 1-. The heat storage device includes a heat storage tank 4 filled with a heat storage body 1, which is drawn in from the outside and uses a heat exchanger tube 1, and a heat tank 4 which is drawn in from the outside and stores methanol 1 therein. 1 and
It consists of a communicating pipe 1- which extends between these two tanks and has a condenser t installed in the middle.
先ず発熱作用について説−すると、加熱管Iに30℃の
熱媒体を流通させると、貯蔵槽1内Oメタノール1が加
熱されて蒸発し、このメタノール蒸気は連通管10を通
って蓄熱槽4に供給される。供給され九メタノール蒸気
は、蓄熱体1−間を通ると共に、カプセル2の網目間を
過って内部に拡散し、充填し九塩化カル7ウムat>*
面に吸着して発熱する。この熱を20℃O水を1001
00d1で流通させた伝熱管5に伝達して熱交換を行な
い、水を加熱した。この場合、水O加熱温度の峠時変化
を調べたところ、第3EOグI)7に曲線aで示すよう
になった。First, to explain the exothermic effect, when a 30°C heat medium is passed through the heating tube I, the methanol 1 in the storage tank 1 is heated and evaporated, and this methanol vapor passes through the communication pipe 10 and enters the heat storage tank 4. Supplied. The supplied methanol vapor passes through the heat storage body 1 and diffuses into the interior of the capsule 2, filling it with calcium nonachloride at>*
It sticks to surfaces and generates heat. This heat is 20℃O water is 1001
The water was transferred to the heat exchanger tube 5 which was circulated at 00d1 to perform heat exchange and heat the water. In this case, when we investigated the change in the water O heating temperature during the mountain pass, we found that it came to be shown by curve a in the third EO group I)7.
次に蓄熱時における作用を説明すると、伝熱管1に12
0℃の熱媒体を流通して蓄熱体1を加熱す為と、蓄熱体
1内の塩化カルシウム3が加熱されて、吸着しているメ
タノール1が蒸発・脱離する。脱離し九メタノール蒸気
は連通管1#管通り凝at器9で#縮されて、再び貯蔵
槽aK貯められる。Next, to explain the action during heat storage, 12
In order to heat the heat storage body 1 by circulating a heat medium at 0° C., the calcium chloride 3 in the heat storage body 1 is heated, and the adsorbed methanol 1 is evaporated and desorbed. The desorbed methanol vapor is condensed in the condenser 9 through the communication pipe 1 and stored in the storage tank aK again.
ξO場会、塩化カルシウム1に吸着しているメタノール
残留量(メ″−“)菖す/塩化カルシウム+メタノール
の重さ)の蓄熱開始後の経時変゛化it第4図のグラフ
に−@aで示すようKlkり九。In the case of ξO, the graph in Figure 4 shows the change over time of the residual amount of methanol adsorbed on calcium chloride (weight of Calcium chloride + methanol) after the start of heat storage. Klk Riku as shown in a.
壇九本発明と比較する九めに、総量l神の塩化カルシウ
ム1をカプセル2に充填せずに、その着ま蓄熱槽4内に
充填した従来0蓄熱装鐙を用い、上記実施例と同様に発
熱時0水oii*変化を調べて、七〇M来を第3図のダ
27に麹纏すで示した。また蓄熱時のメタノール残留量
についても同様に調べたところIII!41iCのグラ
フに曲41bで示すようになりた。As a ninth comparison with the present invention, a conventional heat storage stirrup in which the total amount of calcium chloride 1 was not filled into the capsule 2 but into the heat storage tank 4 was used, and the same as in the above embodiment was used. The change in 0 water oii* during heat generation was investigated, and the temperature after 70M was shown in Da 27 in Figure 3 with koji matte. We also investigated the residual amount of methanol during heat storage and found that it was III! The graph of 41iC now shows the song 41b.
以上説明し九如く本発明に係わゐ蓄熱体によれば、金0
11のメッシ、からなるカフ”−4Eル内に無機塩類を
充填して、無機塩類内Ct*O移動遭fを高めると共に
、吸着質のガス中蒸気の拡散速度を嶌めて熱の山人参を
拘−に且っ速かに行なりて蓄熱効率を向上させることが
でき、しがも蓄熱体との熱交換を行なう伝熱管轄金属製
カグセルがフィン作用をなす丸め、電価なフィン付亀管
を用いずにストレート管を利用で龜る〇で装置−安価と
なるなど原著な効果を有すゐもO″fToる。As explained above, according to the heat storage body according to the present invention, there is no gold.
The cuff consisting of 11 meshes is filled with inorganic salts to increase the Ct*O movement within the inorganic salts, and also to reduce the diffusion rate of vapor in the adsorbent gas, thereby reducing heat. The heat storage efficiency can be improved by quickly and efficiently, and the heat transfer metal cag cells that perform heat exchange with the heat storage body are rounded and have electric fins that act as fins. Using a straight tube instead of a tortoise tube has significant advantages, such as making the device faster and cheaper.
41ElliiO簡単な説明
@1図は本発明の一実施例による蓄熱体を一部砿断して
示す斜視図、第2図は11図の蓄熱体を用いた蓄熱装置
の断面図、第3図は発熱時における水の出口装置の軽時
変化を示すグラフ、llll4Eは蓄熱時におけるメタ
ノール残留量の経時費化を示すグラフである。41ElliiO Brief explanation@1 Figure 1 is a partially cutaway perspective view of a heat storage body according to an embodiment of the present invention, Figure 2 is a sectional view of a heat storage device using the heat storage body shown in Figure 11, and Figure 3 is a cross-sectional view of a heat storage device using the heat storage body shown in Figure 11. A graph showing changes in the water outlet device over time during heat generation, llll4E is a graph showing changes in the amount of methanol remaining over time during heat storage.
1−・蓄熱体、2・・・力!セル、1・・・塩化カルシ
ウム、4・・・蓄熱槽、5・・・伝熱管、6・・・加熱
管、r・−メタノール、8・・・貯蔵槽、9・・・凝縮
器、10・・・連通管。1- Heat storage body, 2... Power! Cell, 1... Calcium chloride, 4... Heat storage tank, 5... Heat exchanger tube, 6... Heating tube, r-methanol, 8... Storage tank, 9... Condenser, 10 ...Communication pipe.
出願人代理人 弁理士 鈴 江 武 彦子Q羽口東蔓
ρApplicant's agent Patent attorney Hikoko Suzue Takeshi Q. Higashi Tsune tuyere ρ
Claims (2)
ガスまたは蒸気を吸着して、発熱あるいは吸熱する無機
塩類を充填したこと1−特徴とする蓄熱体。(1) In the force f-, which consists of metal metal,
1. A heat storage body characterized by being filled with an inorganic salt that adsorbs gas or vapor and generates heat or absorbs heat.
チールなどの熱伝導率の大暑い金属製のメ、シュで形成
されていることを特徴とする特許請求の範囲第1項記載
の蓄熱体。(2) The heat storage body according to claim 1, wherein the capsule is formed of a metal mesh having high thermal conductivity such as copper, aluminum, or stainless steel.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57011133A JPS58129193A (en) | 1982-01-27 | 1982-01-27 | Heat accumulating member |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57011133A JPS58129193A (en) | 1982-01-27 | 1982-01-27 | Heat accumulating member |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58129193A true JPS58129193A (en) | 1983-08-02 |
Family
ID=11769515
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57011133A Pending JPS58129193A (en) | 1982-01-27 | 1982-01-27 | Heat accumulating member |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58129193A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010248374A (en) * | 2009-04-15 | 2010-11-04 | Denso Corp | Thermal storage agent-metal structure and manufacturing method thereof |
JP2011196661A (en) * | 2010-03-23 | 2011-10-06 | Toyota Central R&D Labs Inc | Heat accumulator |
FR3003937A1 (en) * | 2013-03-29 | 2014-10-03 | Hevatech | THERMO-CHEMICAL ENERGY STORAGE DEVICE COMPRISING A DRYING NETWORK AND METHOD OF OPERATING THE DEVICE |
WO2015099063A1 (en) * | 2013-12-26 | 2015-07-02 | カルソニックカンセイ株式会社 | Adsorption-type heat exchanger |
WO2018066407A1 (en) * | 2016-10-06 | 2018-04-12 | 株式会社豊田自動織機 | Chemical heat storage device |
-
1982
- 1982-01-27 JP JP57011133A patent/JPS58129193A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010248374A (en) * | 2009-04-15 | 2010-11-04 | Denso Corp | Thermal storage agent-metal structure and manufacturing method thereof |
JP2011196661A (en) * | 2010-03-23 | 2011-10-06 | Toyota Central R&D Labs Inc | Heat accumulator |
FR3003937A1 (en) * | 2013-03-29 | 2014-10-03 | Hevatech | THERMO-CHEMICAL ENERGY STORAGE DEVICE COMPRISING A DRYING NETWORK AND METHOD OF OPERATING THE DEVICE |
WO2015099063A1 (en) * | 2013-12-26 | 2015-07-02 | カルソニックカンセイ株式会社 | Adsorption-type heat exchanger |
WO2018066407A1 (en) * | 2016-10-06 | 2018-04-12 | 株式会社豊田自動織機 | Chemical heat storage device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Pons et al. | Design of an experimental solar-powered, solid-adsorption ice maker | |
Xu et al. | A zeolite 13X/magnesium sulfate–water sorption thermal energy storage device for domestic heating | |
Anbarasu et al. | Thermal modeling of LmNi4. 91Sn0. 15 based solid state hydrogen storage device with embedded cooling tubes | |
US4329407A (en) | Electrochemical storage battery | |
CN105651091B (en) | Conduct heat enhanced chemical regenerative apparatus and the hold over system using the regenerative apparatus | |
JP2017525933A (en) | Solar energy water heating auxiliary heat storage device and power plant boiler solar energy water heating supply system formed from solar energy water heating auxiliary heat storage device | |
JP2005024231A (en) | Thermal storage heat pump system | |
JPS58129193A (en) | Heat accumulating member | |
Parashar et al. | Experimental study on charging and discharging characteristics of copper finned metal hydride reactor for stationary hydrogen storage applications | |
US3504494A (en) | Intermittent power source | |
US20160206989A1 (en) | Regeneration of a hydrogen impurity trap using the heat exiting a hydride tank | |
CN108800353A (en) | A kind of air dehumidifier using solution | |
JP2002031426A (en) | Heat storage device | |
US3065609A (en) | Absorption refrigeration system | |
CN209197547U (en) | A kind of full liquid type steam accumulator | |
CN109297339A (en) | A kind of flooded steam heat accumulator and preparation method of composite phase change heat storage material | |
CN114307619B (en) | Novel device and method for capturing carbon dioxide in circularly regenerated flue gas | |
CN210135815U (en) | Liquid-solid immersion type adsorption heat storage system | |
JPS5848480Y2 (en) | Hydrogen storage device using metal hydride | |
CN114935273A (en) | A multi-stage phase change ball heat storage device | |
JPS61143689A (en) | Heat pipe | |
JPS5890A (en) | Structure of heat exchanger utilizing metal hydride | |
Dadda et al. | Numerical simulation of fins' effect on the performance of a metal hydride reactor | |
JP3046975B2 (en) | Hydrogen storage container | |
JP6365016B2 (en) | HEAT PUMP AND CRYSTAL GENERATION METHOD |