JPS62162866A - Method of storing cold heat energy - Google Patents

Method of storing cold heat energy

Info

Publication number
JPS62162866A
JPS62162866A JP61004700A JP470086A JPS62162866A JP S62162866 A JPS62162866 A JP S62162866A JP 61004700 A JP61004700 A JP 61004700A JP 470086 A JP470086 A JP 470086A JP S62162866 A JPS62162866 A JP S62162866A
Authority
JP
Japan
Prior art keywords
medium
gas
liquid
low
cold heat
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
Application number
JP61004700A
Other languages
Japanese (ja)
Inventor
江部 正紀
冨田 勉
弘 吉田
古澤 義夫
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chubu Electric Power Co Inc
Kawasaki Heavy Industries Ltd
Original Assignee
Chubu Electric Power Co Inc
Kawasaki Heavy Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Chubu Electric Power Co Inc, Kawasaki Heavy Industries Ltd filed Critical Chubu Electric Power Co Inc
Priority to JP61004700A priority Critical patent/JPS62162866A/en
Publication of JPS62162866A publication Critical patent/JPS62162866A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • 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
    • Y02E60/14Thermal energy storage

Landscapes

  • Air Conditioning Control Device (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、LNGなどの低温液化ガスの冷熱を貯蔵する
方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for storing cold energy of low-temperature liquefied gas such as LNG.

〔発明の背景〕[Background of the invention]

現在国内には、建設中のものを含めていくつかのLNG
などの受入基地があり、そのLNGなどの低温液化ガス
の冷熱は、冷熱発電や)fJ凍倉庫などに利用されてい
る。
There are currently several LNG plants in Japan, including those under construction.
There are receiving terminals such as LNG, and the cold energy of low-temperature liquefied gas such as LNG is used for cold power generation and fJ freezing warehouses.

しかしながら、LNGなどの消費性は、季節2時間帯に
よって変動するために、またこの冷熱は、貯蔵が困難な
ことから、ベースロードの約30%程度しか利用されて
おらず、他の冷熱は投棄されているのが現状である。従
って、大量の冷熱エネルギーが上述の如く投棄せざるを
得ない状態にあり、LNGなどを多量に使用するガス業
界、電力業界においては、冷熱エネルギーの有効利用の
要望が非常に大きい。
However, because the consumption of LNG etc. varies depending on the season and the time of day, and because this cold energy is difficult to store, only about 30% of the base load is used, and other cold energy is dumped. The current situation is that Therefore, a large amount of cold energy has to be discarded as described above, and in the gas industry and electric power industry, which use large amounts of LNG and the like, there is a great demand for effective use of cold energy.

〔発明の目的〕[Purpose of the invention]

本発明は、このような実情に鑑みなされたもので、簡単
な面も合理的手段により従来技術の問題点を解消せしめ
、低温液化ガスから得られる冷熱エネルギーを常温高圧
の液状媒体に担架せしめ、この冷熱を貯蔵し、適宜とり
出して利用し、更に、この利用した後のガス媒体を水な
どの液体を利用してこれに吸収担架させ、この水などの
液体を加熱してずeたガス媒体を循環貯蔵することによ
り、冷熱を投棄することなく有効に利用及び貯蔵しうる
方法を提供せんとするものである。
The present invention has been made in view of the above circumstances, and solves the problems of the prior art by simple and rational means, by transferring cold energy obtained from low-temperature liquefied gas to a liquid medium at room temperature and high pressure, This cold energy is stored, taken out and used as appropriate, and the gas medium after this use is absorbed and carried by a liquid such as water, and the liquid such as water is heated to produce gas. It is an object of the present invention to provide a method that can effectively utilize and store cold energy without wasting it by storing the medium in circulation.

〔問題点を解決するための手段〕 従来の問題点を解決する本発明の構成は、LNGなどの
低温液化ガスの冷熱を貯蔵するに際し、アンモニアなど
の液体に溶解するガスを冷熱貯蔵の媒体とし、これらの
媒体のガスを冷熱交換器にて低温?1に化ガスの冷熱で
nl化し、この液化された媒体をポンプなどの手段て昇
圧したのち、海水などを用いた熱交換器て昇温して常温
高圧の液状媒体を得、これを一時的に媒体貯蔵タンクに
貯蔵せしめ、のち、該常温高圧の貯蔵媒体を適宜とり出
し、膨張弁によって低温低圧状態に膨張せしめて冷凍倉
庫などに冷熱を供給利用させ、しかるのち、ガス吸収槽
にて、吸熱によりガス化された媒体を、水などの液体に
溶解せしめ、これを貯蔵した上で、ガス放出槽で減圧下
で、該溶液を加熱することによって、上記と同様のガス
媒体を得、これを上記冷熱交換器に循環送入するととも
に、ガスを放出した液体をポンプで昇圧し、再度ガス吸
収槽に返送するようにしたことを特徴とするものである
[Means for Solving the Problems] The configuration of the present invention that solves the conventional problems is that when storing the cold energy of low-temperature liquefied gas such as LNG, a gas dissolved in a liquid such as ammonia is used as a cold energy storage medium. , these medium gases are cooled to low temperature in a cold heat exchanger? 1, the liquefied medium is converted to nl by the cold heat of the chemical gas, and the pressure of this liquefied medium is increased using a pump or other means, and then the temperature is raised using a heat exchanger using seawater etc. to obtain a liquid medium at room temperature and high pressure. After that, the storage medium at room temperature and high pressure is appropriately taken out and expanded to a low temperature and low pressure state by an expansion valve to supply cold heat to a frozen warehouse etc., and then in a gas absorption tank. A gaseous medium similar to the above is obtained by dissolving the medium gasified by endotherm in a liquid such as water, storing it, and heating the solution under reduced pressure in a gas release tank. The liquid is circulated through the cold heat exchanger, and the liquid from which the gas has been released is pressurized by a pump and then sent back to the gas absorption tank.

〔実施例2〕 (第1図) 第1図に示すせづについて本発明方法の第1実施例を説
明する。この実施例及び以下の実施例について、アンモ
ニア(N[h )と水(H20)を使用する。
[Embodiment 2] (FIG. 1) A first embodiment of the method of the present invention will be described with respect to the stage shown in FIG. For this example and the following examples, ammonia (N[h2) and water (H20) are used.

発地において、ガスホルダー1から供給される常温低圧
のガス状媒体(NHz )を、LNGなどの低温液化ガ
スの冷熱との冷熱交換器2にて熱交換せしめて低温低圧
の液状と化し、この液化された媒体をレシーバ−タンク
3に蓄溜する。蓄溜された液化媒体は、昇圧ポンプ4に
よって昇圧されるとともに、海水などを用いた熱交換w
5で昇温せしめられ、媒体は常温高圧の液状媒体となる
。この液状媒体は常温高圧の状態で、媒体貯蔵タンク6
に一時的に貯蔵せしめられる。この媒体は、負荷側の要
求により適宜とり出され、膨張弁7によって低温低圧状
態に膨張せしめられ、これにより得られた冷熱エネルギ
ーを冷rR倉庫などの負荷8に冷熱を供給利用する。負
荷8において吸熱ガス化され、かつ、コノゴレ・ソサ9
により昇圧された媒体(例えばNlh )を、ガス吸収
槽12において、液体(例えば水)に溶解させ、溶液を
得る。この溶液は、ポンプ13をもつ配管、または、ロ
ーリ−などの輸送手段によってガス放出槽16に送られ
ろ。該溶液は、膨張弁14によって低温低圧化されたガ
ス放出槽16に送給され、溶液はこのガス放出槽16内
で容易に入手しうる海水、大気などで加熱せしめられ、
溶液のガス媒体は水から放出される。発生した常温低圧
のガス(NH,、It□0)は、ガス?y浄化設備20
に送られて水分(H20)を取り除かれ、得られたガス
媒体(Nil、 )は、上記ガスホルダー1に貯溜せし
められ、適宜上記冷熱交換器2に供給され、上述のサイ
クルで循環する。またガス放出槽16でガス媒体を発生
した水などの液体は、昇圧ポンプ17で高圧化され、上
記ガス吸収槽12に供給され、ガス媒体を効率よ(吸収
する。そして、図から明らかなように、ガス媒体を放出
した液体と、ガス媒体を吸収した溶液の顕熱を交換する
熱交換器18を介装せしめ、ガス媒体を吸収した溶液を
冷却し常温高圧状態とする。なお、ガス吸収FfI+2
において、ガスの溶解時に発生する熱は、ヒートボンゴ
などに活用されろ。
At the source, the gaseous medium (NHZ) at room temperature and low pressure supplied from the gas holder 1 is exchanged with the cold heat of low-temperature liquefied gas such as LNG in the cold heat exchanger 2 to become a low-temperature and low-pressure liquid. The liquefied medium is stored in a receiver tank 3. The stored liquefied medium is pressurized by a boost pump 4 and subjected to heat exchange using seawater etc.
The temperature is raised at step 5, and the medium becomes a liquid medium at room temperature and high pressure. This liquid medium is at room temperature and high pressure in the medium storage tank 6.
be temporarily stored. This medium is taken out as required by the load side and expanded to a low temperature and low pressure state by the expansion valve 7, and the resulting cold energy is used to supply cold heat to the load 8 such as a cold rR warehouse. It is endothermically gasified at load 8, and Konogore Sosa 9
The medium (for example, Nlh 2 ) pressurized by the gas absorption tank 12 is dissolved in a liquid (for example, water) to obtain a solution. This solution is sent to the gas release tank 16 by piping with a pump 13 or by means of transportation such as a lorry. The solution is fed by the expansion valve 14 to a low-temperature, low-pressure gas release tank 16, and the solution is heated in the gas release tank 16 with easily available seawater, air, etc.
The gaseous medium of the solution is released from the water. Is the generated room temperature, low pressure gas (NH,, It□0) a gas? y purification equipment 20
The gas medium (Nil, ) obtained by removing moisture (H20) is stored in the gas holder 1, supplied to the cold heat exchanger 2 as appropriate, and circulated in the cycle described above. In addition, liquid such as water that has generated a gas medium in the gas discharge tank 16 is increased in pressure by a booster pump 17, and is supplied to the gas absorption tank 12, where it efficiently absorbs the gas medium. A heat exchanger 18 is installed to exchange sensible heat between the liquid that has released the gas medium and the solution that has absorbed the gas medium, and cools the solution that has absorbed the gas medium to a normal temperature and high pressure state. FfI+2
The heat generated when the gas melts can be used in things like heat bongos.

〔実施例2〕 (第2図) 第2図に示す設備について本発明方法の第2実施例を説
明する。この実施例は、第1実施例におけるガスホルダ
ー1を省略し、ガス放出槽16で発生したガス媒体(N
[+、 )が、そのままガス清浄化設備20を経て冷熱
交換器2に送られるようにしたものである。更に、仮想
線で示すように、上記昇圧ボンゴ17とガス吸収槽12
を結ぶ管路に設けた上記熱交換器18とは別個に、周辺
に残存せる熱媒を利用した熱交換M18aを設けろよう
にしたもので、他は第1実施例の構成と同一であること
から、詳細な説明については省略する。
[Example 2] (Fig. 2) A second example of the method of the present invention will be described using the equipment shown in Fig. 2. In this embodiment, the gas holder 1 in the first embodiment is omitted, and the gas medium (N
[+, ) are sent as they are to the cold heat exchanger 2 via the gas purification equipment 20. Furthermore, as shown by imaginary lines, the pressurizing bongo 17 and the gas absorption tank 12
Separately from the heat exchanger 18 provided in the conduit connecting the two, a heat exchanger M18a using a heat medium remaining in the vicinity is provided, and the other configuration is the same as that of the first embodiment. Therefore, detailed explanation will be omitted.

〔実施例3〕 (第3図) 第3図に示す設備について、本発明方法の第3実施例を
説明する。ガス媒体の液化、昇圧、常温環化、貯蔵、膨
張弁7による低温低圧化、負荷8での冷熱利用の手段は
、第1実施例と同様であるため、この詳細は省略する。
[Example 3] (Fig. 3) A third example of the method of the present invention will be described with respect to the equipment shown in Fig. 3. The means for liquefying the gas medium, pressurizing it, cyclizing it at room temperature, storing it, lowering the temperature and pressure using the expansion valve 7, and utilizing the cold energy in the load 8 are the same as in the first embodiment, so the details thereof will be omitted.

負荷8の吸熱作用によりガス化された媒体(Nth l
は、ガス吸収槽12内に供給され、該ガス吸収槽12内
の液体(例えば水)に溶解し、溶液となる。(この溶液
は例えばNH40[[となる)この溶液はポンプ13に
よって貯槽19に貯蔵される。この貯蔵された溶液は、
膨張弁14により低温低圧化されてガス放出槽16に送
られ、ここで上述のように加熱せしめられて発生したガ
ス(N)l、 、 l!20)!ま、ガス清浄化設備2
0に送られて水分(It20)を取り除かれ、得られた
ガス媒体(Nil、 )は、上記冷熱交換器2に送られ
、あと(ま、上記第1実施例と同様であるのでその詳細
説明は省略する。なお、設計によっては、各実施例にお
いて熱交換器18を省略してもよい。
The medium gasified by the endothermic action of load 8 (Nth l
is supplied into the gas absorption tank 12, dissolved in the liquid (for example, water) in the gas absorption tank 12, and becomes a solution. (This solution becomes, for example, NH40.) This solution is stored in a storage tank 19 by a pump 13. This stored solution is
The gas (N)l, , l! is reduced in temperature and pressure by the expansion valve 14 and sent to the gas release tank 16, where it is heated as described above and generated. 20)! Well, gas purification equipment 2
The gas medium (Nil, ) obtained by removing moisture (It20) is sent to the cold heat exchanger 2, and the rest (well, since it is the same as the first embodiment, a detailed explanation thereof will be given below. Note that depending on the design, the heat exchanger 18 may be omitted in each embodiment.

ガス放出槽16で溶1夜(例えばN1(40旧を加熱し
、媒体をガス化した液体(個人ばI[20)は、ボンゴ
17によって貯槽15に送られ、ここに貯溜せしめられ
る。そして適宜この液体は、昇圧ポンプ21によって高
圧化されて上記ガス吸着槽12に送られ、ガス媒体を吸
収または吸着する。がす吸着槽12て発生する熱は、と
−トポンプなどに利用されろ。
The liquid (individual I [20) obtained by heating the melt overnight (for example, N1 (40 g)) in the gas release tank 16 and gasifying the medium (individual I [20]) is sent to the storage tank 15 by the bongo 17 and stored there. This liquid is increased in pressure by the booster pump 21 and sent to the gas adsorption tank 12, where it absorbs or adsorbs the gas medium.The heat generated in the gas adsorption tank 12 is used for a gas adsorption tank or the like.

〔効  果〕〔effect〕

上述のように本発明によれば、次のような効果が得られ
る。
As described above, according to the present invention, the following effects can be obtained.

(al  LNGなどの低温液化ガスの冷熱により液化
された媒体を、第4図のPi凹曲線示すように、常温高
圧の液状状態で貯蔵し、適宜とり出し使用することがで
き、従来投棄していた冷熱エネルギーは、上述のように
常温高圧の液状媒体として貯蔵しうる。
(al) The medium liquefied by the cold heat of low-temperature liquefied gas such as LNG can be stored in a liquid state at room temperature and high pressure, as shown by the Pi concave curve in Figure 4, and can be taken out and used as needed. The cooled energy can be stored as a liquid medium at room temperature and high pressure, as described above.

(bl  負荷において吸収しガス化された媒体は、液
体に溶解する性質を利用し、このガス媒体を液体に溶解
せしめ、此れを、常温高圧の状態で貯蔵管理し、ガス放
出槽で而も減圧下で加熱し、媒体を再びガス化し循環使
用し得られる。
(bl) Utilizing the property of the gaseous medium absorbed in the load to dissolve in liquid, this gaseous medium is dissolved in liquid, stored and managed at room temperature and high pressure, and then stored in a gas release tank. By heating under reduced pressure, the medium is again gasified and recycled.

【図面の簡単な説明】[Brief explanation of drawings]

図は本発明方法を実施する設備の概略を示すもので、第
1〜3図は夫々概略ンス子ム図、第4図はPi曲線図で
ある。 ■ ガスホルダー、2 冷熱交換器、3 レシーバ−タ
ンク24 ポンプ、5・・熱交換器、6媒体貯蔵タンク
、7 膨張弁、8 負荷、 12  ガス吸収槽、 1
3  ボンゴ、14  膨張弁、 15  ガス媒体を
放出した液体の貯槽、16  ガス放出槽、17界圧ボ
レブ、 18  熱交換器、19  ガス媒体を吸収し
た溶液の貯槽、20  ガス清浄化設備(脱水設備)。
The drawings schematically show the equipment for carrying out the method of the present invention, and Figs. 1 to 3 are schematic diagrams of the system, respectively, and Fig. 4 is a Pi curve diagram. ■ Gas holder, 2 Cold heat exchanger, 3 Receiver tank 24 Pump, 5...Heat exchanger, 6 Medium storage tank, 7 Expansion valve, 8 Load, 12 Gas absorption tank, 1
3 Bongos, 14 Expansion valve, 15 Liquid storage tank from which the gas medium has been released, 16 Gas release tank, 17 Interfacial pressure valve, 18 Heat exchanger, 19 Storage tank for the solution that has absorbed the gas medium, 20 Gas purification equipment (dehydration equipment) ).

Claims (1)

【特許請求の範囲】 〔第1項〕 (a)LNGなどの低温液化ガスの冷熱を貯蔵するに際
し、 (b)アンモニアなどの液体に溶解するガスを冷熱貯蔵
の媒体とし、これらの媒体のガスを冷熱交換器にて低温
液化ガスの冷熱で液化し、 (c)この液化された媒体をポンプなどの手段で昇圧し
たのち、海水などを用いた熱交換器で昇温して常温高圧
の液状媒体を得、これを一時的に媒体貯蔵タンクに貯蔵
せしめ、 (d)のち、該常温高圧の貯蔵媒体を適宜とり出し、膨
張弁によって低温低圧状態に膨張せしめて冷凍倉庫など
に冷熱を供給利用させ、 (e)しかるのち、ガス吸収槽にて、吸熱によりガス化
された媒体を、水などの液体に溶解せしめ、 (f)これを貯蔵した上で、ガス放出槽で減圧下で、該
溶液を加熱することによって、上記と同様のガス媒体を
得、これを上記冷熱交換器に循環送入するとともに、ガ
スを放出した液体をポンプで昇圧し、再度ガス吸収槽に
返送するようにしたことを特徴とする冷熱エネルギーの
貯蔵方法。
[Claims] [Claim 1] (a) When storing the cold energy of low-temperature liquefied gas such as LNG, (b) Using gases dissolved in liquids such as ammonia as a medium for cold energy storage, the gases of these media is liquefied in a cold heat exchanger using the cold heat of low-temperature liquefied gas, (c) This liquefied medium is pressurized using a pump or other means, and then heated in a heat exchanger using seawater etc. to form a liquid at room temperature and high pressure. Obtain a medium, temporarily store it in a medium storage tank, (d) After that, take out the storage medium at room temperature and high pressure as appropriate and expand it to a low temperature and low pressure state with an expansion valve to supply cold heat to a frozen warehouse etc. (e) Then, in a gas absorption tank, the medium that has been gasified by endotherm is dissolved in a liquid such as water; (f) After storing this, the medium is dissolved under reduced pressure in a gas release tank. By heating the solution, a gas medium similar to the above was obtained, which was then circulated to the cold heat exchanger, and the liquid from which the gas had been released was pressurized by a pump and sent back to the gas absorption tank. A method for storing cold energy characterized by the following.
JP61004700A 1986-01-13 1986-01-13 Method of storing cold heat energy Pending JPS62162866A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61004700A JPS62162866A (en) 1986-01-13 1986-01-13 Method of storing cold heat energy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61004700A JPS62162866A (en) 1986-01-13 1986-01-13 Method of storing cold heat energy

Publications (1)

Publication Number Publication Date
JPS62162866A true JPS62162866A (en) 1987-07-18

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ID=11591157

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61004700A Pending JPS62162866A (en) 1986-01-13 1986-01-13 Method of storing cold heat energy

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Country Link
JP (1) JPS62162866A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6042936A (en) * 1997-09-23 2000-03-28 Fibermark, Inc. Microsphere containing circuit board paper
JP2017538093A (en) * 2014-12-12 2017-12-21 シーメンス アクチエンゲゼルシヤフトSiemens Aktiengesellschaft How the chemical regenerator works

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6042936A (en) * 1997-09-23 2000-03-28 Fibermark, Inc. Microsphere containing circuit board paper
JP2017538093A (en) * 2014-12-12 2017-12-21 シーメンス アクチエンゲゼルシヤフトSiemens Aktiengesellschaft How the chemical regenerator works
US10072894B2 (en) 2014-12-12 2018-09-11 Siemens Aktiengesellschaft Thermochemical heat storage unit

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