JP3811578B2 - Alcohol-based cryogenic storage material - Google Patents
Alcohol-based cryogenic storage material Download PDFInfo
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- JP3811578B2 JP3811578B2 JP31474998A JP31474998A JP3811578B2 JP 3811578 B2 JP3811578 B2 JP 3811578B2 JP 31474998 A JP31474998 A JP 31474998A JP 31474998 A JP31474998 A JP 31474998A JP 3811578 B2 JP3811578 B2 JP 3811578B2
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- Prior art keywords
- alcohol
- solid
- phase
- cold storage
- heat
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- 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
Description
【0001】
【発明の属する技術分野】
本発明は、LNG等に適用するためのアルコール系極低温蓄冷材に係り、特に、−135℃で流動性のよいアルコール系極低温蓄冷材に関するものである。
【0002】
【従来の技術】
従来、極低温用蓄冷材としては、エタノールとメタノールの混合物が知られている。この蓄冷材は、凝固点−143℃と低温であり、極低温の蓄冷に適している。
【0003】
この極低温用蓄冷材を、例えばLNGに適用する場合、LNGの消費量が多い日中に、LNGと極低温用蓄冷材を熱交換させて、BOGとすると共に蓄冷し、夜間に蓄冷した極低温用蓄冷材でLNGタンクから発生するBOGを冷却して再液化することなどに用いることができる。
【0004】
【発明が解決しようとする課題】
しかしながら、LNGに適応する蓄冷材で、固液共存相を用いて蓄冷するには、−143℃では、凝固点が高く、LNG(−169℃)と熱交換すると固相となり、伝熱管のまわりに凝固した固体が成長してしまう問題がある。また、この場合、固相の比熱を蓄冷に利用することになるが、液相の方が固相よりも比熱が大きいため、蓄冷熱量を十分に得られない。
【0005】
そこで、本発明の目的は、上記課題を解決し、凝固温度が約−150℃と極低温で、−135℃で流動性の良好なアルコール系極低温蓄冷材を提供することにある。
【0006】
【課題を解決するための手段】
上記の目的を達成するために、請求項1の発明は、約58重量%のエタノールと約42重量%のメタノールを混合した共晶物質に、水を添加したものである。
【0008】
請求項2の発明は、 共晶物質が水に対して約90重量%以下であり、約−135℃で流動性の良い固液共存相を形成する請求項1記載のアルコール系極低温蓄冷材である。
【0009】
【発明の実施の形態】
以下、本発明の好適一実施の形態を添付図面に基づいて詳述する。
【0010】
先ず、エタノール58重量%、メタノール42重量%を混合して共晶物質を作り、この共晶物質に水を添加してアルコール系極低温蓄冷材とする。
【0011】
図1は、共晶物質の濃度C(wt%)と温度twにおける三成分(エタノール−メタノール−水)の状態図を示したものである。
【0012】
この状態図は、共晶物質と水との混合割合を、0〜100wt%変え、これを−160℃まで温度twを下げたとき、その割合における相変化を起こした温度を測定したもので、Lが液相線、Sが固相線を示し、液相線Lより温度が高い領域が液相(Liquid)、固相線Sより温度が低い領域が固相(Solid)であり、固相線Sと液相線Lの間の領域が固液共存相(L+S)となる。
【0013】
この状態図において、固相線Sは、共晶物質の混合割合0〜100wt%で、−148℃と一定となり、液相線Lは、共晶物質の混合割合が0wt%で0℃から、90wt%で−148℃と順次混合割合が増えるに従って低下する。そして、共晶物質90wt%以上(水10wt%以下)となると、固液共存相(L+S)を形成することなく、液相(Liquid)から温度を下げると直接固相(Solid)に相変化する。
【0014】
そこで、LNGの再液化用の蓄冷材として、−135℃で良好な流動性を有する固液共存相(L+S)を形成する共晶物質90wt%以下の割合のものを使用する。
【0015】
この本発明のアルコール系極低温蓄冷材を、蓄冷槽(図示せず)に充填しておき、他方蓄冷槽に伝熱管を設けておき、その伝熱管内に極低温冷媒を通すことで、蓄冷槽内のアルコール系極低温蓄冷材が蓄冷される。
【0016】
この際、アルコール系極低温蓄冷材は、−135℃で、流動性の良好な固液共存相(L+S)を形成するため、伝熱管の伝熱係数が、伝熱管表面に固相を凝固させる一般の蓄冷材に比べて大きくなるので熱交換が良好に行えると共に、その熱交換面積を小さくでき熱交換器(伝熱管)を小型化できる。
【0017】
また、蓄冷は、固液共存相(L+S)の液相の顕熱のみならず固相の凝固熱分も合わせて蓄冷熱量となるため、蓄冷熱量を高くすることが可能となる。
【0018】
この本発明のアルコール系極低温蓄冷材は、凝固温度が約−148℃であり、−135℃で、流動性の良好な固液共存相(L+S)を形成するため、LNGに適用することで良好な蓄冷材とすることができる。
【0019】
すなわち、LNGの温度は−169℃であり、このLNGを、消費量の多い日中に蓄冷槽に通して、アルコール系極低温蓄冷材を、−135℃に蓄冷し、夜間、LNG消費量の少ないとき、LNG低温タンクから発生するBOGガスを、圧縮した状態で蓄冷槽内の伝熱管を通してタンクに戻すことで、蓄冷熱量を利用して再液化が可能となる。
【0021】
【発明の効果】
以上要するに本発明によれば、凝固点が約−150℃であり、これまで使用されている蓄冷材と比較して極低温での蓄冷に良好な蓄冷材とすることができると共に、−135℃で流動性の良好な固液共存相を形成するため、蓄冷用熱交換器での熱交換率を高めることができる。
【図面の簡単な説明】
【図1】本発明のアルコール系極低温蓄冷材の状態図を示す図である。
【符号の説明】
L 液相線
S 固相線
L+S 固液共存相[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an alcohol-based cryogenic regenerator material for application to LNG and the like, and more particularly to an alcohol-based cryogenic regenerator material having good fluidity at -135 ° C.
[0002]
[Prior art]
Conventionally, a mixture of ethanol and methanol is known as a cryogenic regenerator material. This cold storage material has a freezing point of −143 ° C. and a low temperature, and is suitable for extremely low temperature cold storage.
[0003]
When this cryogenic regenerator material is applied to, for example, LNG, during the day when the amount of LNG consumption is large, the LNG and the cryogenic regenerator material are heat-exchanged to form a BOG and cool, and stored at night. It can be used for cooling and re-liquefying BOG generated from the LNG tank with a cold storage material for low temperature.
[0004]
[Problems to be solved by the invention]
However, it is a regenerator material suitable for LNG, and in order to store cold using a solid-liquid coexisting phase, the freezing point is high at -143 ° C, it becomes a solid phase when heat exchange with LNG (-169 ° C), and around the heat transfer tube There is a problem that solidified solids grow. In this case, the specific heat of the solid phase is used for cold storage. However, since the specific heat of the liquid phase is larger than that of the solid phase, a sufficient amount of cold storage heat cannot be obtained.
[0005]
Accordingly, an object of the present invention is to solve the above problems and provide an alcohol-based cryogenic regenerator material having a solidification temperature of about −150 ° C. and an extremely low temperature, and having a good fluidity at −135 ° C.
[0006]
[Means for Solving the Problems]
To achieve the above object, the invention of
[0008]
A second aspect of the present invention, the eutectic material is about 90 wt% or less in water, alcohol cryogenic cold accumulating material according to
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, a preferred embodiment of the present invention will be described in detail with reference to the accompanying drawings.
[0010]
First, 58% by weight of ethanol and 42% by weight of methanol are mixed to form a eutectic material, and water is added to this eutectic material to obtain an alcohol-based cryogenic regenerator material.
[0011]
FIG. 1 shows a phase diagram of three components (ethanol-methanol-water) at a concentration C (wt%) of an eutectic substance and a temperature tw.
[0012]
In this phase diagram, the mixing ratio of the eutectic substance and water was changed from 0 to 100 wt%, and when the temperature tw was lowered to -160 ° C, the temperature at which the phase change occurred was measured. L is a liquidus, S is a solidus, a region where the temperature is higher than the liquidus L is a liquid phase, and a region where the temperature is lower than the solidus S is a solid. A region between the line S and the liquidus line L is a solid-liquid coexisting phase (L + S).
[0013]
In this state diagram, the solid phase line S is constant at −148 ° C. at a eutectic material mixing ratio of 0 to 100 wt%, and the liquidus line L is from 0 ° C. at a eutectic material mixing ratio of 0 wt%, At 90 wt%, it decreases as the mixing ratio increases successively at -148 ° C. And if it becomes 90 wt% or more of eutectic substance (10 wt% or less of water), it will change into a solid phase (Solid) directly when the temperature is lowered from the liquid phase (Liquid) without forming a solid-liquid coexisting phase (L + S). .
[0014]
Therefore, as a regenerator material for reliquefaction of LNG, a material having a ratio of eutectic substance of 90 wt% or less that forms a solid-liquid coexisting phase (L + S) having good fluidity at −135 ° C. is used.
[0015]
The alcohol-based cryogenic regenerator material of the present invention is filled in a regenerator (not shown), a heat transfer tube is provided in the other regenerator, and a cryogenic refrigerant is passed through the heat exchanger tube, thereby The alcohol-based cryogenic regenerator material in the tank is regenerated.
[0016]
At this time, the alcohol-based cryogenic regenerator material forms a solid-liquid coexisting phase (L + S) with good fluidity at −135 ° C., so that the heat transfer coefficient of the heat transfer tube solidifies the solid phase on the surface of the heat transfer tube. Since it becomes larger than a general cold storage material, heat exchange can be performed well, and the heat exchange area can be reduced, and the heat exchanger (heat transfer tube) can be downsized.
[0017]
In addition, since the cold storage stores the amount of cold storage not only in the sensible heat of the liquid phase of the solid-liquid coexisting phase (L + S) but also in the solidification heat of the solid phase, the amount of cold storage heat can be increased.
[0018]
This alcohol-based cryogenic regenerator material of the present invention has a solidification temperature of about −148 ° C. and forms a solid-liquid coexisting phase (L + S) with good fluidity at −135 ° C. It can be a good cold storage material.
[0019]
That is, the temperature of LNG is −169 ° C., and this LNG is passed through a cold storage tank during the day when consumption is high, and the alcohol-based cryogenic cold storage material is stored at −135 ° C. When the amount is small, BOG gas generated from the LNG low-temperature tank is returned to the tank through a heat transfer tube in the cold storage tank in a compressed state, so that reliquefaction can be made using the amount of cold storage heat.
[0021]
【The invention's effect】
In short, according to the present invention, the freezing point is about −150 ° C., and it can be a cold storage material that is good for cold storage at extremely low temperatures compared to the cold storage materials used so far, and at −135 ° C. Since a solid-liquid coexisting phase with good fluidity is formed, the heat exchange rate in the heat storage heat exchanger can be increased.
[Brief description of the drawings]
FIG. 1 is a diagram showing a state diagram of an alcohol-based cryogenic regenerator material according to the present invention.
[Explanation of symbols]
L Liquidus line S Solidus line L + S Solid-liquid coexisting phase
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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JP31474998A JP3811578B2 (en) | 1998-11-05 | 1998-11-05 | Alcohol-based cryogenic storage material |
Applications Claiming Priority (1)
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JP31474998A JP3811578B2 (en) | 1998-11-05 | 1998-11-05 | Alcohol-based cryogenic storage material |
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JP2000144123A JP2000144123A (en) | 2000-05-26 |
JP3811578B2 true JP3811578B2 (en) | 2006-08-23 |
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JP31474998A Expired - Fee Related JP3811578B2 (en) | 1998-11-05 | 1998-11-05 | Alcohol-based cryogenic storage material |
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Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
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ITFI20090212A1 (en) * | 2009-10-05 | 2011-04-06 | Univ Firenze | CRYOGENIC SYSTEM WITH CHANGE OF SOLID-LIQUID PHASE FOR LOW TEMPERATURE INDUSTRIAL PROCESSES. |
JP6837966B2 (en) * | 2015-06-19 | 2021-03-03 | 株式会社カネカ | Cold storage material composition, cold storage material and shipping container |
WO2018180506A1 (en) * | 2017-03-29 | 2018-10-04 | 株式会社カネカ | Cold storage material composition, method for using cold storage material composition, cold storage material and transport container |
WO2019172149A1 (en) | 2018-03-06 | 2019-09-12 | 株式会社カネカ | Cold storage material composition and use thereof |
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