JP2008273756A - Apparatus and method for producing solid/liquid two-phase nitrogen - Google Patents
Apparatus and method for producing solid/liquid two-phase nitrogen Download PDFInfo
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- JP2008273756A JP2008273756A JP2007115862A JP2007115862A JP2008273756A JP 2008273756 A JP2008273756 A JP 2008273756A JP 2007115862 A JP2007115862 A JP 2007115862A JP 2007115862 A JP2007115862 A JP 2007115862A JP 2008273756 A JP2008273756 A JP 2008273756A
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本発明は、固液2相窒素の製造装置および固液2相窒素の製造方法に係り、例えば、超電導応用機器の冷却装置に使用される固液2相窒素の製造装置および製造方法に関する。 The present invention relates to an apparatus for producing solid-liquid two-phase nitrogen and a method for producing solid-liquid two-phase nitrogen, and relates to, for example, an apparatus and a method for producing solid-liquid two-phase nitrogen used for a cooling device for superconducting equipment.
近年、スラッシュ窒素(微細な固体窒素粒子が分散したスラリー状の液体窒素)を超電導送電ケーブルの冷却に用いるために管内搬送特性に関する基礎研究が盛んに行われている。スラッシュ窒素を含めて固液2相窒素を製造するためには、主として次の2種類の方法がある。第1の方法は、真空ポンプにより減圧して窒素の三重点まで圧力を下げることにより固体窒素を生成する方法であり、第2の方法は、液体窒素中に固体窒素のできる温度(63K)以下の温度の極低温ガス(ネオン、水素、ヘリウム)を液体窒素中に噴出させて液体窒素を固化させる方法である。
しかし、上記第1の方法は、圧力が大気圧以下となるため、搬送のために加圧すると温度が上昇したり、外気の吸い込みによるトラブルが生じるおそれがある。また、真空ポンプにより排気するため、液体窒素の量が減少する。また、上記第2の方法は、ヘリウム等の極低温ガスが高価であるという問題点がある。
本発明の目的は、上記の問題点に鑑みて、簡便な構成により容易に固液2相窒素を製造する装置、および簡便な方法により容易に固液2相窒素の製造する方法を提供することにある。
However, in the first method, since the pressure is equal to or lower than the atmospheric pressure, there is a risk that when the pressure is increased for conveyance, the temperature rises or troubles due to inhalation of outside air occur. Further, since the vacuum pump exhausts, the amount of liquid nitrogen decreases. Further, the second method has a problem that a cryogenic gas such as helium is expensive.
In view of the above problems, an object of the present invention is to provide an apparatus for easily producing solid-liquid two-phase nitrogen with a simple structure and a method for easily producing solid-liquid two-phase nitrogen by a simple method. It is in.
本発明は、上記の課題を解決するために、次のような手段を採用した。
第1の手段は、固液2相窒素を収容する貯槽と、該貯槽上に取り付けられた冷凍機と、前記貯槽内の液体窒素内に浸漬され、前記冷凍機により冷却されるコールドヘッドと、該コールドヘッドに取り付けられたヒータとからなり、前記冷凍機により冷却されて前記コールドヘッドに付着した固体窒素を前記ヒータにより加熱して剥離し、前記貯槽内に固液2相窒素を製造することを特徴とする固液2相窒素製造装置である。
第2の手段は、第1の手段において、前記コールドヘッドは、該コールドヘッドの端部側に前記ヒータが取り付けられ、前記端部側より前記冷凍機側が断熱材で被覆されていることを特徴とする固液2相窒素の製造装置である。
第3の手段は、冷凍機により液体窒素内で冷却されるコールドヘッドと、該コールドヘッドに取り付けられたヒータとからなり、前記冷凍機により前記コールドヘッドを冷却して該コールドヘッドに固体窒素を付着させる工程と、その後、前記コールドヘッドの冷却を中止して前記ヒータを加熱し、前記付着した固体窒素を前記コールドヘッドから剥離する工程とを繰り返すことにより、固液2相窒素を製造することを特徴とする固液2相窒素の製造方法である。
The present invention employs the following means in order to solve the above problems.
The first means is a storage tank containing solid-liquid two-phase nitrogen, a refrigerator attached to the storage tank, a cold head immersed in liquid nitrogen in the storage tank and cooled by the refrigerator, It comprises a heater attached to the cold head, and solid nitrogen that has been cooled by the refrigerator and attached to the cold head is heated and peeled off by the heater to produce solid-liquid two-phase nitrogen in the storage tank. Is a solid-liquid two-phase nitrogen production apparatus.
According to a second means, in the first means, the cold head has the heater attached to an end side of the cold head, and the refrigerator side is covered with a heat insulating material from the end side. The solid-liquid two-phase nitrogen production apparatus.
The third means comprises a cold head cooled in liquid nitrogen by a refrigerator and a heater attached to the cold head, and the cold head is cooled by the refrigerator to supply solid nitrogen to the cold head. Producing solid-liquid two-phase nitrogen by repeating the step of adhering and then the step of stopping cooling of the cold head, heating the heater, and peeling the adhering solid nitrogen from the cold head Is a method for producing solid-liquid two-phase nitrogen.
本発明の固液2相窒素の製造装置によれば、簡便な構成により安価に固液2相窒素を製造することができ、また、本発明の固液2相窒素の製造方法によれば、簡便な方法により安価に固液2相窒素の製造することができる。 According to the solid-liquid two-phase nitrogen production apparatus of the present invention, it is possible to produce solid-liquid two-phase nitrogen at a low cost with a simple configuration, and according to the solid-liquid two-phase nitrogen production method of the present invention, Solid-liquid two-phase nitrogen can be produced at low cost by a simple method.
本発明の一実施形態を図1を用いて説明する。
図1は本実施形態の発明に係る固液2相窒素製造装置の構成を示す図である。
同図において、1は小型冷凍機、2は液体窒素6と固体窒素7からなる固液2相窒素を収容する透明ガラス貯槽、3は小型冷凍機1により冷却されるコールドヘッド、4はコールドヘッド3の端部表面に、例えば、巻回して設けられたヒータ、5はコールドヘッド3の端部表面のみに固体窒素7を付着させ、端部表面以外の箇所には固体窒素7が付着されないようにするために設けられた断熱材、6は液体窒素、7は固体窒素である。なお、透明ガラス貯槽2は2重構造になっており、2重構造内は真空引きされており、所謂魔法瓶のような断熱構造となっている。また透明ガラスも貯槽2内を可視化するために使用したものであり、本来ガラスである必要はなく、魔法瓶のようにステンレスで構成してもよい。
An embodiment of the present invention will be described with reference to FIG.
FIG. 1 is a diagram showing a configuration of a solid-liquid two-phase nitrogen production apparatus according to the invention of this embodiment.
In the figure, 1 is a small refrigerator, 2 is a transparent glass storage tank for storing solid-liquid two-phase nitrogen composed of liquid nitrogen 6 and solid nitrogen 7, 3 is a cold head cooled by the small refrigerator 1, and 4 is a cold head. For example, a heater 5 wound around the end surface of 3 is attached with solid nitrogen 7 only on the end surface of the cold head 3, so that solid nitrogen 7 does not adhere to portions other than the end surface. Insulating material provided for the purpose, 6 is liquid nitrogen, and 7 is solid nitrogen. In addition, the transparent glass storage tank 2 has a double structure, and the inside of the double structure is evacuated, and has a heat insulation structure like a so-called thermos. Further, the transparent glass is also used for visualizing the inside of the storage tank 2, and is not necessarily glass, but may be made of stainless steel like a thermos.
同装置において、固液2相窒素は次の手順で製造される。まず、透明ガラス貯槽2に液体窒素6を充填し、小型冷凍機1の運転を開始する。運転開始後約6時間で固体窒素7がコールドヘッド3の端部周囲にでき始める。さらに運転を続けると固体窒素7の厚みは、例えば、約1mm/10 min.の割合で増加していく。ある程度の厚さの固体窒素7がコールドヘッド3の端部周囲に付着されたら、小型冷凍機1の運転を停止し、ヒータ4を投入する。数分後、ヒータ4と固体窒素7との間に気泡が生じ、その後、固体窒素7が剥離し、液体窒素6中に固体窒素7が混在した固液2相窒素が製造される。この一連の作業を繰り返すことにより、透明ガラス貯槽2内において、固液2相窒素中における固体窒素7の割合を増やすことができる。 In this apparatus, solid-liquid two-phase nitrogen is produced by the following procedure. First, the transparent glass storage tank 2 is filled with liquid nitrogen 6 and the operation of the small refrigerator 1 is started. About 6 hours after the start of operation, solid nitrogen 7 starts to form around the end of the cold head 3. When the operation is further continued, the thickness of the solid nitrogen 7 increases, for example, at a rate of about 1 mm / 10 min. When solid nitrogen 7 having a certain thickness is attached around the end of the cold head 3, the operation of the small refrigerator 1 is stopped and the heater 4 is turned on. After a few minutes, bubbles are generated between the heater 4 and the solid nitrogen 7, and then the solid nitrogen 7 is peeled off to produce solid-liquid two-phase nitrogen in which the solid nitrogen 7 is mixed in the liquid nitrogen 6. By repeating this series of operations, the ratio of solid nitrogen 7 in the solid-liquid two-phase nitrogen can be increased in the transparent glass storage tank 2.
超電導応用機器の冷却装置において、特に、超電導機器からの発熱が定常的ではなく、負荷変動が大きい場合には固体窒素の融解潜熱を利用することにより、冷媒温度を一定に保つことができる。 In the cooling device for superconducting equipment, particularly when the heat generated from the superconducting equipment is not steady and the load fluctuation is large, the refrigerant temperature can be kept constant by utilizing the latent heat of fusion of solid nitrogen.
1 小型冷凍機
2 透明ガラス貯槽
3 コールドヘッド
4 ヒータ
5 断熱材
6 液体窒素
7 固体窒素
DESCRIPTION OF SYMBOLS 1 Small refrigerator 2 Transparent glass storage tank 3 Cold head 4 Heater 5 Heat insulating material 6 Liquid nitrogen 7 Solid nitrogen
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04280801A (en) * | 1991-03-08 | 1992-10-06 | Iwatani Internatl Corp | Slash hydrogen-producing device |
JPH06281321A (en) * | 1993-03-31 | 1994-10-07 | Nippon Sanso Kk | Method and apparatus for manufacturing slush hydrogen |
JPH07239095A (en) * | 1994-02-25 | 1995-09-12 | Mitsubishi Heavy Ind Ltd | Slash hydrogen receiving and discharging pipe |
JPH08283001A (en) * | 1995-04-12 | 1996-10-29 | Mitsubishi Heavy Ind Ltd | Production of slush hydrogen and device therefor |
WO2004080892A1 (en) * | 2003-03-11 | 2004-09-23 | Mayekawa Mfg. Co., Ltd. | Process for producing slush nitrogen and apparatus therefor |
WO2005075352A1 (en) * | 2004-02-06 | 2005-08-18 | Mayekawa Mfg.Co.,Ltd. | Method and apparatus for producing slush nitrogen |
JP2008002715A (en) * | 2006-06-20 | 2008-01-10 | Tohoku Univ | Very low temperature micro-slush production system |
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Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04280801A (en) * | 1991-03-08 | 1992-10-06 | Iwatani Internatl Corp | Slash hydrogen-producing device |
JPH06281321A (en) * | 1993-03-31 | 1994-10-07 | Nippon Sanso Kk | Method and apparatus for manufacturing slush hydrogen |
JPH07239095A (en) * | 1994-02-25 | 1995-09-12 | Mitsubishi Heavy Ind Ltd | Slash hydrogen receiving and discharging pipe |
JPH08283001A (en) * | 1995-04-12 | 1996-10-29 | Mitsubishi Heavy Ind Ltd | Production of slush hydrogen and device therefor |
WO2004080892A1 (en) * | 2003-03-11 | 2004-09-23 | Mayekawa Mfg. Co., Ltd. | Process for producing slush nitrogen and apparatus therefor |
WO2005075352A1 (en) * | 2004-02-06 | 2005-08-18 | Mayekawa Mfg.Co.,Ltd. | Method and apparatus for producing slush nitrogen |
JP2008002715A (en) * | 2006-06-20 | 2008-01-10 | Tohoku Univ | Very low temperature micro-slush production system |
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