JP4164203B2 - Gas liquefaction recovery equipment - Google Patents
Gas liquefaction recovery equipment Download PDFInfo
- Publication number
- JP4164203B2 JP4164203B2 JP23340299A JP23340299A JP4164203B2 JP 4164203 B2 JP4164203 B2 JP 4164203B2 JP 23340299 A JP23340299 A JP 23340299A JP 23340299 A JP23340299 A JP 23340299A JP 4164203 B2 JP4164203 B2 JP 4164203B2
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- Prior art keywords
- gas
- liquefied
- recovered
- chamber
- liquefaction recovery
- 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.)
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、低温の作業環境を得るために液化ガスを使用する技術分野で、使用した液化ガスの回収再液化装置に関し、特に、液化ガス貯蔵容器への液化ガスの移充填時や理科学機器の冷却に使用した後に放出される液化ガスの回収再液化装置に関する。
【0002】
【従来の技術】
電子顕微鏡やNMR等の電子計測機器類や超伝導実験設備等の理科学機器の冷却では極低温の作業環境を作り出すために、液化窒素、液化アルゴン、液化ヘリウムあるいは液化水素等の液化ガスの寒冷熱を利用している。
【0003】
【発明が解決しようとする課題】
ところが、この場合、これら液化ガスを補給したり、容器に充填したりする際に、容器内から液化ガスの気化成分や移充填時に気化したガスを放出している。また、電子計測機器類や超伝導実験設備等の理科学機器では気化熱を利用して低温維持をするようにしていることから、容器内の圧力を一定に保つために気化ガスを放出している。このため高価な液化ガスを無駄に捨てている状態となり、液化ガスの有効利用率が低くなるという問題があった。
【0004】
本発明はこのような点に着目して、液化ガスの移充填時や理科学機器の冷却後に放出される気化ガスを回収液化できるガス液化回収装置を提供することを目的とする。
【0005】
【課題を解決するための手段】
上述の目的を達成するために請求項1に記載した発明は、断熱容器の内部を熱交換板により上下二室に区画し、上側室に極低温冷凍機のコールドエンドを位置させ、この上側室に冷媒ガスを液体状態で貯溜するとともに、下側室に被回収ガスを導入し、上側室に貯溜している液化冷媒ガスの保有熱で被回収ガスを液化して回収するようにしたことを特徴とし、請求項2に記載の発明は下側室内に不純物除去フィルタを装着したことを特徴としている。
【0006】
【発明の作用】
本発明では、断熱容器の内部を熱交換板により上下二室に区画し、上側室に極低温冷凍機のコールドエンドを臨ませて配置し、この上側室に冷媒ガスを、下側室に被回収ガスをそれぞれ導入するようにしていることから、冷媒ガスは上側室において直接極低温冷凍機で冷却され、液化されるのに対し、下側室では熱交換板を介して伝達される上側室の冷熱で被回収ガスが冷却され再液化することになる。
【0007】
【発明の実施の形態】
図は本発明を適用したひとつの実施形態を示すガス液化回収装置の概略構成図である。このガス液化回収装置は、断熱容器(1)の内部空間を熱交換板(2)を配置して、断熱容器(1)内を上側室(3)と下側室(4)とに区画してある。なお、熱交換板(2)は上に凸の鏡板で形成してある。
【0008】
上側室(3)には、液化アルゴン、液化ヘリウム、液化水素、液化窒素等の冷媒ガスの導入路(5)が開口するとともに、極低温冷凍機(6)のコールドエンド(7)が臨んでいる。そして、上側室(3)に流入した冷媒ガスを液体状態で貯溜するようにしてある。極低温冷凍機(6)は、上側室(3)内の液面を検出する液面計(8)又は圧力計の検出結果に基づき運転制御されるようにしてあり、上側室(3)内には常時所定量の液体冷媒ガスが貯溜するようにしてある。
【0009】
一方、下側室(4)には、液化ガスに移充填時や電子計測機器類や超伝導実験設備等で低温を維持するために放出された被回収ガスの導入路(9)が開口しており、下側室(4)内に不純物除去フィルタ(10)が複数段に装着してある。なお、この被回収ガスの導入路(9)の先端部は、下側室(4)の天井を構成する熱交換板(2)に小間隔へだてて対向配置した反射板(11)に向けて開口してあり、噴出した被回収ガスが熱交換板(2)に効率よく接触できるようにしてある。
【0010】
被回収ガスの導入路(9)には、補充ガス通路(12)が連通しており、この補充ガス通路(12)には補充用ガスボンベ(13)が接続してある。また、この補充用ガス通路(12)から分岐した真空引き路(14)に真空ポンプ(15)が装着してある。
【0011】
図中符号(16)は下側室(4)の底部に連通している再液化ガス取出管、(17)は上側室(3)の底部に連通している冷媒ガス取出管である。
【0012】
このように構成した再液化回収装置では、上側室(3)に貯溜されている液化冷媒ガスが保有している寒冷熱エネルギーが熱交換板(2)に伝達されることになる。一方、ガス放出現場で回収された被回収ガスは被回収ガス導入路(9)から下側室(4)に導入される。この導入時に冷媒ガスの寒冷熱で冷やされている熱交換板(2)に接触する状態に噴出されることから、被回収ガスは凝縮・液化することになる。しかも、下側室(4)には不純物除去フィルタ(10)が複数段に装着してあることから、再液化した被回収ガスは高純度なものになり、液化被回収ガスを取り出して使用することができる。
【0013】
このとき、被回収ガスと冷媒ガスとが同種のガスであっても、液体状態での保有熱エネルギーと気体状態での保有熱エネルギーに差があること、及び、上側室(3)では、極低温冷凍機により、冷却エネルギーが補給されていることから、下側室(4)に導入された被回収ガスは冷却されることになり、凝縮液化が継続して行われる。
【0014】
【発明の効果】
本発明では、断熱容器内を上下二室に区画し、上側室を冷媒ガス室に形成するとともに、下側室を回収ガス室に形成し、上側室内にコールドヘッドが臨む状態に極低温冷凍機を配置して上側室内に一定量の冷媒ガスを液体状態で貯溜するようにしているので、下側室に導入した液化ガスの移充填現場から排出された気化ガスや液化ガスを使用している理科学機器から排出された気化ガスを上側室に貯溜されている液化冷媒ガスの保有熱エネルギーで冷却し、再液化することができる。これにより、従来廃棄されていた気化ガスを回収して再利用できることになり、高価な液化ガスの有効利用率を高めることができる。
【図面の簡単な説明】
【図1】本発明を適用したひとつの実施形態を示すガス液化回収装置の概略構成図である。
【符号の説明】
1…断熱容器、2…熱交換板、3…上側室、4…下側室、6…極低温冷凍機、7…極低温冷凍機のコールドエンド、10…不純物除去フィルタ。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a recovery and liquefaction apparatus for liquefied gas used in a technical field that uses liquefied gas in order to obtain a low-temperature working environment. The present invention relates to a recovery and liquefaction apparatus for liquefied gas released after being used for cooling.
[0002]
[Prior art]
Cooling of liquefied gas such as liquefied nitrogen, liquefied argon, liquefied helium or liquefied hydrogen is required to create a cryogenic working environment for cooling of electronic measuring instruments such as electron microscope and NMR, and scientific equipment such as superconducting experimental equipment. Uses heat.
[0003]
[Problems to be solved by the invention]
However, in this case, when the liquefied gas is replenished or filled into the container, the vaporized component of the liquefied gas or the gas vaporized at the time of transfer and filling is released from the container. In addition, scientific and scientific instruments such as electronic measuring instruments and superconducting experimental facilities use heat of vaporization to maintain a low temperature, so that vaporized gas is released to keep the pressure inside the container constant. Yes. For this reason, expensive liquefied gas was wasted, and there was a problem that the effective utilization rate of liquefied gas was lowered.
[0004]
The present invention pays attention to such a point, and an object of the present invention is to provide a gas liquefaction recovery apparatus capable of recovering and liquefying the vaporized gas released at the time of transferring and filling the liquefied gas or after cooling the scientific instrument.
[0005]
[Means for Solving the Problems]
In order to achieve the above-mentioned object, the invention described in claim 1 divides the inside of the heat insulating container into two upper and lower chambers by a heat exchange plate, and positions the cold end of the cryogenic refrigerator in the upper chamber. The refrigerant gas is stored in a liquid state, and the gas to be recovered is introduced into the lower chamber, and the gas to be recovered is liquefied and recovered by the retained heat of the liquefied refrigerant gas stored in the upper chamber. The invention according to
[0006]
[Effects of the Invention]
In the present invention, the inside of the heat insulating container is partitioned into two upper and lower chambers by a heat exchange plate, and the cold chamber of the cryogenic refrigerator is disposed facing the upper chamber, and the refrigerant gas is collected in the lower chamber, and the refrigerant gas is collected in the lower chamber. Since each gas is introduced, the refrigerant gas is directly cooled and liquefied by the cryogenic refrigerator in the upper chamber, whereas the lower chamber is transmitted through the heat exchange plate in the lower chamber. Thus, the gas to be recovered is cooled and reliquefied.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 is a schematic configuration diagram of a gas liquefaction recovery apparatus showing one embodiment to which the present invention is applied. In this gas liquefaction recovery device, the heat exchange plate (2) is arranged in the inner space of the heat insulating container (1), and the heat insulating container (1) is partitioned into an upper chamber (3) and a lower chamber (4). is there. In addition, the heat exchange plate (2) is formed of an upwardly convex end plate.
[0008]
In the upper chamber (3), an introduction path (5) for refrigerant gas such as liquefied argon, liquefied helium, liquefied hydrogen, and liquefied nitrogen opens, and a cold end (7) of the cryogenic refrigerator (6) faces. Yes. The refrigerant gas flowing into the upper chamber (3) is stored in a liquid state. The cryogenic refrigerator (6) is controlled to operate based on the detection result of the liquid level gauge (8) or pressure gauge for detecting the liquid level in the upper chamber (3). In this case, a predetermined amount of liquid refrigerant gas is always stored.
[0009]
On the other hand, in the lower chamber (4), there is an opening (9) for introducing a gas to be recovered that is released in order to maintain a low temperature during transfer and filling of liquefied gas, electronic measuring instruments, superconducting experimental equipment, and the like. In the lower chamber (4), impurity removal filters (10) are mounted in a plurality of stages. The leading end of the gas to be collected (9) opens toward the reflecting plate (11) arranged facing the heat exchange plate (2) constituting the ceiling of the lower chamber (4) at a small interval. Thus, the ejected gas to be collected can be efficiently brought into contact with the heat exchange plate (2).
[0010]
A replenishment gas passage (12) communicates with the recovery gas introduction passage (9), and a refill gas cylinder (13) is connected to the replenishment gas passage (12). In addition, a vacuum pump (15) is attached to the vacuum drawing path (14) branched from the replenishing gas path (12).
[0011]
In the figure, reference numeral (16) denotes a reliquefied gas take-out pipe communicating with the bottom of the lower chamber (4), and (17) denotes a refrigerant gas take-out pipe communicating with the bottom of the upper chamber (3).
[0012]
In the reliquefaction recovery apparatus configured as described above, the cold energy stored in the liquefied refrigerant gas stored in the upper chamber (3) is transmitted to the heat exchange plate (2). On the other hand, the gas to be recovered collected at the gas discharge site is introduced into the lower chamber (4) from the gas to be recovered introduction path (9). The gas to be recovered is condensed and liquefied because it is ejected in contact with the heat exchange plate (2) cooled by the cold heat of the refrigerant gas at the time of introduction. In addition, since the lower chamber (4) is equipped with the impurity removal filter (10) in a plurality of stages, the liquefied gas to be recovered becomes high purity, and the liquefied gas to be recovered is taken out and used. Can do.
[0013]
At this time, even if the gas to be recovered and the refrigerant gas are the same type of gas, there is a difference between the retained thermal energy in the liquid state and the retained thermal energy in the gaseous state, and in the upper chamber (3), Since the cooling energy is replenished by the low-temperature refrigerator, the gas to be recovered introduced into the lower chamber (4) is cooled, and the condensation is continuously performed.
[0014]
【The invention's effect】
In the present invention, the inside of the heat insulating container is divided into two upper and lower chambers, the upper chamber is formed in the refrigerant gas chamber, the lower chamber is formed in the recovered gas chamber, and the cryogenic refrigerator is placed with the cold head facing the upper chamber. Since a certain amount of refrigerant gas is stored in a liquid state in the upper chamber, the science and science that uses vaporized gas or liquefied gas discharged from the transfer and filling site of liquefied gas introduced into the lower chamber The vaporized gas discharged from the device can be cooled by the retained heat energy of the liquefied refrigerant gas stored in the upper chamber and reliquefied. Thereby, the vaporized gas that has been conventionally discarded can be recovered and reused, and the effective utilization rate of the expensive liquefied gas can be increased.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram of a gas liquefaction recovery apparatus showing an embodiment to which the present invention is applied.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Thermal insulation container, 2 ... Heat exchange plate, 3 ... Upper chamber, 4 ... Lower chamber, 6 ... Cryogenic refrigerator, 7 ... Cold end of cryogenic refrigerator, 10 ... Impurity removal filter.
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23340299A JP4164203B2 (en) | 1999-08-20 | 1999-08-20 | Gas liquefaction recovery equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23340299A JP4164203B2 (en) | 1999-08-20 | 1999-08-20 | Gas liquefaction recovery equipment |
Publications (2)
Publication Number | Publication Date |
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JP2001059676A JP2001059676A (en) | 2001-03-06 |
JP4164203B2 true JP4164203B2 (en) | 2008-10-15 |
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Application Number | Title | Priority Date | Filing Date |
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JP23340299A Expired - Lifetime JP4164203B2 (en) | 1999-08-20 | 1999-08-20 | Gas liquefaction recovery equipment |
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Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5070541B2 (en) * | 2006-09-12 | 2012-11-14 | 国立大学法人富山大学 | Laboratory instrument for observing liquid oxygen |
CN104390125B (en) * | 2014-10-27 | 2016-06-15 | 中国海洋石油总公司 | Liquefied natural gas flashed vapour constant voltage recovery method and equipment |
KR101822263B1 (en) * | 2016-03-24 | 2018-03-08 | 한국과학기술연구원 | Low thermal liquid storage tank with a detachable cryocooler |
CN114046439B (en) * | 2021-11-02 | 2023-08-15 | 深圳供电局有限公司 | Liquid nitrogen nondestructive storage system |
-
1999
- 1999-08-20 JP JP23340299A patent/JP4164203B2/en not_active Expired - Lifetime
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JP2001059676A (en) | 2001-03-06 |
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