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JPH0126474B2 - - Google Patents
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JPH0126474B2 - - Google Patents

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Publication number
JPH0126474B2
JPH0126474B2 JP210282A JP210282A JPH0126474B2 JP H0126474 B2 JPH0126474 B2 JP H0126474B2 JP 210282 A JP210282 A JP 210282A JP 210282 A JP210282 A JP 210282A JP H0126474 B2 JPH0126474 B2 JP H0126474B2
Authority
JP
Japan
Prior art keywords
gas
condensing
convection
condensing section
heat exchange
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.)
Expired
Application number
JP210282A
Other languages
Japanese (ja)
Other versions
JPS58120071A (en
Inventor
Toshuki Amano
Osamu Ogino
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP210282A priority Critical patent/JPS58120071A/en
Publication of JPS58120071A publication Critical patent/JPS58120071A/en
Publication of JPH0126474B2 publication Critical patent/JPH0126474B2/ja
Granted legal-status Critical Current

Links

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  • Separation By Low-Temperature Treatments (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

【発明の詳細な説明】 この発明はガス凝縮装置に関するものである。[Detailed description of the invention] This invention relates to a gas condensing device.

従来のこの種の装置について説明する。従来
は、凝縮させたい気体中に寒冷発生装置と熱的に
凍結された凝縮部を設置し、フアン等の装置で凝
縮させたい気体を強制的に送り込んで凝縮部と接
触させるか、あるいは気体の流れの中に凝縮部を
設置することにより熱交換させるものであつた。
しかしながら、フアン等の機械的・電気的動力を
必要とする装置を設置することは不利であり、ま
た構造的に設置することが出来ない場合がある。
あるいは気体の流れが無い場合等には単に気体中
に凝縮容量の大きい凝縮部を設置するという構成
であつた。その一例が第1図である。図におい
て、1が凝縮タンク、1aが凝縮液化させたい気
体の気相部、1bが液相部、2が図示されていな
い寒冷発生装置と熱的に連結された(この場合、
冷媒流体が流れている)凝縮部である。
A conventional device of this type will be explained. Conventionally, a cold generator and a thermally frozen condensing section were installed in the gas to be condensed, and the gas to be condensed was forced into contact with the condensing section using a device such as a fan, or the gas was Heat exchange was performed by installing a condensing section in the flow.
However, it is disadvantageous to install devices that require mechanical or electrical power, such as fans, and may not be structurally possible.
Alternatively, when there is no gas flow, a condensing section with a large condensing capacity is simply installed in the gas. An example is shown in FIG. In the figure, 1 is a condensation tank, 1a is a gas phase portion of the gas to be condensed and liquefied, 1b is a liquid phase portion, and 2 is thermally connected to a cold generator (not shown) (in this case,
This is the condensing section (through which the refrigerant fluid flows).

図示されていない寒冷発生部と熱的に凍結され
た凝縮部2に凝縮液化させたい気体を接触させる
ことにより、凝縮部2と気体とを凝縮熱伝達によ
つて熱交換させ気体を液化させる。
By bringing the gas to be condensed and liquefied into contact with a cold generation part (not shown) and the thermally frozen condensing part 2, the condensing part 2 and the gas exchange heat through condensation heat transfer, and the gas is liquefied.

第1図のように単に気体を凝縮部2に接触させ
る場合には、凝縮部2に気体が接触することによ
り、凝縮熱伝達によつて熱交換をし、凝縮液化す
る。この時の熱交換は自然対流によるものであ
り、これは強制対流によるものと比べて熱交換特
性が落ちる。また、凝縮部2に液膜が生じて、凝
縮部2に気体が直接接触することが出来なくな
り、この液膜が熱抵抗となつて熱交換特性が落ち
るという欠点があつた。そこで熱交換特性を良く
するため、凝縮部に強制的に気体を流して、強制
対流により熱交換特性を向上させるよう、また強
制対流により液膜を取り除き気体と凝縮部2を直
接接触させ熱交換特性を向上させるよう、フアン
等の送風装置で強制対流を発生させるか、あるい
は流れている気体中に凝縮部2を置くといつた方
法がとられていた。しかしそのような方法をとる
ことが出来ない場合、あるいは不利な場合、例え
ば、ヘリウムを容器内で凝縮器によつて液化させ
たい場合では凝縮温度が−269℃と極低温条件に
あるためフアン等の取り付けが困難でありまた高
価になる欠点がある。
When the gas is simply brought into contact with the condensing section 2 as shown in FIG. 1, the gas comes into contact with the condensing section 2, thereby exchanging heat through condensation heat transfer, and condensing and liquefying the gas. Heat exchange at this time is based on natural convection, which has poor heat exchange characteristics compared to forced convection. In addition, a liquid film is formed in the condensing part 2, making it impossible for gas to directly contact the condensing part 2, and this liquid film becomes a thermal resistance, resulting in a deterioration of heat exchange characteristics. Therefore, in order to improve the heat exchange characteristics, gas is forced to flow into the condensing section, and forced convection improves the heat exchange characteristics.Also, forced convection removes the liquid film and brings the gas into direct contact with the condensing section 2 for heat exchange. In order to improve the characteristics, methods have been used such as generating forced convection with a blower such as a fan or placing the condensing section 2 in the flowing gas. However, if such a method is not possible or disadvantageous, for example, when it is desired to liquefy helium in a container using a condenser, the condensation temperature is extremely low at -269°C, so a fan, etc. The drawback is that it is difficult and expensive to install.

この発明は、上記のような欠点を除くためのも
ので、凝縮部に、少なくとも一組の流体入口と流
体出口とを有し、煙突効果(ここで言う煙突効果
とは煙突の内外の圧力差によつて煙突外部の気体
が内部に引き込まれる現象を言う。以下同じ)を
生じるような対流構造体、例えば円筒状のものを
設置し強制対流を起こすことによつて、より良好
な熱交換特性を有するようなガス凝縮装置を提供
することを目的としている。
This invention is intended to eliminate the above-mentioned drawbacks, and includes at least one set of fluid inlets and fluid outlets in the condensing section, and the chimney effect (the chimney effect here refers to the pressure difference between the inside and outside of the chimney). This refers to the phenomenon in which gas from outside the chimney is drawn into the chimney by air (hereinafter the same applies).By installing a convection structure, such as a cylindrical structure, to create forced convection, better heat exchange characteristics can be achieved. The object of the present invention is to provide a gas condensing device having the following features.

以下にこの発明の一実施例について説明する。
第2図において図示されていない寒冷発生装置と
熱的に連結された(この場合、冷媒となる流体が
流れている)凝縮部2を被い、その上部及び下部
に少なくとも一組の流体入口4と流体出口5とを
有し、煙突効果を生じるような対流構造体3を適
当な取り付け冶具及び方法で設置した構成であ
る。この対流構造体3に関しては強制対流を誘起
する煙突効果を持つものであれば、どのような形
状にでも任意で良い。例えば図にあるように円筒
部の下部に絞り部6を付けた形状でも良いし、円
筒部だけでも良い。流体入口4と流体出口5につ
いても、その形状・寸法・数などは任意で良い。
また、この対流構造体3は凝縮部2に取り付けて
も、他のもの、例えば凝縮タンク1等に取り付け
ても良く、取り付けに当つては、凝縮部2あるい
は凝縮タンク1等と熱的に絶縁されていてもされ
てなくても良い。
An embodiment of the present invention will be described below.
It covers a condensing section 2 which is thermally connected to a cold generation device (not shown in FIG. 2) (in this case, a fluid serving as a refrigerant is flowing therethrough), and has at least one set of fluid inlets 4 at its upper and lower parts. In this configuration, a convection structure 3 having a fluid outlet 5 and a chimney effect is installed using an appropriate mounting jig and method. The convection structure 3 may have any shape as long as it has a chimney effect that induces forced convection. For example, as shown in the figure, the shape may be a cylindrical portion with a converging portion 6 attached to the lower part, or the cylindrical portion alone may be used. The shape, size, number, etc. of the fluid inlet 4 and fluid outlet 5 may be arbitrary.
Further, this convection structure 3 may be attached to the condensing section 2 or to another object, such as the condensing tank 1, etc., and when attached, it is necessary to thermally insulate it from the condensing section 2 or the condensing tank 1, etc. It doesn't have to be done or not.

上記で説明したように構成することにより、図
示されていない寒冷発生装置と熱的に連結された
凝縮部2と接触した気相部1aの気体は、凝縮熱
伝達によつて、熱交換をし、より低温の気体とな
り降下するかあるいは液化して落下することにな
る。この際、対流構造体3の内外で圧力差を生じ
煙突効果によつて、流体入口4より気体が内部に
引き込まれることになる。この時、気体が引き込
まれることによつて出来る流れは、対流構造体3
の存在によつて絞られることになり、通常の自然
対流による流れより、流速が大きくなり、強制対
流とみなせる流れとなる。従つて、凝縮部2の周
囲に強制的な流れが生じることになり、この強制
対流によつて、凝縮部2と気体との熱交換特性が
良好となる。また、凝縮部2に液膜が生じたなら
ば、強制対流がこれを除去する作用をし、非常に
良好な熱交換特性が得られることになる。
With the configuration as described above, the gas in the gas phase portion 1a that comes into contact with the condensing portion 2 which is thermally connected to a cold generation device (not shown) exchanges heat through condensation heat transfer. , it becomes a cooler gas and falls, or it liquefies and falls. At this time, a pressure difference is created between the inside and outside of the convection structure 3, and gas is drawn into the interior through the fluid inlet 4 due to the chimney effect. At this time, the flow created by the gas being drawn into the convection structure 3
The presence of this convection causes the flow to become constricted, resulting in a flow that is faster than normal natural convection, resulting in a flow that can be considered forced convection. Therefore, a forced flow is generated around the condensing section 2, and this forced convection improves the heat exchange characteristics between the condensing section 2 and the gas. Furthermore, if a liquid film forms in the condensing section 2, forced convection acts to remove it, resulting in very good heat exchange characteristics.

上記の実施例以外にも例えば第3図、第4図の
ように、種々の形状が考えられる。つまり前述の
ことは流体の流れを機械的・電気的な動力による
送風機構によつて作るのではなく、煙突効果を利
用して誘起させるような対流構造体を設けたガス
凝縮装置全般に渡つて適用されるものである。
In addition to the embodiments described above, various shapes can be considered, for example, as shown in FIGS. 3 and 4. In other words, the above applies to all gas condensing devices equipped with a convection structure that uses the chimney effect to induce fluid flow, rather than using a mechanically or electrically powered blower mechanism. applicable.

この発明によれば、機械的・電気的動力による
送風機構の取り付けが出来ない場合、及び不利な
場合等にこの発明を適用することにより、良好な
熱交換特性が得られる。また、従来と比べ送風機
構を含めて考えた場合装置のコンパクト化、安価
が計れる。
According to the present invention, good heat exchange characteristics can be obtained by applying the present invention to cases where it is impossible or disadvantageous to install a mechanically or electrically powered air blowing mechanism. Furthermore, compared to the conventional method, the device can be made more compact and inexpensive when considering the blower mechanism.

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

第1図は、従来のガス凝縮装置を示す断面側面
図、第2図は、この発明の一実施例のガス凝縮装
置を示す断面側面図、第3図、第4図はそれぞれ
他の実施例を示す断面側面図である。 図中、1は凝縮タンク、1aは気相部、1bは
液相部、2は凝縮部、3は対流構造体、4は流体
入口、5は流体出口、6は絞り部である。なお図
中同一符号は同一又は相当部分を示す。
FIG. 1 is a cross-sectional side view showing a conventional gas condensing device, FIG. 2 is a cross-sectional side view showing a gas condensing device according to an embodiment of the present invention, and FIGS. 3 and 4 are respective examples of other embodiments. FIG. In the figure, 1 is a condensation tank, 1a is a gas phase part, 1b is a liquid phase part, 2 is a condensation part, 3 is a convection structure, 4 is a fluid inlet, 5 is a fluid outlet, and 6 is a constriction part. Note that the same reference numerals in the figures indicate the same or equivalent parts.

Claims (1)

【特許請求の範囲】 1 凝縮タンクの気相部に凝縮部を配設するガス
凝縮装置において、凝縮部を被う対流構造体を設
けたことを特徴とするガス凝縮装置。 2 対流構造体の上部および下部に少なくとも一
組の流体入口と流体出口とを設けたことを特徴と
する特許請求の範囲第1項記載のガス凝縮装置。
[Scope of Claims] 1. A gas condensing device in which a condensing section is disposed in a gas phase portion of a condensing tank, characterized in that a convection structure covering the condensing section is provided. 2. The gas condensing device according to claim 1, wherein at least one set of a fluid inlet and a fluid outlet are provided at the upper and lower parts of the convection structure.
JP210282A 1982-01-08 1982-01-08 Gas condenser Granted JPS58120071A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP210282A JPS58120071A (en) 1982-01-08 1982-01-08 Gas condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP210282A JPS58120071A (en) 1982-01-08 1982-01-08 Gas condenser

Publications (2)

Publication Number Publication Date
JPS58120071A JPS58120071A (en) 1983-07-16
JPH0126474B2 true JPH0126474B2 (en) 1989-05-24

Family

ID=11519974

Family Applications (1)

Application Number Title Priority Date Filing Date
JP210282A Granted JPS58120071A (en) 1982-01-08 1982-01-08 Gas condenser

Country Status (1)

Country Link
JP (1) JPS58120071A (en)

Also Published As

Publication number Publication date
JPS58120071A (en) 1983-07-16

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