JPS6312641B2 - - Google Patents
Info
- Publication number
- JPS6312641B2 JPS6312641B2 JP58168777A JP16877783A JPS6312641B2 JP S6312641 B2 JPS6312641 B2 JP S6312641B2 JP 58168777 A JP58168777 A JP 58168777A JP 16877783 A JP16877783 A JP 16877783A JP S6312641 B2 JPS6312641 B2 JP S6312641B2
- Authority
- JP
- Japan
- Prior art keywords
- propellant
- multilayer
- discharge pipe
- tank body
- cylinders
- 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
Links
- 239000007788 liquid Substances 0.000 claims description 26
- 238000000926 separation method Methods 0.000 claims description 5
- 230000037431 insertion Effects 0.000 claims description 2
- 238000003780 insertion Methods 0.000 claims description 2
- 239000003380 propellant Substances 0.000 description 32
- 238000010586 diagram Methods 0.000 description 3
- 230000001133 acceleration Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
Landscapes
- Degasification And Air Bubble Elimination (AREA)
- Loading And Unloading Of Fuel Tanks Or Ships (AREA)
Description
【発明の詳細な説明】
本発明は、推薬タンクの排出口から常に液体の
みを排出し得るようにした気液分離装置に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a gas-liquid separation device that can always discharge only liquid from the outlet of a propellant tank.
無重力下の宇宙では、常に加速度が微小g〜数
gの範囲で変動するため、推薬タンク内の液体は
不安定となり、液面を固定することは難しい。従
つて、タンク内の液体には気体が混入するので、
推薬タンクの排出口から常に液体のみを取出すた
めの気液分離装置が必要となる。 In space, where there is no gravity, acceleration constantly fluctuates in the range of micrograms to several grams, making the liquid in the propellant tank unstable and making it difficult to fix the liquid level. Therefore, gas is mixed into the liquid in the tank, so
A gas-liquid separator is required to always extract only liquid from the outlet of the propellant tank.
斯かる従来の気液分離装置の例は第1図及び第
2図に示されている。 Examples of such conventional gas-liquid separators are shown in FIGS. 1 and 2.
第1図中aはタンク本体、bはタンク本体a内
に収納されたダイヤフラム、cは推薬dの排出
口、eはダイヤフラムbを圧縮するための加圧ガ
スであり、ダイヤフラムbが加圧ガスeにより圧
縮されて推薬dが排出口cより排出される。しか
し、斯かる従来装置では大型化が難しく、ダイヤ
フラムbの信頼性に欠け、再使用ができない、等
の欠点があつた。 In Fig. 1, a is the tank body, b is the diaphragm housed in the tank body a, c is the discharge port for the propellant d, and e is pressurized gas for compressing the diaphragm b. The propellant d is compressed by the gas e and is discharged from the discharge port c. However, such conventional devices have drawbacks such as difficulty in increasing their size, lack of reliability of diaphragm b, and inability to reuse.
又、第2図中fはゴム製のブラダであり、図中
第1図に示す符号と同一の符号のものは同一のも
のを示す。本装置ではブラダf中は閉じ込められ
た推薬は、加圧ガスeで圧縮され、排出口cから
排出される。しかし、該従来装置では、ブラダf
はゴム製であるため、推薬の種類によつては使用
することができず、大型化できないうえ、ゴムの
信頼性に欠け、再使用不可能である、等の欠点が
あつた。 Further, f in FIG. 2 is a rubber bladder, and the same reference numerals as those shown in FIG. 1 indicate the same parts. In this device, the propellant trapped in the bladder f is compressed by the pressurized gas e and is discharged from the discharge port c. However, in the conventional device, the bladder f
Since it is made of rubber, it cannot be used with some types of propellant, cannot be made larger, and has disadvantages such as lack of reliability of rubber and being unable to be reused.
本発明は、大型化可能で信頼性に富み、再使用
可能な気液分離装置を提供することを目的として
なしたもので、タンク本体に一端を挿入された排
出管と、該排出管の挿入部を包囲するようタンク
本体内に取付けられ且つ多数の小孔を有する複数
の孔あき多層円筒とを備え、孔あき多層円筒間の
間隙を排出管側から外側に向い順次大きく構成し
ている。 The present invention was made for the purpose of providing a gas-liquid separation device that can be enlarged, is highly reliable, and reusable, and includes a discharge pipe whose one end is inserted into a tank body, and an insertion pipe into which the discharge pipe is inserted. A plurality of perforated multilayer cylinders are attached to the tank body so as to surround the tank body and have a large number of small holes, and the gaps between the perforated multilayer cylinders are gradually increased outward from the discharge pipe side.
以下、本発明の実施例を図面を参照しつつ説明
する。 Embodiments of the present invention will be described below with reference to the drawings.
タンク本体1に排出管2を接続すると共に、該
排出管2の一端側をタンク本体1内に挿入し、排
出管2の一端部に固着したサポート3に多数の小
孔のあいた複数の孔あき多層円筒4a,4b,4
c,4dを排出管2に対して略同心状に取付け
る。孔あき多層円筒は、排出管2と円筒4aとの
間隔をl1、円筒4aと円筒4bとの間隔をl2、円
筒4bと円筒4cとの間隔をl3、円筒4cと円筒
4dとの間隔をl4とすると、内側程間隔が小さく
なるようl1<l2<l3<l4とし、孔あき多層円筒4
a,4b,4c,4dの高さをh1、h2、h3、h4と
すると、内側程高さが高く且つタンク本体1内面
と孔あき多層円筒4a,4b,4c,4d端部と
の間隙が小さくなるよう、h1>h2>h3>h4にし、
孔あき多層円筒4a下端と4b下端とを結んだ直
線が水平線に対し傾斜する角度をα、孔あき多層
円筒4b下端と4c下端とを結んだ直線が水平線
に対し傾斜する角度をβ、孔あき多層円筒4c下
端と4d下端とを結んだ直線が水平線に対して傾
斜する角度をγとすると、0<α、β、γ<90に
形成する。なお、図中5は排出管2の推薬流入口
部に設けられた十字状の渦止め板、6はサポート
3,3間に設けられ、推薬をタンク本体1から排
出管2へ排出する排出口、7は推薬がタンク本体
1から孔あき多層円筒を通らず直接排出管2へ排
出しないよう設けた蓋板、8は多数の小孔が設け
られ孔あき多層円筒4a,4b,4c,4dが固
着された孔あき板である。又、多層円筒4a,4
b,4c,4dの小孔の大きさは0.001mm〜5.0mm
程度とし、小孔のピツチは0.0015mm〜5.5mmとす
る。 A discharge pipe 2 is connected to the tank body 1, one end of the discharge pipe 2 is inserted into the tank body 1, and a support 3 fixed to one end of the discharge pipe 2 is provided with a plurality of small holes. Multilayer cylinder 4a, 4b, 4
c and 4d are attached approximately concentrically to the discharge pipe 2. The perforated multilayer cylinder has the following dimensions: the distance between the discharge pipe 2 and the cylinder 4a is l 1 , the distance between the cylinders 4a and 4b is l 2 , the distance between the cylinders 4b and 4c is l 3 , and the distance between the cylinders 4c and 4d is If the interval is l 4 , then l 1 < l 2 < l 3 < l 4 so that the interval becomes smaller towards the inside, and the perforated multilayer cylinder 4
If the heights of a, 4b, 4c, and 4d are h 1 , h 2 , h 3 , and h 4 , the height is higher toward the inside, and the inner surface of the tank body 1 and the end portions of the perforated multilayer cylinders 4a, 4b, 4c, and 4d Set h 1 > h 2 > h 3 > h 4 so that the gap between
α is the angle at which the straight line connecting the lower ends of the perforated multilayer cylinders 4a and 4b is inclined with respect to the horizontal line, and β is the angle at which the straight line connecting the lower ends of the perforated multilayer cylinders 4b and 4c is inclined with respect to the horizontal line. If the angle at which the straight line connecting the lower end of the multilayer cylinder 4c and the lower end of the multilayer cylinder 4d is inclined with respect to the horizontal line is γ, then 0<α, β, and γ<90 are formed. In the figure, 5 is a cross-shaped vortex stopper plate provided at the propellant inlet of the discharge pipe 2, and 6 is a cross-shaped vortex stopper plate provided between the supports 3 and 3 to discharge the propellant from the tank body 1 to the discharge pipe 2. A discharge port 7 is a cover plate provided to prevent the propellant from passing through the perforated multilayer cylinder from the tank body 1 and being directly discharged into the discharge pipe 2, and 8 is a perforated multilayer cylinder 4a, 4b, 4c provided with a large number of small holes. , 4d are perforated plates to which are fixed. Moreover, the multilayer cylinders 4a, 4
The size of the small holes in b, 4c, and 4d is 0.001mm to 5.0mm.
The pitch of the small holes should be 0.0015mm to 5.5mm.
所要の推薬をタンク本体1から排出管2へ排出
する場合には、タンク本体1内に加圧ガスが供給
され、その圧力によつて推薬はタンク本体1から
排出管2へ排出される。而して孔あき多層円筒4
a,4b,4c,4dや孔あき板8が推薬中に浸
漬された状態の場合には、推薬は円筒及び孔あき
板の小孔を通り、排出口6から排出管2へ排出さ
れ、推薬中の気泡は孔あき多層円筒4a,4b,
4c,4d、孔あき板8によりトラツプされる。 When discharging the required propellant from the tank body 1 to the discharge pipe 2, pressurized gas is supplied into the tank body 1, and the propellant is discharged from the tank body 1 to the discharge pipe 2 due to the pressure. . Therefore, the perforated multilayer cylinder 4
When a, 4b, 4c, 4d or the perforated plate 8 are immersed in the propellant, the propellant passes through the cylinder and the small holes in the perforated plate and is discharged from the discharge port 6 into the discharge pipe 2. , the air bubbles in the propellant are perforated multilayer cylinders 4a, 4b,
4c, 4d, and are trapped by the perforated plate 8.
推薬が所定量まで減少すると、第5図に示すご
とく、最外層の孔あき多層円筒4dとタンク本体
1内面との間に液面Aが生じるが、この場合には
推薬は孔あき多層円筒内を適宜通り、排出管2へ
排出される。気泡は液面A及び多層円筒間でトラ
ツプされる。 When the propellant decreases to a predetermined amount, a liquid level A occurs between the outermost perforated multilayer cylinder 4d and the inner surface of the tank body 1, as shown in FIG. It passes through the cylinder as appropriate and is discharged to the discharge pipe 2. Air bubbles are trapped between the liquid level A and the multilayer cylinder.
更に推薬が減少すると、推薬は第5図に示すよ
うに、孔あき多層円筒4a,4b,4c,4d内
に保持され、推薬の表面張力により、多層円筒4
d,4cの下端部間に液面B、多層円筒4c,4
bの下端部間に液面Cが、多層円筒4b,4aの
下端部間に液面Dが、多層円筒4aの下端と排出
管2の側面との間に液面Eが夫々形成される。こ
の場合液面の表面張力は各多層円筒間の間隙l1、
l2、l3、l4で決まり、E>D>C>Bであるため、
先ず多層円筒4d,4c間の推薬が多層円筒4c
から、多層円筒4cと4bとの間の空間に排出さ
れ、次いで多層円筒4c,4b間の推薬が多層円
筒4bから、多層円筒4bと4aとの間の空間に
排出され、続いて多層円筒4b,4a間の推薬が
多層円筒4aと排出管2との間の空間に排出さ
れ、最後に多層円筒4aと排出管2との間の推薬
が排出管2へ排出される。従つて推薬は中心に向
つて流れるため、推薬の排出は良好に行われる。
推薬中の気泡は推薬が各多層円筒を通過する際、
各多層円筒間の空間にトラツプされる。又、表面
張力による液面B,C,D,Eが多層円筒間に生
じた場合にはタンク本体1内面から推薬が分離さ
れるため、外部から推薬中に侵入する熱を少なく
することができ、液の蒸発量が減少する。 When the propellant decreases further, the propellant is retained in the perforated multilayer cylinders 4a, 4b, 4c, and 4d, as shown in FIG. 5, and the surface tension of the propellant causes the multilayer cylinder 4 to
There is a liquid level B between the lower ends of the multilayer cylinders 4c and 4c.
A liquid level C is formed between the lower ends of the multilayer cylinders 4b and 4a, a liquid level D is formed between the lower ends of the multilayer cylinders 4b and 4a, and a liquid level E is formed between the lower ends of the multilayer cylinder 4a and the side surface of the discharge pipe 2. In this case, the surface tension of the liquid surface is determined by the gap l 1 between each multilayer cylinder,
It is determined by l 2 , l 3 and l 4 , and since E>D>C>B,
First, the propellant between the multilayer cylinders 4d and 4c is the multilayer cylinder 4c.
The propellant between the multilayer cylinders 4c and 4b is then discharged from the multilayer cylinder 4b into the space between the multilayer cylinders 4b and 4a, and then The propellant between 4b and 4a is discharged into the space between the multilayer cylinder 4a and the discharge pipe 2, and finally the propellant between the multilayer cylinder 4a and the discharge pipe 2 is discharged into the discharge pipe 2. Therefore, the propellant flows toward the center, so that the propellant can be discharged well.
Air bubbles in the propellant are formed when the propellant passes through each multilayer cylinder.
It is trapped in the space between each multilayer cylinder. In addition, when liquid levels B, C, D, and E are generated between the multilayer cylinders due to surface tension, the propellant is separated from the inner surface of the tank body 1, so that the heat entering the propellant from the outside can be reduced. This reduces the amount of liquid evaporation.
なお、本発明の実施例においては孔あき多層円
筒を4組設ける場合について説明したが複数組な
ら何組設けても実施し得ること、加速度レベルが
0g〜0.3g位のLH2、LO2等のの低沸点推薬に
対して特に有効であるが、それ以外の推薬に対し
ても適用できること、その他、本発明の要旨を逸
脱しない範囲内で種々変更を加え得ること、等は
勿論である。 In addition, in the embodiment of the present invention, the case where four sets of perforated multilayer cylinders are provided has been described, but it is possible to implement any number of sets of multilayer cylinders with multiple holes . Although it is particularly effective for low boiling point propellants, it goes without saying that it can also be applied to other propellants, and that various other changes can be made without departing from the gist of the present invention. be.
本発明の気液分離装置によれば、加速度レベル
の低い条件下においてもガスフリーの液排出を行
うことができ、しかもタンク本体の大型化が可能
であり、又従来方式に比較してゴムや可動部がな
いため装置の耐久性が向上して信頼性が高まり、
更には再使用が可能で経済的である、等の優れた
効果を奏し得る。 According to the gas-liquid separator of the present invention, it is possible to perform gas-free liquid discharge even under conditions of low acceleration level, and the tank body can be made larger, and compared to conventional systems, it is possible to perform gas-free liquid discharge. Since there are no moving parts, the equipment is more durable and reliable.
Furthermore, it can exhibit excellent effects such as being reusable and economical.
第1図は従来の気液分離装置の一例の説明図、
第2図は従来の気液分離装置の他の例の説明図、
第3図は本発明の気液分離装置の一実施例の説明
図、第4図は第3図の−方向矢視図、第5図
は第3図の気液分離装置により推薬が排出される
状態の説明図である。
図中1はタンク本体、2は排出管、4a,4
b,4c,4dは孔あき多層円筒を示す。
FIG. 1 is an explanatory diagram of an example of a conventional gas-liquid separation device,
FIG. 2 is an explanatory diagram of another example of a conventional gas-liquid separation device,
Fig. 3 is an explanatory diagram of one embodiment of the gas-liquid separator of the present invention, Fig. 4 is a view taken from the - direction arrow in Fig. 3, and Fig. 5 is a propellant discharged by the gas-liquid separator of Fig. 3. FIG. In the figure, 1 is the tank body, 2 is the discharge pipe, 4a, 4
b, 4c, and 4d indicate perforated multilayer cylinders.
Claims (1)
部を包囲するよう、多数の小孔を有する複数の孔
あき多層円筒を略同心状にタンク本体内に配設
し、孔あき多層円筒間の間隙を排出管側から外側
に向い順次大きくしたことを特徴とする気液分離
装置。1 A plurality of perforated multilayer cylinders having a large number of small holes are arranged approximately concentrically within the tank body so as to surround the insertion part of the discharge pipe whose one end is inserted into the tank body, and the holes between the perforated multilayer cylinders are A gas-liquid separation device characterized in that the gap gradually increases from the discharge pipe side outward.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58168777A JPS6061008A (en) | 1983-09-13 | 1983-09-13 | Gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58168777A JPS6061008A (en) | 1983-09-13 | 1983-09-13 | Gas-liquid separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6061008A JPS6061008A (en) | 1985-04-08 |
| JPS6312641B2 true JPS6312641B2 (en) | 1988-03-22 |
Family
ID=15874266
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58168777A Granted JPS6061008A (en) | 1983-09-13 | 1983-09-13 | Gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6061008A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20210100028A (en) * | 2020-02-04 | 2021-08-13 | 어플라이드 머티리얼즈 이스라엘 리미티드 | Method of examining specimens and system thereof |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0715546Y2 (en) * | 1991-12-12 | 1995-04-12 | タカラベルモント株式会社 | Support device for medical treatment table |
-
1983
- 1983-09-13 JP JP58168777A patent/JPS6061008A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20210100028A (en) * | 2020-02-04 | 2021-08-13 | 어플라이드 머티리얼즈 이스라엘 리미티드 | Method of examining specimens and system thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6061008A (en) | 1985-04-08 |
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