JPH0641798B2 - Gas-liquid two-phase fluid distributor - Google Patents
Gas-liquid two-phase fluid distributorInfo
- Publication number
- JPH0641798B2 JPH0641798B2 JP61176717A JP17671786A JPH0641798B2 JP H0641798 B2 JPH0641798 B2 JP H0641798B2 JP 61176717 A JP61176717 A JP 61176717A JP 17671786 A JP17671786 A JP 17671786A JP H0641798 B2 JPH0641798 B2 JP H0641798B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- gas
- outflow
- phase fluid
- cylindrical container
- 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 - Fee Related
Links
Landscapes
- Branch Pipes, Bends, And The Like (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は気液二相流体分配器、殊にボイラの蒸気・水二
相流体の分配に用いられる分配器、又は冷媒や化学プロ
セスにおける種々の気液二相流体を取扱う熱交換器など
に設けられる分配器に関する。Description: FIELD OF THE INVENTION The present invention relates to a gas-liquid two-phase fluid distributor, particularly a distributor used for distributing a steam / water two-phase fluid in a boiler, or a refrigerant or various gas in a chemical process. The present invention relates to a distributor provided in a heat exchanger that handles a liquid two-phase fluid.
従来の技術 従来の気液二相流体分配器を第2図及び第3図に基づい
て説明する。2. Description of the Related Art A conventional gas-liquid two-phase fluid distributor will be described with reference to FIGS. 2 and 3.
これらの図において、円筒容器21の一端は閉じており、
他端は直径が小さくなって流入管22が流体密に接続され
ている。そして、この円筒容器21の側壁には円筒中心か
ら放射状に多数の流出孔23が穿設され、これらの流出孔
23の夫々には中心が円筒容器21の軸に垂直な同一の断面
上にある流出管24がそれぞれ流体密に接続されている。In these figures, one end of the cylindrical container 21 is closed,
The other end has a smaller diameter and the inflow pipe 22 is fluid-tightly connected. A large number of outflow holes 23 are radially formed from the center of the cylinder on the side wall of the cylindrical container 21.
Outflow pipes 24 whose center is on the same cross section perpendicular to the axis of the cylindrical container 21 are fluid-tightly connected to the respective 23.
しかして、円筒容器21はその閉じた端面が上方に、流入
管22が下方になるように設置され、気液二相流体は流入
管22を通って下方から円筒容器21内に流入する。気液二
相流体は円筒容器21の内部において、気体と液体の密度
差のために気体と液体に分離し、流出孔23のレベルに液
面25が形成される。Then, the cylindrical container 21 is installed so that its closed end face is upward and the inflow pipe 22 is downward, and the gas-liquid two-phase fluid flows into the cylindrical container 21 from below through the inflow pipe 22. The gas-liquid two-phase fluid is separated into gas and liquid inside the cylindrical container 21 due to the difference in density between gas and liquid, and a liquid surface 25 is formed at the level of the outflow hole 23.
この液面25下の液体中には気泡が存在し、また気泡が下
方から液面25を破って上昇する際に液体をはね上げるの
で、液面25上方の気体中には液滴が存在するが、液面25
下の気泡が直接流出管24へ流出する量や液面25上の液滴
が直接流出管24へ流出する量は全体に比べると比較的少
なく、各流出管24へは、おもに液面25上から気体が、液
面25下から液体が、流出孔23を通って流出する。There are bubbles in the liquid below the liquid surface 25, and since the liquid splashes up when the bubbles break from the liquid surface 25 and rise, the liquid droplets exist in the gas above the liquid surface 25. Liquid level 25
The amount of bubbles below directly flowing out to the outflow pipe 24 and the amount of liquid droplets on the liquid level 25 directly outflowing to the outflow pipe 24 are relatively small compared to the whole, and each outflow pipe 24 is mainly on the liquid level 25. From the liquid, and liquid from below the liquid surface 25 flows out through the outflow hole 23.
このような従来の分配器において、流入管22から流入す
る気液二相流体の気体と液体とが一様に混合している
か、またはそれらに分布があっても流入管22の軸に対し
て対称、すなわち全周均一である場合には、円筒容器21
の内部の状態も全周均一になり、液面25は半径方向には
高低は生じることはあっても周方向には同じ高さとな
り、流出孔23に対する液面25の高さはすべての流出孔23
について同じになる。したがって、各流出管24へ流出す
る気体、液体の量はすべての流出管24で同じになり、気
液二相流体は均等に各流出管24へ分配される。In such a conventional distributor, the gas and the liquid of the gas-liquid two-phase fluid flowing in from the inflow pipe 22 are uniformly mixed, or even if they are distributed, with respect to the axis of the inflow pipe 22. In the case of symmetry, that is, the entire circumference is uniform, the cylindrical container 21
The inner state of the liquid is also uniform around the entire circumference, and although the liquid surface 25 may have heights in the radial direction, the liquid surface 25 has the same height in the circumferential direction, and the height of the liquid surface 25 relative to the outflow hole 23 is equal to that of all outflows. Hole 23
About the same. Therefore, the amount of gas and liquid flowing out to each outflow pipe 24 is the same in all outflow pipes 24, and the gas-liquid two-phase fluid is evenly distributed to each outflow pipe 24.
発明が解決しようとする問題点 しかしながら、このような従来の分配器においては、た
とえば流入管22の途中に曲りがある場合、この曲り部で
の遠心力によって密度が大きい液体は曲りの外側の方
へ、密度の小さい気体は曲り内側の方へ片寄った流れと
なるが、このように気体、液体が片寄ったままで円筒容
器21に流入した場合には、液面25にも片寄りが生じて全
周均一とはならず、たとえばある流出孔23の側には液面
25が低く、この流出孔23のほぼ全体が液面25上にあり、
反対側の流出孔23の側は液面25が高く、この流出孔23の
ほぼ全体が液面25下にあるといった状態になる。この場
合、流出管24には気体が多く流出し、反対側の流出管24
には液体が多く流出するので、気液二相流体の均一な分
配はできないという問題がある。DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention However, in such a conventional distributor, when there is a bend in the middle of the inflow pipe 22, for example, a liquid having a high density is generated on the outside of the bend due to the centrifugal force at the bend. The gas having a low density has a curved flow that is biased toward the inner side. However, when the gas and the liquid flow into the cylindrical container 21 while being biased in this way, the liquid level 25 is also biased and the total flow is lost. The circumference is not uniform.
25 is low, almost all of this outflow hole 23 is on the liquid level 25,
The liquid surface 25 is high on the side of the outflow hole 23 on the opposite side, and almost all of the outflow hole 23 is below the liquid surface 25. In this case, a large amount of gas flows out to the outflow pipe 24 and the outflow pipe 24 on the opposite side.
However, since a large amount of liquid flows out, there is a problem that the gas-liquid two-phase fluid cannot be uniformly distributed.
問題点を解決するための手段 そこで、本発明は、上記問題点を解決するために、上端
を閉じた円筒容器を垂直に立て、その下端に流入管を接
続するとともに、その側壁に円筒中心から放射状に多数
の流出孔を穿設し、これら各流出孔に流出管をそれぞれ
接続してなる気液二相流体分配器において、前記円筒容
器よりも小径の、上端が閉じた内筒を前記円筒容器の中
に同心的に配置するとともに、その下端を前記流入管に
接続し、かつこの内筒側壁の、前記流出孔よりも上方の
部分に多数の小孔を穿設したものである。Therefore, in order to solve the above-mentioned problems, the present invention, in order to solve the above-mentioned problems, vertically stands a cylindrical container with an upper end closed, connects an inflow pipe to the lower end thereof, and connects the side wall of the cylindrical container to the center of the cylinder. In a gas-liquid two-phase fluid distributor having a large number of radially extending outflow holes and connecting an outflow pipe to each of these outflow holes, an inner cylinder having a diameter smaller than that of the cylindrical container and having an upper end closed It is arranged concentrically in the container, has its lower end connected to the inflow pipe, and has a large number of small holes formed in a portion of the inner cylinder side wall above the outflow hole.
作用 このような手段によれば、流入管から流入した片寄った
流れの気液二相流体は、内筒側壁に穿設されている多数
の小孔の流動抵抗のために内筒内部で均一化され、前記
小孔を通って内筒外面と円筒容器内面との間に形成され
ている環状空間部を流れる際の流動抵抗によりさらに均
一化される。また、多数の小孔は流出孔よりも上方の内
筒側壁部分に穿設されているので、気液二相流体が流入
管ないで逆流しても、流出管での流動変動を増大させる
ことはない。By such means, the uneven flow of the gas-liquid two-phase fluid flowing in from the inflow pipe is made uniform inside the inner cylinder due to the flow resistance of the many small holes formed in the side wall of the inner cylinder. And is further homogenized by the flow resistance when flowing through the annular space formed between the outer surface of the inner cylinder and the inner surface of the cylindrical container through the small holes. In addition, since many small holes are formed in the side wall of the inner cylinder above the outflow hole, even if the gas-liquid two-phase fluid flows backward without the inflow pipe, the flow fluctuation in the outflow pipe is increased. There is no.
実施例 以下第1図を参照して、本発明の実施例について説明す
る。Embodiment An embodiment of the present invention will be described below with reference to FIG.
第1図において、円筒容器11は従来のものと同様で、上
端は閉じており、また下端は直径が小さくなって流入管
12が流体密に接続されている。そして、この円筒容器11
の側壁の下方部分には多数の流出孔13が円筒中心から放
射状に穿設され、これらの流出孔13には流出管14がそれ
ぞれ流体密に接続されている。この流出孔13及び流出管
14の横断面内での配置は従来の分配器と同様である。In FIG. 1, the cylindrical container 11 is the same as the conventional one, the upper end is closed, and the lower end has a smaller diameter so that the inflow pipe is
12 are fluid-tightly connected. And this cylindrical container 11
A large number of outflow holes 13 are radially formed in the lower part of the side wall of the cylinder from the center of the cylinder, and outflow pipes 14 are fluid-tightly connected to these outflow holes 13, respectively. This outflow hole 13 and outflow pipe
The arrangement of 14 in the cross section is similar to the conventional distributor.
しかして、円筒容器11の内部には、この円筒容器よりも
小径の内筒16が、同心的にかつその閉じている上端が流
出孔13のレベルよりも上方になるようにして配置され、
かつその下端が流入管12に流体密に接続されている。そ
して、この内筒側壁の、流出孔13よりも上方の部分には
多数の小孔17が内筒16の円周方向及び軸方向に一様な密
度で穿設されている。Then, inside the cylindrical container 11, an inner cylinder 16 having a diameter smaller than that of the cylindrical container is concentrically arranged so that its closed upper end is located above the level of the outflow hole 13,
Moreover, the lower end thereof is fluid-tightly connected to the inflow pipe 12. A large number of small holes 17 are formed in the inner cylinder side wall above the outflow holes 13 at a uniform density in the circumferential direction and the axial direction of the inner cylinder 16.
したがって、流入管12から内筒16へ片寄って流入した気
液二相流体は、この内筒16の側壁に穿設している多数の
小孔17の流動抵抗のために内筒内部で均一化され、さら
に小孔17を通って内筒16の外面と円筒容器11の内面との
間に形成されている環状空間部18を流れる際の流動抵抗
によってより一層均一化されるので、液面15はすべての
流出孔13に対して同じ高さになり、気液二相流体はすべ
ての流出管14へ均等に分配される。Therefore, the gas-liquid two-phase fluid flowing from the inflow pipe 12 to the inner cylinder 16 in one direction is made uniform inside the inner cylinder due to the flow resistance of the many small holes 17 formed in the side wall of the inner cylinder 16. Further, the liquid surface 15 is further homogenized by the flow resistance when flowing through the annular space 18 formed between the outer surface of the inner cylinder 16 and the inner surface of the cylindrical container 11 through the small hole 17. Have the same height for all outflow holes 13, and the gas-liquid two-phase fluid is evenly distributed to all outflow pipes 14.
また、気液二相流体が流入管12内で逆流しても、流出管
14での流量変動を増大させることはない。すなわち、気
液二相流体の流れは本質的に脈動を伴うものであり、気
体や液体の流量が増減したり、ときには逆流することも
あるが、液面15は環状空間部18の流出孔13のレベルに形
成され、この位置は内筒16の側壁に穿設された小孔17よ
り低いので、流入管12内で逆流が起こっても、環状空間
部18の液面15下に溜っている液体が小孔17を通って流入
管12へ逆流することはない。Even if the gas-liquid two-phase fluid flows backward in the inflow pipe 12, the outflow pipe
It does not increase flow fluctuations at 14. That is, the flow of the gas-liquid two-phase fluid is inherently accompanied by pulsation, and the flow rate of gas or liquid may increase or decrease, and sometimes flow backward, but the liquid level 15 is the outflow hole 13 of the annular space portion 18. Since this position is lower than the small hole 17 formed in the side wall of the inner cylinder 16, even if a backflow occurs in the inflow pipe 12, it is accumulated below the liquid surface 15 of the annular space portion 18. The liquid does not flow back into the inflow pipe 12 through the small hole 17.
したがって、気液二相流体が流入管12で逆流していると
きには液面15下の流体が流出管14へ流出するものの、液
面15は流出孔13の下の縁より下がることはなく、次に流
入管12内で気液二相流体が順流になって小孔17を通り環
状空間部18に入ると、気体は直接流出孔13から流出管14
へ流出し、液体は液面15に落下して液面15を上昇させて
流出孔13から流出管14へ流出する。このように、液面15
の低下がほとんどないので、流入管12での気液二相流体
の逆流が流出管14での流量変動を増大させることはな
い。Therefore, when the gas-liquid two-phase fluid is flowing backward in the inflow pipe 12, the fluid below the liquid level 15 flows out to the outflow pipe 14, but the liquid level 15 does not go below the lower edge of the outflow hole 13, and When the gas-liquid two-phase fluid becomes a forward flow in the inflow pipe 12 through the small hole 17 and enters the annular space 18, the gas is directly discharged from the outflow hole 13 to the outflow pipe 14.
The liquid drops onto the liquid surface 15 to raise the liquid surface 15 and flow out from the outflow hole 13 to the outflow pipe 14. Thus, the liquid level 15
The reverse flow of the gas-liquid two-phase fluid in the inflow pipe 12 does not increase the flow rate fluctuation in the outflow pipe 14 because there is almost no decrease in the flow rate.
発明の効果 以上詳述したように、本発明によれば、内筒の側壁に穿
設した多数の小孔及びこの内筒外面と円筒容器内面との
間に形成される環状空間部におけるそれぞれの流動抵抗
によって気液二相流体の片寄りをなくして均一化し、気
液二相流体をすべての流出管へ均等に分配することがで
きる。また、多数の小孔は流出孔よりも上方の内筒側壁
部分に穿設されているので、気液二相流体が流入管内で
逆流しても、流出管での流動変動を増大させることはな
い。EFFECTS OF THE INVENTION As described in detail above, according to the present invention, a large number of small holes formed in the side wall of the inner cylinder and each of the annular spaces formed between the outer surface of the inner cylinder and the inner surface of the cylindrical container. Due to the flow resistance, the gas-liquid two-phase fluid can be made uniform without any deviation, and the gas-liquid two-phase fluid can be evenly distributed to all the outflow pipes. Moreover, since many small holes are formed in the inner cylinder side wall portion above the outflow hole, even if the gas-liquid two-phase fluid flows backward in the inflow pipe, it is possible to increase the flow fluctuation in the outflow pipe. Absent.
【図面の簡単な説明】 第1図は本発明による気液二相流体分配器の一例を示す
縦断面図、第2図は従来の気液二相流体分配器を示す縦
断面図、第3図は第2図のIII−III線断面図である。 11……円筒容器、12……流入管、13……流出孔、14……
流出管、15……液面、16……内筒、17……小孔、18……
環状空間部。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a vertical sectional view showing an example of a gas-liquid two-phase fluid distributor according to the present invention, and FIG. 2 is a vertical sectional view showing a conventional gas-liquid two-phase fluid distributor. The drawing is a sectional view taken along the line III-III in FIG. 11 …… Cylindrical container, 12 …… Inflow pipe, 13 …… Outflow hole, 14 ……
Outflow pipe, 15 …… liquid level, 16 …… inner cylinder, 17 …… small hole, 18 ……
Ring space part.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 山本 健次郎 東京都千代田区丸の内2丁目5番1号 三 菱重工業株式会社内 (56)参考文献 実公 昭56−1600(JP,Y2) ─────────────────────────────────────────────────── ─── Continued Front Page (72) Kenjiro Yamamoto Inventor Kenjiro Yamamoto 2-5-1, Marunouchi, Chiyoda-ku, Tokyo Sanryo Heavy Industries Co., Ltd. (56) References: Jikho Sho 56-1600 (JP, Y2)
Claims (1)
下端に流入管を接続するとともに、その側壁に円筒中心
から放射状に多数の流出孔を穿設し、これらの各流出孔
に流出管をそれぞれ接続してなる気液二相流体分配器に
おいて、前記円筒容器よりも小径の、上端が閉じた内筒
を前記円筒容器の中に同心的に配置するとともに、その
下端を前記流入管に接続し、かつこの内筒側壁の、前記
流出孔よりも上方の部分に多数の小孔を穿設したことを
特徴とする気液二相流体分配器。1. A cylindrical container having a closed upper end is erected vertically, an inflow pipe is connected to the lower end thereof, and a large number of outflow holes are radially formed in the side wall of the cylindrical container from the center of the cylinder so that the outflow holes flow out to the respective outflow holes. In a gas-liquid two-phase fluid distributor in which pipes are connected to each other, an inner cylinder having a diameter smaller than that of the cylindrical container and having an upper end closed is concentrically arranged in the cylindrical container, and the lower end thereof is the inflow pipe. A gas-liquid two-phase fluid distributor characterized in that a large number of small holes are formed in a portion of the inner cylinder side wall above the outflow hole.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61176717A JPH0641798B2 (en) | 1986-07-29 | 1986-07-29 | Gas-liquid two-phase fluid distributor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61176717A JPH0641798B2 (en) | 1986-07-29 | 1986-07-29 | Gas-liquid two-phase fluid distributor |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6334393A JPS6334393A (en) | 1988-02-15 |
JPH0641798B2 true JPH0641798B2 (en) | 1994-06-01 |
Family
ID=16018534
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61176717A Expired - Fee Related JPH0641798B2 (en) | 1986-07-29 | 1986-07-29 | Gas-liquid two-phase fluid distributor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0641798B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4454779B2 (en) * | 2000-03-31 | 2010-04-21 | 株式会社日阪製作所 | Plate heat exchanger |
JP4749054B2 (en) * | 2005-06-22 | 2011-08-17 | エドワーズ株式会社 | Turbomolecular pump and method of assembling turbomolecular pump |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5933356Y2 (en) * | 1979-06-19 | 1984-09-17 | 東芝熱器具株式会社 | steam iron |
-
1986
- 1986-07-29 JP JP61176717A patent/JPH0641798B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPS6334393A (en) | 1988-02-15 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |