JPS6236503Y2 - - Google Patents
Info
- Publication number
- JPS6236503Y2 JPS6236503Y2 JP1981106198U JP10619881U JPS6236503Y2 JP S6236503 Y2 JPS6236503 Y2 JP S6236503Y2 JP 1981106198 U JP1981106198 U JP 1981106198U JP 10619881 U JP10619881 U JP 10619881U JP S6236503 Y2 JPS6236503 Y2 JP S6236503Y2
- Authority
- JP
- Japan
- Prior art keywords
- slope
- angle
- line
- plate
- ridgeline
- 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 6
- 238000005452 bending Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000009792 diffusion process Methods 0.000 description 4
- 238000004804 winding Methods 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002985 plastic film Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011081 inoculation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Landscapes
- Gas Separation By Absorption (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Description
本考案は、波形板の板面に沿い水を流下せしめ
る方式の気液接触用充填板に関するもので、その
目的は循環水の拡散をはかり、気液接触効率を高
めることにある。
従来から用いられている斯種の充填板には、プ
ラスチツクシート等から成る波形板の稜線が垂直
に立つた状態で該波形板を支持し、その板面に沿
い冷却水を流下せしめるようにしたものがある。
しかしながら、この場合には板面に付着した冷却
水は縦方向にのみ流れ、横方向には殆ど拡散しな
いため気液接触効率が低いので、波形板の斜面に
凹凸を設けて横方向の拡散を行なわせるようにし
たものもあるが、その効果は充分ではない。
そこで之を改善すべく波形板の稜線を傾斜させ
ることが提案されているが単に任意の角度傾斜さ
せただけでは充分な効果は期待できない。その状
態を第1図によつて説明すると、プラスチツクシ
ート等から成りW状に屈曲した波形板1の斜面同
士の夾角2αが稜線の傾斜角度θに対して過度に
大きいときは例えば斜面12の一点Oに落下した
水滴が該点Oから板面と直交する下方へ稜線2
3、斜面13、稜線24、斜面14、稜線25、
斜面15を経て線Pに沿つて直下方へ流下するの
で横方向への拡散は殆ど行なわれず、また上記夾
角2αが稜線の傾斜角度θに対して過度に小さい
ときは前記斜面12の一点Oに落下した水滴は稜
線22のQ線に沿つて流下するので斜面12上で
の他方向への拡散は殆ど行なわれない。
この拡散原理を第7図に基づいて更に詳しく説
明する。図中Vは斜面12の一点Oを通る垂線、
P1は板面と直交して垂直下方へ延びた線Pが稜線
23と交差する点であり、線Pは垂線Vに対して
角度β傾斜している。また、Q1は稜線22と平
行するQ線上で点であり、垂線V上の一点O1を
通る線P1−O1,Q1−O1はそれぞれ垂線Vと直交
している。このようにして、斜面12上に点O,
P1,Q1を結んだ三角面を想定したとき、傾斜角
度βがθより過度に大きいときには、O点に落下
した水滴は線O−Q1(又は稜線22)に沿つて
流下することになる。逆に傾斜角度βがθ1より
過度に小さいときには、線O−P1に沿つて直ちに
稜線23に達し、いずれの場合にも、斜面12に
落下した水滴を拡散させることができず、気液接
種不良が生じる。
本考案は、上述の如き欠点を改善したもので、
板状体を屈曲して平坦な斜面を形成した波形板の
各斜面の稜線を垂線Vに対して角度θ傾斜させた
とき、斜面同士の夾角を2α、斜面上の一点から
板面と直交して斜面に沿つて直下する線Pと垂線
Vとのなす角度をβとしてθ=βとなるように角
度αを設定したことを特徴とする気液接触用充填
板に係る。
以下これを図示の実施例によつて説明すると、
第2図乃至第4図はW状に屈曲した第1図の波形
板に関する説明図であつて、これらの図では説明
の便宜上、第1図の点Oを稜線22上に移して示
し、そしてhは板面に沿つて直下する線Pが相隣
る二稜線と交わる二点間の垂直成分長さ、lは屈
曲した波形のピツチ、pは上記底辺から頂点に相
当する稜線までの高さ即ち、波形板の幅寸法を示
す。
第2図から sinθ=l/h …(1)
第3図から tanα=l/p ∴l=p tanα …(2)
上記(1)に(2)を代入して
sinθ=p tanα/h ∴h=p tanα/si
nθ…(3)
第4図から tanβ=p/h …(4)
上記(3)を(4)に代入して
tanβ=p/p tanα/sinθ=p sinθ/
p tanα=sinθ/tanα…(5)
∴tanαsinθ/tanβ …(6)
この(6)式からθ=βとなるαの価を求めると次
表の如くなる。
The present invention relates to a packed plate for gas-liquid contact that allows water to flow down along the surface of a corrugated plate, and its purpose is to diffuse the circulating water and increase the gas-liquid contact efficiency. Conventionally used filling plates of this kind include a corrugated plate made of a plastic sheet or the like, in which the corrugated plate is supported with its ridge line standing vertically, and cooling water is allowed to flow down along the plate surface. There is something.
However, in this case, the cooling water adhering to the plate surface flows only in the vertical direction and hardly diffuses in the horizontal direction, resulting in low gas-liquid contact efficiency. Therefore, unevenness is provided on the slope of the corrugated plate to reduce the horizontal diffusion. There are some methods that have been made to do this, but the effect is not sufficient. In order to improve this, it has been proposed to tilt the ridgeline of the corrugated plate, but simply tilting it at an arbitrary angle cannot expect a sufficient effect. This state will be explained with reference to FIG. 1. When the included angle 2α between the slopes of the corrugated plate 1 made of plastic sheet etc. and bent in a W shape is excessively large with respect to the inclination angle θ of the ridgeline, for example, one point on the slope 12 The water droplets that fell on point O move downward from point O to the ridge line 2 perpendicular to the board surface.
3, slope 13, ridgeline 24, slope 14, ridgeline 25,
Since it flows directly downward along the line P via the slope 15, there is almost no lateral diffusion, and if the included angle 2α is too small with respect to the inclination angle θ of the ridgeline, it flows to a point O on the slope 12. Since the falling water droplets flow down along the Q line of the ridgeline 22, they hardly diffuse in other directions on the slope 12. This diffusion principle will be explained in more detail based on FIG. In the figure, V is a perpendicular line passing through one point O of the slope 12,
P 1 is a point where a line P extending perpendicularly to the plate surface and extending vertically downward intersects the ridge line 23, and the line P is inclined at an angle β with respect to the perpendicular line V. Moreover, Q 1 is a point on the Q line parallel to the ridgeline 22, and lines P 1 -O 1 and Q 1 -O 1 passing through one point O 1 on the perpendicular line V are orthogonal to the perpendicular line V, respectively. In this way, the point O on the slope 12,
Assuming a triangular surface connecting P 1 and Q 1 , if the inclination angle β is excessively larger than θ, the water droplet falling at point O will flow down along the line O-Q 1 (or the ridge line 22). Become. On the other hand, when the inclination angle β is excessively smaller than θ 1 , the ridge line 23 is immediately reached along the line O-P 1 , and in either case, the water droplets that have fallen onto the slope 12 cannot be diffused, and the gas-liquid Inoculation defects occur. The present invention improves the above-mentioned drawbacks,
When the ridgeline of each slope of a corrugated plate formed by bending a plate to form a flat slope is inclined at an angle θ with respect to the perpendicular V, the included angle between the slopes is 2α, and the slope is perpendicular to the plate surface from one point on the slope. The present invention relates to a filling plate for gas-liquid contact characterized in that the angle α is set so that θ=β, where β is the angle between a line P directly below the slope and a perpendicular line V. This will be explained below using the illustrated example.
2 to 4 are explanatory diagrams of the corrugated plate of FIG. 1 bent in a W shape, and in these figures, for convenience of explanation, point O in FIG. 1 is moved onto the ridge line 22, and h is the vertical component length between two points where a line P directly down along the plate surface intersects with two adjacent ridgelines, l is the pitch of the curved waveform, and p is the height from the base to the ridgeline corresponding to the apex. That is, it shows the width dimension of the corrugated plate. From Figure 2, sinθ=l/h...(1) From Figure 3, tanα=l/p ∴l=p tanα...(2) Substituting (2) into (1) above, sinθ=p tanα/h ∴ h=p tanα/si
nθ...(3) From Figure 4, tanβ=p/h...(4) Substituting the above (3) into (4), tanβ=p/p tanα/sinθ=p sinθ/
p tanα=sinθ/tanα...(5) ∴tanαsinθ/tanβ...(6) From equation (6), the value of α that makes θ=β is calculated as shown in the following table.
【表】【table】
【表】
即ち、β=θとなるαはθが0゜を越え90゜未
満で成立するが、実用的には稜線の傾斜角度θを
10゜〜60゜の範囲内で適宜設定するのが好まし
い。
尚、波形板の形状は第1図の如きW状屈曲のみ
に限らず、第5図及び第6図に示す如く波の形を
平面部3と斜面部4との連続した断面台形にして
もよい。何れの場合にも波形屈曲の斜面部に凹凸
模様を設けてもよい。
上記波形板は多数枚を1枚毎に稜線の方向を反
対にして互に交叉するように集積し結合するか、
或は渦巻状に且つ各巻相互間に帯状の隔離材を入
れて巻くか、或は稜線の向きを反対にして2枚の
波形板を重ねた状態で渦巻状に巻くなど、各種の
施工が可能であり、また波形板に間隔保持用の突
部を設けてこの突部を互に接して結合する。
以上に述べた如く、本考案の充填板は、波形板
の各斜面の稜線を垂線Vに対して角度θ傾斜さ
せ、また斜面上の一点から板面と直交して斜面に
沿つて直下する線Pと垂線Vとのなす角度βをθ
=βとしたので、斜面に落下した水滴を縦・横両
方向に万遍なく拡散させることができる。即ち、
第7図において、θ=βであると点O,P1,Q1
を結んだ三角面は二等辺三角形となり、点Oに落
下した水滴はこの三角面の中心を通つて斜面12
上を流下する。このため、水滴は谷の稜線22に
沿つて流下することもなく、また山の稜線23に
直ちに達することもないので、任意の角度に傾斜
させた従来の波形板と比較して格段に気液接触効
率を高めることができた。[Table] In other words, α such that β = θ is satisfied when θ exceeds 0° and is less than 90°, but in practical terms, the inclination angle θ of the ridgeline
It is preferable to set the angle appropriately within the range of 10° to 60°. Note that the shape of the corrugated plate is not limited to the W-shaped bend as shown in Fig. 1, but also the shape of the wave can be made into a continuous trapezoidal cross-section with a plane part 3 and a slope part 4 as shown in Figs. 5 and 6. good. In either case, an uneven pattern may be provided on the slope portion of the wave-shaped bend. The above-mentioned corrugated plates may be stacked and combined so that the ridge lines of each plate are in opposite directions so as to intersect with each other, or
Alternatively, various construction methods are possible, such as winding in a spiral shape with a band-shaped isolation material between each winding, or winding in a spiral shape with two corrugated plates stacked on top of each other with the ridges facing in opposite directions. Further, protrusions for maintaining the distance are provided on the corrugated plate, and the protrusions are brought into contact with each other and connected. As described above, in the filling plate of the present invention, the ridgeline of each slope of the corrugated plate is inclined at an angle θ with respect to the perpendicular line V, and a line that is perpendicular to the plate surface and directly down along the slope from one point on the slope The angle β between P and the perpendicular V is θ
= β, the water droplets falling on the slope can be evenly spread both vertically and horizontally. That is,
In Fig. 7, when θ=β, the points O, P 1 , Q 1
The triangular surface connecting them is an isosceles triangle, and the water droplet falling at point O passes through the center of this triangular surface and reaches the slope 12.
flowing down above. For this reason, water droplets do not flow down along the ridgeline 22 of the valley, nor do they immediately reach the ridgeline 23 of the mountain, so compared to the conventional corrugated plate tilted at an arbitrary angle, the water droplets are much easier to handle. We were able to increase the contact efficiency.
図面は本考案の実施例を示すもので、第1図は
波形板の斜視図、第2図乃至第4図は該波形板に
関する説明図で第2図は第1図の正面図、第3図
は第2図の矢印Y1方向の平面図、第4図は第1
図の左側面図、第5図は波の形状を変えた波形板
の正面図、第6図は第5図の矢印Y2方向の平面
図、第7図は水滴の拡散原理を説明するための説
明図である。
1は波形板、3は平面部、4は斜面部、10〜
15は斜面、20〜25は稜線である。
The drawings show an embodiment of the present invention, and FIG. 1 is a perspective view of a corrugated plate, FIGS. 2 to 4 are explanatory diagrams of the corrugated plate, and FIG. 2 is a front view of FIG. 1, and FIG. The figure is a plan view in the direction of arrow Y1 in figure 2, and figure 4 is a plan view in the direction of arrow Y1 in figure 2.
The left side view of the figure, Figure 5 is a front view of a corrugated plate with a different wave shape, Figure 6 is a plan view in the two directions of arrow Y in Figure 5, and Figure 7 is for explaining the principle of water droplet diffusion. FIG. 1 is a corrugated plate, 3 is a plane part, 4 is a slope part, 10~
15 is a slope, and 20 to 25 are ridgelines.
Claims (1)
の各斜面の稜線を垂直Vに対して角度θ傾斜させ
たとき、斜面同士の夾角を2α、斜面上の一点か
ら板面と直交して斜面に沿つて直下する線Pと垂
線Vとのなす角度をβとしてθ=βとなるように
角度αを設定したことを特徴とする気液接触用充
填板。 When the ridgeline of each slope of a corrugated plate formed by bending a plate to form a flat slope is inclined at an angle θ with respect to the vertical V, the included angle between the slopes is 2α, and the angle from one point on the slope is perpendicular to the plate surface. A filling plate for gas-liquid contact, characterized in that the angle α is set so that θ=β, where β is the angle between a line P directly below the slope and a perpendicular line V.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10619881U JPS5814938U (en) | 1981-07-17 | 1981-07-17 | Packing plate for gas-liquid contact |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10619881U JPS5814938U (en) | 1981-07-17 | 1981-07-17 | Packing plate for gas-liquid contact |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5814938U JPS5814938U (en) | 1983-01-29 |
JPS6236503Y2 true JPS6236503Y2 (en) | 1987-09-17 |
Family
ID=29900706
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10619881U Granted JPS5814938U (en) | 1981-07-17 | 1981-07-17 | Packing plate for gas-liquid contact |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5814938U (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4831177A (en) * | 1971-07-20 | 1973-04-24 |
-
1981
- 1981-07-17 JP JP10619881U patent/JPS5814938U/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4831177A (en) * | 1971-07-20 | 1973-04-24 |
Also Published As
Publication number | Publication date |
---|---|
JPS5814938U (en) | 1983-01-29 |
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