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JP4037861B2 - Fluid discharge path structure - Google Patents
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JP4037861B2 - Fluid discharge path structure - Google Patents

Fluid discharge path structure Download PDF

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JP4037861B2
JP4037861B2 JP2004327526A JP2004327526A JP4037861B2 JP 4037861 B2 JP4037861 B2 JP 4037861B2 JP 2004327526 A JP2004327526 A JP 2004327526A JP 2004327526 A JP2004327526 A JP 2004327526A JP 4037861 B2 JP4037861 B2 JP 4037861B2
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JP2005118779A (en
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和正 生島
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Musashi Engineering Inc
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この発明は、流体等を、複数個の吐出口からまたは、そこに装着したノズルから吐出するに用いて好適な液体の吐出路構造に関するものであり、とくに、それぞれの吐出口からの吐出量を十分均一ならしめるものである。   The present invention relates to a liquid discharge path structure suitable for discharging a fluid or the like from a plurality of discharge ports or from nozzles attached thereto, and in particular, discharge amount from each discharge port. It should be uniform enough.

たとえば、接着剤、電子材料等の液状物質を能率的に定量吐出したり、塗布したりする場合に用いられる吐出路としては、図4に略線縦断面で例示するように、1の流入口101 から流入させた液状物質を、所要個数の吐出口102 まで自然に分岐流動させ、それらの各吐出口102 に装着したノズル103 から、ノズル103 の運動下で液状物質を同時に吐出させるものがある。   For example, as an ejection path used for efficiently dispensing and applying a liquid substance such as an adhesive or an electronic material, as shown in FIG. There is a type in which the liquid material flowing in from 101 is naturally branched and flowed to the required number of discharge ports 102, and the liquid material is discharged simultaneously from the nozzles 103 attached to the discharge ports 102 under the movement of the nozzles 103. .

ところで、このような従来技術において、ノズル103 を図示のように横一列に配設した場合には、液状物質が、一の流入口101 からそれぞれの吐出口102 に至るまでの分岐流路の長さが吐出口102 の位置によって異なることに加え、分岐流路の長いものほど大きな流動抵抗を受けて圧力損失が大きくなること等に起因して、ノズル103 からの液状物質の吐出量が、分岐流路の長さの短い中央部分で多く、端部に向けて次第に減少するという、吐出量ないしは塗布量のばらつきの問題を生じ、この傾向は、粘性の小さい液体、圧縮性を有する気体についてもほぼ同様である。   By the way, in such a conventional technique, when the nozzles 103 are arranged in a horizontal row as shown in the figure, the length of the branch flow path from the one inlet 101 to each discharge outlet 102 is measured. In addition to the fact that the length varies depending on the position of the discharge port 102, the longer the branch flow path, the greater the flow resistance and the greater the pressure loss. There is a problem of variation in the discharge amount or application amount, which is mostly in the short central part of the flow path and gradually decreases toward the end part, and this tendency also applies to liquids with low viscosity and compressible gases. It is almost the same.

この発明は、従来技術が抱えるこのような問題点を解決することを課題として検討した結果なされたものであり、それの目的とするところは、一の流入口から流入させた液体を、複数個の吐出口または、そこに装着したノズルから吐出するに当たり、流入口に対する吐出口の相対位置のいかんにかかわらず、全ての吐出口等での吐出量を十分均一にすることができる流体の吐出路構造を提供することにある。   The present invention has been made as a result of studying as a subject to solve such problems of the prior art. The object of the present invention is to provide a plurality of liquids introduced from one inlet. When discharging from the discharge port or the nozzle mounted on it, the discharge path of the fluid can make the discharge amount at all the discharge ports sufficiently uniform regardless of the relative position of the discharge port with respect to the inflow port To provide a structure.

この発明の、流体の吐出路構造は、流体の一の流入口から複数個の吐出口に至るまでの間に、流路を分岐させる複数段の流路分岐部を設け、各々が単一の区画室からなる各流路分岐部内のそれぞれの自然の分岐路の長さをともにほぼ等しくしたものであって、縦断面内で、上段側の流路分岐部を形成している区画室の横幅を、該流路分岐部に隣接する下段側の流路分岐部の流体入口間の距離よりも広く構成し、それらの上下の区画室を、下段側の区画室の分岐路の中心の延長線上に重ねて配置した、曲がりのないまっすぐな管路で連通させるとともに、その管路を、それによって連通される上下の区画室内のいずれの分岐路よりも短く形成したことを特徴とするものであるThe fluid discharge path structure of the present invention is provided with a plurality of stages of flow path branching sections that branch the flow path from one fluid inlet to a plurality of outlets, each of which is a single unit. in each of the flow path branching portion consisting of compartments, I der that respective lengths of the nature of the branching paths together substantially equal, in a longitudinal section, compartment forming a flow path branching portion of the upper side The lateral width of the lower branch side of the lower channel branch adjacent to the lower channel branch part is configured to be wider, and the upper and lower compartments thereof are arranged at the center of the lower branch chamber branch path. It is characterized in that it is communicated with a straight pipe line that is arranged on the extension line and has no bend, and the pipe line is formed shorter than any branch path in the upper and lower compartments communicated therewith. It is .

ここで好ましくは、同一の分岐段内のそれぞれの流路分岐部の相互間で、分岐路の長さをともにほぼ等しくする。
これによれば、一の流入口から流入した流体が、それぞれの吐出口に達するまでの分岐路のトータル長さが、流路分岐部の段数の多少にかかわらず、また、それぞれの吐出口の配置位置のいかんにかかわらず、実質的に等しくなり、結果として、流体がどの分岐路を通る場合でも圧力損失がほぼ等しくなるので、それぞれの吐出口からの流体吐出量を十分均一なものとすることができる。
Here, preferably, the lengths of the branch paths are made substantially equal between the respective flow path branch portions in the same branch stage.
According to this, the total length of the branch path until the fluid flowing in from one inflow port reaches each discharge port is the same regardless of the number of stages of the flow path branching section. Regardless of the arrangement position, they are substantially the same, and as a result, the pressure loss is almost equal regardless of which branch the fluid passes through, so that the amount of fluid discharged from each outlet is sufficiently uniform. be able to.

ところで、各流路分岐部内でのそれぞれの分岐路の長さがほぼ等しい場合であっても、流路分岐部の横断面内の内輪郭形状との関連において、それぞれの分岐路の圧力損失を十分等しくできないおそれもあるので、より好ましくは、それぞれの分岐路の、流路分岐部内表面からの距離および、流路分岐部中心からの距離の少なくとも一方をともにほぼ等しくして、それぞれの分岐路の圧力損失を一層均等ならしめる。
そしてこのことは、それぞれの分岐路を、流路分岐部の中心からともにほぼ等しい距離に、その中心に対して点対称に配置した場合および、流路分岐部の中心線からともにほぼ等しい距離に、その中心線に対して線対称に配置した場合にもまた効果的である。
また、全ての区画室において、分岐路本数を2本とすること、同一分岐段内において、区画室間が連通していないことが好ましい。
By the way, even when the lengths of the respective branch paths in each flow path branch section are substantially equal, the pressure loss of each branch path is related to the inner contour shape in the cross section of the flow path branch section. Since there is a possibility that they may not be sufficiently equal, more preferably, each branch path is made such that at least one of the distance from the inner surface of the flow path branch section and the distance from the center of the flow path branch section is substantially equal. To make the pressure loss more uniform.
And this means that each branch path is located at approximately the same distance from the center of the flow path branching section and point-symmetrically with respect to the center, and at the same distance from the center line of the flow path branching section. It is also effective when arranged symmetrically with respect to the center line.
Moreover, it is preferable that the number of branch paths is two in all the compartments, and that the compartments do not communicate with each other in the same branch stage.

かくしてこの発明によれば、流体の一の流入口から複数個の吐出口に至るまでの間のそれぞれの分岐路のトータル長さをほぼ等しくすることで、どの分岐路を通る流体の圧力損失をもほぼ等しくして、それぞれの吐出口から吐出される流体の吐出量を高い精度で均一化させることができる。   Thus, according to the present invention, by making the total length of each branch path from one fluid inlet to a plurality of outlets substantially equal, the pressure loss of the fluid passing through which branch is reduced. The discharge amount of the fluid discharged from each discharge port can be made uniform with high accuracy.

以下に、この発明の実施の形態を図面に示すところに基づいて説明する。
図1は、この発明の実施の形態を示す図であり、図1(a) は略線縦断面図であり、図1(b) は、一の流路分岐部の略線横断面図である。
これは、入口継手1から流入する液体の流路を、三段の分岐段2, 3, 4のそれぞれにて分岐させて、一列に並ぶ総計16本のノズル5から吐出させる場合について示す。従ってここでは、流体流入口としての一の入口継手1から流入した液体は、16個の吐出口6へ分岐流動されることになり、その分岐の態様は、第一段目の分岐段2に設けた一の流路分岐部7で、液体を二本の、均等にして実質的に等長の分岐路8に分岐させ、第二段目の分岐段3に設けた二つの流路分岐部9のそれぞれで、液体をさらに二本ずつの、均等にして実質的に等長の分岐路10に分岐させ、そして、第三段目の分岐段4に形成した四つの流路分岐部11で四本ずつのほぼ等長の分岐路12に分岐させ、さらに、同一の分岐段内に位置するそれぞれの流路分岐部の相互間でもまた分岐路の長さをともにほぼ等しくしたものである。
Embodiments of the present invention will be described below with reference to the drawings.
FIG. 1 is a diagram showing an embodiment of the present invention. FIG. 1 (a) is a schematic vertical cross-sectional view, and FIG. 1 (b) is a schematic cross-sectional view of one flow path branching portion. is there.
This shows a case where the flow path of the liquid flowing in from the inlet joint 1 is branched at each of the three branch stages 2, 3, and 4 and discharged from a total of 16 nozzles 5 arranged in a line. Therefore, here, the liquid flowing in from one inlet joint 1 as a fluid inlet is branched and flowed to 16 discharge ports 6, and the branching mode is the first branch stage 2. Two flow path branch portions provided in the second branch stage 3 by branching the liquid into two equal and substantially equal length branch paths 8 by the one flow path branch section 7 provided 9, the liquid is further divided into two equal, substantially equal-length branch paths 10, and four flow path branch portions 11 formed in the third branch stage 4. Each of the four branch paths 12 is made to branch into approximately equal-length branch paths 12, and the lengths of the branch paths are made substantially equal between the flow path branch portions located in the same branch stage.

ここで、それぞれの流路分岐部7, 9における液体の均等なる分岐のためには、流路分岐部7を例にとって図1(b) に横断面図で示すように、仮想線で囲んで示すそれぞれの分岐路8が、流路分岐部7の内表面からともに等しい距離に存在し、また、流路分岐部7の中心Oからもともに等しい距離に存在する配置構成とすることが好ましく、これによれば、いずれの分岐路8を流動する液体も、ともにほぼ等しい液体摩擦、流路摩擦等を受けることになり、圧力損失もまたほぼ等しくなるので、両分岐路8からの次の分岐段3への液体吐出量は実質的に等しくなり、このことは、第二段目の分岐段3から第三段目の分岐段4への液体吐出量についても同様である。   Here, in order to evenly divide the liquid in each of the flow path branch portions 7 and 9, the flow path branch portion 7 is taken as an example and surrounded by an imaginary line as shown in a cross-sectional view in FIG. It is preferable that the respective branch paths 8 shown are present at an equal distance from the inner surface of the flow path branching section 7 and are also disposed at an equal distance from the center O of the flow path branching section 7. According to this, since the liquid flowing through any of the branch paths 8 is subjected to substantially the same liquid friction, flow path friction, etc., and the pressure loss is also substantially equal, the next branch from both branch paths 8 The liquid discharge amount to the stage 3 is substantially equal, and this is the same for the liquid discharge amount from the second branch stage 3 to the third branch stage 4.

ところで、第三段目の分岐段4における流路分岐部11では、液体を四本の分岐路12に分岐させていることから、中央寄りの二本の分岐路12の長さが他の二本のそれより必然的に短くなるが、そもそも、この流路分岐部11内の分岐路長さは、各分岐路8, 10, 12 のトータル長さに比してはるかに小さいものであるので、流路分岐部11内での分岐路12の長さの違いは、そのトータル長に対してほとんど無視し得る程度のものであり、従って、それぞれの吐出口6、ひいては、ノズル5からの液体吐出量もまた十分均等なものとなる。   By the way, in the flow path branching section 11 in the third branching stage 4, since the liquid is branched into the four branching paths 12, the lengths of the two branching paths 12 closer to the center are the other two. Although it is inevitably shorter than that of the book, in the first place, the branch path length in this flow path branch section 11 is much smaller than the total length of each branch path 8, 10, 12 The difference in the length of the branch path 12 in the flow path branching portion 11 is almost negligible with respect to the total length. Therefore, the liquid from each discharge port 6 and by extension, the nozzle 5 is obtained. The discharge amount is also sufficiently uniform.

なお、吐出量精度のより一層の向上のためには、第三段目の分岐段4の流路分岐部11での分岐路本数を二本とし、さらに付加した第四段目の分岐段の流路分岐部にさらに二本の分岐路を設けることも可能であり、これによれば、入口継手1から吐出口に至るまでの間のそれぞれの分岐路のトータル長さをより等しいものとすることができる。   In order to further improve the discharge amount accuracy, the number of branch paths in the flow path branching section 11 of the third branch stage 4 is set to two, and the added fourth branch stage is further provided. It is possible to further provide two branch paths in the flow path branching section, and according to this, the total length of each branch path from the inlet joint 1 to the discharge port is made more equal. be able to.

以上のように構成したところによれば、入口継手1から流路分岐部7へ流入した液体は、二つに分岐されて、ともにほぼ等しい圧力損失の下で、それぞれの流路分岐部9へ流入し、それらのそれぞれにおいても同様に二つに分岐され、しかも、両流路分岐部9の相互間にてもほぼ等しい圧力損失にてそれぞれの流路分岐部11へ流入し、四本ずつの分岐路12からそれぞれの吐出口6を経てノズル5から吐出されることになり、ここでは、各分岐路8, 10, 12のトータル長さがほぼ等しくなって、各分岐路を通る液体の圧力損失がいずれもほぼ等しくなるので、それぞれのノズル5からの液体吐出量を高い精度で均一化させることができる。そしてこのことは、全てのノズル5を一列に並列配置することに代えて、それらのノズルを千鳥状に配置した場合にも同様である。   According to the configuration as described above, the liquid flowing from the inlet joint 1 to the flow path branching portion 7 is branched into two, and both flow into the respective flow path branching portions 9 under substantially equal pressure loss. Each of them is also branched in two in the same way, and also flows into each flow path branch section 11 with substantially equal pressure loss between both flow path branch sections 9, and four each. In this case, the total length of each of the branch paths 8, 10, 12 is substantially equal, and the liquid passing through each branch path is discharged from the nozzle 5 through the respective discharge ports 6. Since the pressure losses are almost equal, the liquid discharge amount from each nozzle 5 can be made uniform with high accuracy. This is the same when the nozzles 5 are arranged in a staggered manner instead of arranging all the nozzles 5 in a line.

図2,3はそれぞれ、流路分岐部、なかでも流路分岐部7,9における流路の他の分岐形態を示す略線横断面図であり、これらはいずれも、流路分岐部7を例として、その横断面内の内輪郭形状を円形,正方形,正三角形とした場合に、図に仮想線で囲んで示すそれぞれの分岐路8の、任意の横断面内で、流路分岐部7の内表面および中心のそれぞれからの距離をともに等しくしたものである。
ここで、図2に示すそれぞれの分岐路8は、流路分岐部7の中心Oからの距離をともにほぼ等しくするとともに、その中心Oに対して点対称に位置するものであり、また、流路分岐部7の中心線からの距離をともにほぼ等しくし、その中心線を通るとともに二個の分岐路を通る平面内で、中心線に対して線対称に位置するものである。
2 and 3 are respectively schematic cross-sectional views showing other branch forms of the flow path in the flow path branching section, in particular, the flow path branching sections 7 and 9. as an example, the inner contour circle in its horizontal cross-section, a square, when an equilateral triangle, each branch channel 8 enclosed by a phantom line in the figure, at any transverse plane, the flow path branching portion The distances from the inner surface and the center of 7 are equal.
Here, each of the branch paths 8 shown in FIG. 2 has a substantially equal distance from the center O of the flow path branching section 7 and is positioned point-symmetrically with respect to the center O. The distances from the center line of the road branching portion 7 are both substantially equal, and are located symmetrically with respect to the center line in a plane passing through the center line and passing through the two branch paths.

ところで、最終段の分岐段の流路分岐部に設ける分岐路としては、ノズルの前後、左右等の二次元の吐出もしくは塗布運動に際して、吐出もしくは塗布軌跡が重複するおそれの少ない図3に示す配置構成の方が好ましい。   By the way, as the branch path provided in the flow path branch portion of the final branch stage, the arrangement shown in FIG. A configuration is preferred.

ノズル数を30本、ノズル間隔を3mmとするとともに、分岐段を3段としたこの発明に係る吐出路構造を用いて、フィラー入りの接着材を吐出した場合における、ノズル間の吐出量の最大ばらつき率を求めたところ、この発明の実施例では19.5%であったところ、図4に示す従来技術に基づき同数のノズルを1mm間隔で配置した場合の最大ばらつき率は27.5%であった。
従って、この実施例では、ノズル間隔を3倍としてなお、ばらつき率を5/7程度にまで低減させることが可能となった。
The maximum discharge amount between nozzles when the adhesive material containing filler is discharged using the discharge path structure according to the present invention in which the number of nozzles is 30, the nozzle interval is 3 mm, and the branch stage is 3 stages. When the variation rate was determined, it was 19.5% in the embodiment of the present invention, and the maximum variation rate when the same number of nozzles were arranged at 1 mm intervals based on the prior art shown in FIG. 4 was 27.5%.
Therefore, in this embodiment, it is possible to reduce the variation rate to about 5/7 even if the nozzle interval is tripled.

この発明の実施の形態を示す略線縦断面図および横断面図である。1 is a schematic longitudinal sectional view and a transverse sectional view showing an embodiment of the present invention. 分岐路の他の配置態様を示す略線横断面図である。It is a rough line cross-sectional view which shows the other arrangement | positioning aspect of a branched path. 分岐路のさらに他の配置態様を示す略線横断面図である。It is a rough line cross-sectional view which shows the other arrangement | positioning aspect of a branch path. 従来技術を示す略線縦断面図である。It is a basic line longitudinal cross-sectional view which shows a prior art.

符号の説明Explanation of symbols

1 入口継手
2, 3, 4 分岐段
5 ノズル
6 吐出口
7, 9, 11 流路分岐部
8, 10, 12 分岐路
1 Inlet joint 2, 3, 4 Branch stage 5 Nozzle 6 Discharge port 7, 9, 11 Channel branch 8, 10, 12 Branch

Claims (8)

流体の一の流入口から複数個の吐出口に至るまでの間に、流路を分岐させる複数段の流路分岐部を設け、各々が単一の区画室からなる各流路分岐部内のそれぞれの自然の分岐路の長さをともにほぼ等しくしてなる流体の吐出路構造であって、
縦断面内で、上段側の流路分岐部を形成している区画室の横幅を、該流路分岐部に隣接する下段側の流路分岐部の流体入口間の距離よりも広く構成し、
それらの上下の区画室を、下段側の区画室の分岐路の中心の延長線上に重ねて配置した、曲がりのないまっすぐな管路で連通させるとともに、その管路を、それによって連通される上下の区画室内のいずれの分岐路よりも短く形成したこと
を特徴とする流体の吐出構造
Provided with a plurality of stages for branching the flow path from one fluid inlet to a plurality of outlets, each in a flow path branch consisting of a single compartment , It is a fluid discharge path structure in which the length of each natural branch path is approximately equal ,
Within the longitudinal section, the lateral width of the compartment forming the upper flow path branching section is configured wider than the distance between the fluid inlets of the lower flow path branching section adjacent to the flow path branching section,
The upper and lower compartments are communicated with straight straight pipes that are arranged on the extension line of the center of the lower branch compartment, and the upper and lower compartments communicated with the upper and lower compartments. Being shorter than any branch path in the compartment
Fluid discharge structure characterized by
同一の分岐段内のそれぞれの流路分岐部の相互間で、分岐路の長さをともにほぼ等しくしてなる請求項1に記載の流体の吐出路構造。 2. The fluid discharge path structure according to claim 1, wherein the lengths of the branch paths are made substantially equal between the respective flow path branch portions in the same branch stage. それぞれの分岐路の、流路分岐部内表面からの距離をともにほぼ等しくしてなる請求項1もしくは2に記載の吐出路構造。 The discharge path structure according to claim 1 or 2, wherein the distance of each branch path from the inner surface of the flow path branching section is substantially equal. それぞれの分岐路の、流路分岐部中心からの距離をともにほぼ等しくしてなる請求項1〜3のいずれかに記載の吐出路構造。 The discharge path structure according to any one of claims 1 to 3, wherein the distances of the respective branch paths from the center of the flow path branch section are substantially equal. それぞれの分岐路を、流路分岐部の中心からともにほぼ等しい距離に、その中心に対して点対称に配置してなる請求項1〜4のいずれかに記載の吐出路構造。 The discharge path structure according to any one of claims 1 to 4, wherein the respective branch paths are disposed at substantially equal distances from the center of the flow path branching portion and point-symmetrically with respect to the center. それぞれの分岐路を、流路分岐部の中心線からともにほぼ等しい距離に、その中心線に対して線対称に配置してなる請求項1〜5のいずれかに記載の吐出路構造。 The discharge path structure according to any one of claims 1 to 5, wherein the respective branch paths are arranged symmetrically with respect to the center line at substantially the same distance from the center line of the flow path branch portion. 全ての区画室において、分岐路本数を2本とすることを特徴とする請求項1〜6のいずれかに記載の吐出路構造 7. The discharge path structure according to claim 1, wherein the number of branch paths is two in all the compartments . 同一分岐段内において、区画室間が連通していないことを特徴とする請求項1〜7のいずれかに記載の吐出路構造 The discharge path structure according to any one of claims 1 to 7, wherein the compartments do not communicate with each other in the same branch stage .
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