TW202009065A - Foam material flow distribution nozzle - Google Patents
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本創作是關於一種噴嘴,尤其是一種可分配發泡材流量的噴嘴。This creation is about a nozzle, especially a nozzle that can distribute the flow of foam.
一般平板或浪板的加工作業之一,係將該浪板置放於輸送帶上,再由噴嘴以往復式的移動方式將發泡材噴塗於該浪板,然而在噴塗的加工過程中,該浪板的部分區域會發生重複噴塗的問題。況且,由於該發泡材料從入料口到達各噴嘴的距離不同,因此若該噴嘴較遠離該入料口,則會產生因流速過慢而於該噴嘴內產生結膜的現象,進而導致該噴嘴有阻塞需時常替換噴嘴的問題。One of the general flat or wave board processing operations is to place the wave board on the conveyor belt, and then spray the foamed material on the wave board in a reciprocating manner by the nozzle. However, in the spraying process, the wave board The problem of repeated spraying may occur in some areas. Moreover, since the distance of the foamed material from the feed inlet to each nozzle is different, if the nozzle is farther away from the feed inlet, a phenomenon of film formation in the nozzle due to the too slow flow rate may occur, which in turn causes the nozzle There is a problem that the nozzle needs to be replaced frequently.
如中華民國新型專利字號第M303942中所述的浪板結構,其包含一板體,該板體表面一體彎折形成有複數呈縱向延伸之第一凸部,且該板體表面於各相鄰第一凸部間分別彎折形成有一高度較低之第二凸部,再者該板體一側端緣形成有一對應第一凸部外緣形狀之接合部。一發泡層係披覆於該板體內側底面。The wave plate structure as described in the new patent number M303942 of the Republic of China includes a plate body whose surface is integrally bent to form a plurality of longitudinally extending first convex portions, and the plate body surface is adjacent to each A second convex portion with a low height is bent between the convex portions, and a joint portion corresponding to the outer edge shape of the first convex portion is formed on one end edge of the plate body. A foam layer is coated on the inner bottom surface of the board body.
上述新型專利案中,已揭露該浪板之板體內側底面具有發泡層,且揭露該發泡體較佳者如PU發泡材質。然而,該專利案中僅揭露該板體內側底面披覆有該發泡層,並未教示針對該浪板凹部應以何種技術手段施予較多的披覆量,以達到依成品表面構型噴出對應流量之目的。In the above-mentioned new patent case, it has been disclosed that the inner bottom surface of the board body of the wave board has a foam layer, and it is disclosed that the foam body is preferably a PU foam material. However, the patent only discloses that the inner bottom surface of the board body is covered with the foam layer, and does not teach what technical means should be applied to the concave portion of the wave board to apply more coating amount to achieve the surface configuration according to the finished product. The purpose of spraying the corresponding flow.
本發明之主要目的在於提供一種發泡材流量分配噴嘴,其可依成品表面構型噴出對應的流量,且具有成本低、不須經常替換噴頭,以及結構精簡的優點。The main purpose of the present invention is to provide a foam material flow distribution nozzle, which can spray the corresponding flow rate according to the surface configuration of the finished product, and has the advantages of low cost, no need to frequently replace the nozzle, and a simplified structure.
為達上述目的及功效,本發明所揭示的一種發泡材流量分配噴嘴,其包含一外管件。In order to achieve the above purpose and effect, a foam material flow distribution nozzle disclosed by the present invention includes an outer tube.
一等比式分流管路系統,係安裝在該外管件的內部,該等比式分流管路系統依序包含一第一分流層至第m分流層,其中第一分流層具有一第一分流段,該第m分流層具有rm-1 個第m分流段。其中各該分流層的每一該分流段具有一分流入口及r分流出口,且該分流口至每一該分流出口的距離相等。An equal ratio shunt piping system is installed inside the outer pipe fitting. The equal ratio shunt piping system sequentially includes a first shunt layer to an mth shunt layer, wherein the first shunt layer has a first shunt Segment, the mth distribution layer has r m-1 mth distribution segments. Each shunt section of each shunt layer has a shunt inlet and an r shunt outlet, and the distance from the shunt outlet to each shunt outlet is equal.
相鄰的二該分流層,前一該分流層中的各該分流段的各該分流口各自對應連接次一分流層中的該分流段的該分流入口。其中m為自然數、r為自然數且大於等於2、第m分流層的分流出口數量為rm 個。複數噴嘴,係分別安裝在第m分流層的各該分流出口。In the two adjacent shunt layers, the shunt ports of the shunt sections in the previous shunt layer respectively correspond to the shunt inlets of the shunt section in the next shunt layer. Where m is a natural number, r is a natural number and is greater than or equal to 2, and the number of shunt outlets in the m- th shunt layer is r m . A plurality of nozzles are respectively installed in each of the m-th distribution layer.
在一實施例中,其中該m為4、r為2,第m分流層的分流出口數量為16個。In an embodiment, wherein the m is 4, the r is 2, and the number of shunt outlets of the mth shunt layer is 16.
在一實施例中,其中該分流段係一金屬管,該分流出口位在該金屬管長度方向的中間位置,該分流口位在該金屬管的二端。In an embodiment, wherein the shunt section is a metal pipe, the shunt outlet is located at a middle position in the length direction of the metal pipe, and the shunt outlet is located at both ends of the metal pipe.
在一實施例中,其中該第m層的各該分流段具有一第一分流通道及一第二分流通道,該第一分流通道與該m-1層的分流出口及該m+1層的該分流入口相接,該第二分流通道與該m-1層的分流出口及該m+1層的另一該分流入口相接,該第一分流通道相接的m-1層的分流出口,與該第二分流通道相接的m-1層的分流出口為同一個分流出口,該第一分流通道相接的m+1層的分流入口,與該第二分流通道相接的m+1層的分流入口為不同的分流入口,該第一分流通道的通道寬度相同於該第二分流通道的通道寬度,該材料自各該噴嘴的輸出量相等,致使該發泡材可均勻噴塗於該板材表面。In an embodiment, each of the shunt sections of the mth layer has a first shunt channel and a second shunt channel, the first shunt channel and the shunt outlet of the m-1 layer and the m+1 layer The splitter inlet is connected, the second splitter channel is connected to the splitter outlet of the m-1 layer and another splitter inlet of the m+1 layer, and the splitter outlet of the m-1 layer is connected to the first splitter channel , The split outlet of the m-1 layer connected to the second split channel is the same split outlet, the split inlet of the m+1 layer connected to the first split channel, and m+ connected to the second split channel The split inlets of layer 1 are different split inlets, the channel width of the first split channel is the same as the channel width of the second split channel, the output of the material from each of the nozzles is equal, so that the foamed material can be evenly sprayed on the Plate surface.
在一實施例中,其中各該分流段具有一第一分流通道及一第二分流通道,該第一分流通道與該m-1層的分流出口及該m+1層的該分流入口相接,該第二分流通道與該m-1層的分流出口及該m+1層的另一該分流入口相接,該第一分流通道相接的m-1層的分流出口,與該第二分流通道相接的m-1層的分流出口為同一個分流出口,該第一分流通道相接的m+1層的分流入口,與該第二分流通道相接的m+1層的分流入口為不同的分流入口,該第一分流通道的通道寬度小於該第二分流通道的通道寬度,該第二分流通道的該噴嘴的輸出量大於該第一分流通道的該噴嘴的輸出量。In an embodiment, each of the shunt sections has a first shunt channel and a second shunt channel, the first shunt channel is connected to the shunt outlet of the m-1 layer and the shunt inlet of the m+1 layer , The second shunt channel is connected to the shunt outlet of the m-1 layer and another shunt inlet of the m+1 layer, and the shunt outlet of the m-1 layer connected to the first shunt channel is connected to the second The shunt outlet of the m-1 layer connected to the shunt channel is the same shunt outlet, the shunt inlet of the m+1 layer connected to the first shunt channel, and the shunt inlet of the m+1 layer connected to the second shunt channel For different branch inlets, the channel width of the first branch channel is smaller than the channel width of the second branch channel, and the output of the nozzle of the second branch channel is greater than the output of the nozzle of the first branch channel.
在一實施例中,其中該第一分流通道的該噴嘴及該第二分流通道的該噴嘴相對應於該板材,該板材具有複數個凹槽,二該凹槽之間具有一平面部,該第一分流通道的該噴嘴相對該板材的該平面部,該第二分流通道的該噴嘴相對該凹槽,致使該凹槽內該發泡材的噴塗量大於該平面部表面該發泡材的噴塗量。In an embodiment, wherein the nozzle of the first shunt channel and the nozzle of the second shunt channel correspond to the plate, the plate has a plurality of grooves, and a plane portion between the grooves, the The nozzle of the first shunt channel is opposed to the plane portion of the plate, and the nozzle of the second shunt channel is opposed to the groove, so that the spraying amount of the foam material in the groove is greater than that of the foam material on the surface of the plane portion Spray volume.
而本發明上述之目的及優點,可從下述所選用實施例之詳細說明與附圖中獲得深入了解。The above objects and advantages of the present invention can be obtained from the following detailed description of the selected embodiments and the accompanying drawings.
請參閱第1圖,本發明的第一實施例所提供的發泡材流量分配噴嘴,其包含有一預定的長度及形狀的外管件10,例如該外管件10可以是圓管狀或方管狀。Please refer to FIG. 1, the foam material flow distribution nozzle provided in the first embodiment of the present invention includes an
一等比式分流管路系統20係安裝在該外管件10的內部。該等比式分流管路系統20係採用階級分層結構的形式,也就說,該等比式分流管路系統20至少包含具有一第一分流層22及一第二分流層30。該第一分流層22與該第二分流層30相鄰,且各自具有不同數量的通道。進一步而言,該第一分流層22具有一第一分流段24。該第一分流段24具有一第一分流入口26及二第一分流出口28。A proportional
請搭配參閱第2圖,各該分流段(如第一分流段24所示)具有該第一分流通道25及該第二分流通道27。該第一分流通道25與前一層的該分流出口及次一層的該分流入口相接,該第二分流通道27與前一層的該分流出口及次一層的該分流入口相接,該第一分流通道25相接前一層的分流出口,與該第二分流通道27相接前一層的分流出口為同一個分流出口,該第一分流通道25相接次一層的分流入口,與該第二分流通道27相接次一層的分流入口為不同的分流入口。該第一分流通道25與該第二分流通道27的通道寬度相等。於本實施例中,該第一分流段24係一金屬管,該第一分流入口26位在該金屬管長度方向的中間位置,二該第一分流出口28位在該金屬管的二端。該第一分流入口26至二該第一分流出口28的距離相等。該第一分流段24的結構與其他各分流層的各分流段的結構相同。Please refer to FIG. 2 for collocation. Each of the shunt sections (as shown in the first shunt section 24) has the
該第二分流層30具有二第二分流段32。各該第二分流段32具有一第二分流入口34及二第二分流出口36。該第二分流層30的各該第二分流段32的各該第二分流入口34,係相對應連接該第一分流層22的該第一分流段24的各該第一分流出口28。該第二分流入口34至二該第二分流出口36的距離相等。The
本實施例更包含有複數個噴嘴38,各該噴嘴38係分別安裝在第二分流層30的各該第二分流出口36。The present embodiment further includes a plurality of
該第一分流入口26至二端的二該第一分流出口28等距離;該第二分流入口34連接該第一分流出口28,且該第二分流入口34至二端的二該第二分流出口36等距離。因此材料進入該等比式分流管路系統20後,先在該第一分流層22的該第一分流段24分成二份材料,且可以同時進入該第二分流層30的二該第二分流段32,且材料在每個該第二分流段32內再分成二份,最後同時由四個該第二分流出口36輸出。The first branching
根據上述的說明,得知由於相鄰的二該分流層,前一分流層至次一分流層的各該分流段總數係以等比方式增加,可縮短該入料口至各噴嘴的距離,如此便能解決習知因該入料口至各噴嘴行程較長,而產生發泡材流量分配噴嘴體積過大的問題。According to the above description, it is known that due to the adjacent two split layers, the total number of split sections from the previous split layer to the next split layer is increased in a proportional manner, which can shorten the distance from the inlet to each nozzle, In this way, it is possible to solve the problem that the conventional flow path of the foam inlet is too large due to the long stroke from the inlet to each nozzle.
第3圖顯示為本發明的第二實施例所提供的發泡材流量分配噴嘴,其主要結構與第一實施例相同,差別在於:該等比式分流管路系統20更具有一第三分流層40。FIG. 3 shows the foam material flow distribution nozzle provided by the second embodiment of the present invention. Its main structure is the same as that of the first embodiment, and the difference is that the proportional
該第三分流層40具有四個第三分流段42。各該第三分流段42具有一第三分流入口44及二第三分流出口46。該第三分流層40的該第三分流段42的該第三分流入口44,係相對應連接該第二分流層30的該第二分流段32的該第二分流出口36。該第三分流入口44至二該第三分流出口46的距離相等。各該噴嘴38係分別安裝在第三分流層40的各該第三分流出口46。The
由第一實施例及第二實施例中可推論得知,該等比式分流管路系統20依序包含該第一分流層22至第m分流層,其中該第m分流層具有rm-1
個第m分流段。各該分流層的每一該分流段具有一分流入口及r分流出口,且該分流入口至每一該分流出口的距離相等。相鄰的二該分流層,前一該分流層中的各該分流段的各該分流出口各自對應連接次一分流層中的該分流段的該分流入口。其中m為自然數、r為自然數且大於等於二、第m分流層的分流出口數量為rm
個。各該噴嘴38係分別安裝在第m分流層的各該分流出口。It can be inferred from the first embodiment and the second embodiment that the proportional
請參閱第4圖,為本發明的第三實施例所提供的發泡材流量分配噴嘴,舉例而言,若該等比式分流管路系統20包含第一分流層22至第四分流層50,且每一該分流段具有一分流入口及二分流出口,則代入上述各個公式可計算得出:該等比式分流管路系統20的第四分流層50具有八個第四分流段52,及十六個第四分流出口54,如此便有十六個該噴嘴38係分別安裝在各該第四分流出口54。Please refer to FIG. 4, which is a flow distribution nozzle for foamed material provided by a third embodiment of the present invention. For example, if the proportional
請參閱第5圖,於實際使用時,自該第一分流段24進入的一份材料(發泡材)90被分成二份材料90後,再由二份材料90分成四份材料90,由於該材料90自各該噴嘴38的輸出量相等,所以在噴塗一平板92時,可以將材料(發泡材)90穩定且均勻的噴塗於該平板92表面。Please refer to FIG. 5, in actual use, after one part of the material (foamed material) 90 entered from the first diverting
前述等比式分流管路系統20的相關公式中,當r為三(每一分流段具有三個分流出口),且m為二時,該發泡材流量分配噴嘴係包含有一第一分流層及一第二分流層,且該第二分流層具有九個第二分流出口,如此便有九個噴嘴係分別安裝於各該第二分流出口。In the related formula of the aforementioned proportional
請參閱第6圖,為本發明的第四實施例所提供的發泡材流量分配噴嘴,其與該第一實施例的差別在於:該等比式分流管路系統20的各該分流段80具有不同的寬度。Please refer to FIG. 6, which is a flow distribution nozzle for foamed material according to a fourth embodiment of the present invention. The difference from the first embodiment is that each of the split sections 80 of the proportional
位於第m層的各該分流段80具有該第一分流通道801及該第二分流通道802。該第一分流通道801與前一分流層(第m-1層)的該分流出口及次一分流層(第m+1層)的該分流入口相接;同理該第二分流通道802與前一分流層(第m-1層)的該分流出口及次一分流層(第m+1層)的該分流入口相接。Each shunt section 80 located on the mth layer has the
前述該第一分流通道801相接前一分流層的分流出口,與該第二分流通道802相接前一分流層的分流出口,所稱的「前一分流層的分流出口」係為同一個;又,該第一分流通道801相接次一分流層的分流入口,與該第二分流通道802相接次一分流層的分流入口,所稱的「次一分流層的分流入口」為不同的分流入口。The aforementioned
本實施例中,特別的是將該第一分流通道801的寬度設計成小於該第二分流通道802,據此使得該第一分流通道801的通道截面積係小於該第二分流通道802的通道截面積。於實際使用時,最後一該分流層的各該分流出口配接該噴嘴用以提供噴出發泡材料的目的,且各該分流段可依灌注成品斷面尺寸的需要,規劃不同的寬度或深度,以達到使原料依成品斷面位置噴出對應的流量之需求。In this embodiment, in particular, the width of the
請參閱第7圖,舉例而言,當本創作用於噴塗一浪板94時,該浪板94具有複數個凹槽96,二該凹槽96之間具有一平面部98,連接在具有較小截面積的該第一分流通道801的該噴嘴38相對該平面部98,連接在具有較大截面積的該第二分流通道802的該噴嘴38相對該凹槽96,由於該第二分流通道802的通道寬度大於該第一分流通道801的通道寬度,致使該凹槽96內該材料(發泡材)90的噴塗量大於該平面部表面該材料90的噴塗量,如此便能具有依成品表面結構噴出對應流量之功效,致使該浪板94各位置的該材料(發泡材)90膨脹後可以具有一致的高度,以免除該浪板94的發泡層膨脹不均的情形。Please refer to FIG. 7. For example, when the present invention is used to spray a
由上述各實施例中得知,原物料導入該等比式分流管路系統20至各該噴嘴38的距離都是相同的情況下,該材料於各分流段內的流速也是一致的,除了不會產生因材料流速過慢而提早於分流段內結膜造成阻塞的問題,更可延長該發泡材流量分配噴嘴的使用壽命。此外,本創作可用於低壓氣噴混和的噴塗方式,如此便能降低設備成本,達到成本較低之目的。It is known from the above embodiments that when the distance between the raw material introduced into the proportional
以上所述僅為說明本發明的例示,並非對本發明做任何形式上的限制,本發明所主張之權利範圍自應以申請專利範圍所述為準,而非僅限於上述實施例。任何所屬技術領域中具有通常知識者,在不脫離本發明技術方案的範圍內,當可利用上述揭示的技術內容做出些許更動或修飾為等同變化的等效實施例,但凡是未脫離本發明之技術方案的內容,均仍屬於本發明技術方案的範圍內。The above is merely an illustration for illustrating the present invention, and does not limit the present invention in any form. The scope of the rights claimed by the present invention should be subject to the scope of the patent application, not limited to the above embodiments. Any person with ordinary knowledge in the technical field of the art can use the technical contents disclosed above to make some alterations or modifications to equivalent equivalent embodiments without departing from the scope of the technical solutions of the present invention, but those who do not deviate from the present invention The contents of the technical solutions are still within the scope of the technical solutions of the present invention.
10‧‧‧外管件20‧‧‧等比式分流管路系統22、60‧‧‧第一分流層24、62‧‧‧第一分流段25‧‧‧第一分流通道26、64‧‧‧第一分流入口27‧‧‧第二分流通道28、66‧‧‧第一分流出口30、70‧‧‧第二分流層32、72‧‧‧第二分流段34、74‧‧‧第二分流入口36、76‧‧‧第二分流出口38‧‧‧噴嘴40‧‧‧第三分流層42‧‧‧第三分流段44‧‧‧第三分流入口46‧‧‧第三分流出口50‧‧‧第四分流層52‧‧‧第四分流段54‧‧‧第四分流出口80‧‧‧分流段801‧‧‧第一分流通道802‧‧‧第二分流通道803‧‧‧分流入口90‧‧‧材料92‧‧‧平板94‧‧‧浪板96‧‧‧凹槽98‧‧‧平面部10‧‧‧
第1圖為本發明第一實施例的架構平面圖。 第2圖為本發明第一實施例分流段的平面圖。 第3圖為本發明第二實施例的架構平面圖。 第4圖為本發明第三實施例的架構平面圖。 第5圖為本發明第一實施例的使用狀態圖。 第6圖為本發明第四實施例分流段的平面圖。 第7圖為本發明第四實施例的使用狀態圖。FIG. 1 is a plan view of the architecture of the first embodiment of the present invention. Fig. 2 is a plan view of the splitter section of the first embodiment of the invention. FIG. 3 is an architectural plan view of a second embodiment of the invention. FIG. 4 is a plan view of the architecture of the third embodiment of the present invention. Fig. 5 is a diagram showing the state of use of the first embodiment of the present invention. Fig. 6 is a plan view of a split section according to a fourth embodiment of the invention. FIG. 7 is a usage state diagram of the fourth embodiment of the present invention.
20‧‧‧等比式分流管路系統 20‧‧‧Proportional shunt piping system
22‧‧‧第一分流層 22‧‧‧The first tributary layer
38‧‧‧噴嘴 38‧‧‧ nozzle
50‧‧‧第四分流層 50‧‧‧The fourth shunt
52‧‧‧第四分流段 52‧‧‧The fourth branch
54‧‧‧第四分流出口 54‧‧‧The fourth diversion outlet
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