JPH0459070A - Device for coating latticed substrate with adhesive - Google Patents
Device for coating latticed substrate with adhesiveInfo
- Publication number
- JPH0459070A JPH0459070A JP2164080A JP16408090A JPH0459070A JP H0459070 A JPH0459070 A JP H0459070A JP 2164080 A JP2164080 A JP 2164080A JP 16408090 A JP16408090 A JP 16408090A JP H0459070 A JPH0459070 A JP H0459070A
- Authority
- JP
- Japan
- Prior art keywords
- adhesive
- substrate
- bath
- filter
- conveyor
- 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.)
- Granted
Links
- 239000000853 adhesive Substances 0.000 title claims abstract description 59
- 230000001070 adhesive effect Effects 0.000 title claims abstract description 59
- 239000000758 substrate Substances 0.000 title claims abstract description 57
- 239000011248 coating agent Substances 0.000 title claims description 17
- 238000000576 coating method Methods 0.000 title claims description 17
- 238000007664 blowing Methods 0.000 claims abstract description 6
- 239000007788 liquid Substances 0.000 claims description 4
- 238000007598 dipping method Methods 0.000 abstract description 10
- 239000012790 adhesive layer Substances 0.000 abstract description 5
- 238000011109 contamination Methods 0.000 abstract 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 38
- 239000002245 particle Substances 0.000 description 13
- 239000003463 adsorbent Substances 0.000 description 11
- 230000001877 deodorizing effect Effects 0.000 description 10
- 239000000463 material Substances 0.000 description 8
- 238000005520 cutting process Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000000123 paper Substances 0.000 description 6
- 238000007873 sieving Methods 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000005470 impregnation Methods 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 244000043261 Hevea brasiliensis Species 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical group [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920003052 natural elastomer Polymers 0.000 description 1
- 229920001194 natural rubber Polymers 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000013464 silicone adhesive Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Coating Apparatus (AREA)
- Treating Waste Gases (AREA)
- Separation Of Gases By Adsorption (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は格子状基体の粘着剤塗布装置に関し、特に、フ
ィルタ基体と該フィルタ基体に接着された活性炭粒子と
からなるニアコンディショナ用脱臭フィルタの製造シス
テムにおいて、上記格子状基体に粘着剤を塗布する為の
装置に関する。Detailed Description of the Invention [Industrial Field of Application] The present invention relates to an adhesive coating device for a grid-like substrate, and more particularly to a deodorizing filter for near conditioners comprising a filter substrate and activated carbon particles adhered to the filter substrate. The present invention relates to an apparatus for applying an adhesive to the lattice-shaped substrate in the manufacturing system.
[従来の技術]
本件出願人は、特願平L−258748号において、格
子状のフィルタ基体と、フィルタ基体に接着されたガス
吸着剤(主に活性炭)粒子とからなるフィルタを提案し
ている。このフィルタは、上記基体の厚さ一約15mm
以下、上記基体の格子の1セルの平面積=約0.20−
約[]、335cm2上記ガス吸着剤粒子の寸法−約2
0−約BOメツシュ、上記基体平面単位面積当りのガス
吸着剤粒子の使用量−約400約2000g/m2、本
フィルタの開口率−約50−約80%、の条件を満たす
ことを特徴とする。[Prior Art] In Japanese Patent Application No. 258,748, the applicant has proposed a filter consisting of a lattice-shaped filter base and gas adsorbent (mainly activated carbon) particles adhered to the filter base. . This filter has a thickness of about 15 mm on the base.
Hereinafter, the planar area of one cell of the lattice of the above substrate = approximately 0.20-
Approximately [], 335 cm2 Dimensions of the above gas adsorbent particles - approx.
It is characterized by satisfying the following conditions: 0 - about BO mesh, the amount of gas adsorbent particles used per unit area of the plane of the substrate - about 400 about 2000 g/m2, and the aperture ratio of the filter - about 50 - about 80%. .
要約すると、このフィルタは、活性炭(ガス吸着剤)粒
子の寸法が比較的大きく、またフィルタの厚さが小さい
点で、従来のフィルタと異なる。In summary, this filter differs from conventional filters by the relatively large size of the activated carbon (gas adsorbent) particles and by the small thickness of the filter.
従って、フィルタ基体の取扱い、活性炭の添着等に関し
、従来品とは異なる特別の配慮が必要となる。特に使用
される粘着剤液は高粘度(約10〜50ポイズ)である
ことが必須となる。Therefore, special consideration, which is different from conventional products, is required regarding handling of the filter base, impregnation of activated carbon, etc. In particular, it is essential that the adhesive liquid used has a high viscosity (approximately 10 to 50 poise).
従来のこの種フィルタの製造システムにおいて使用され
ている基体の粘着剤塗布装置は、スプレーによって粘着
剤を基体に吹付ける構造が主流である。Adhesive coating devices for substrates used in conventional manufacturing systems for this kind of filters have a structure in which the adhesive is sprayed onto the substrate by spraying.
[発明が解決しようとする課題]
上記従来のスプレー式塗布装置にあっては、しかし、本
発明が対象としている粘性の高い粘着剤を使用しようと
しても、良好な分散状態の粘着剤ミストの形成が難しく
、粘着剤を基体表面全域に亘って均一に塗布することが
できないという問題が生じる。またスプレー式塗布装置
は周囲環境を汚染するという問題もある。[Problems to be Solved by the Invention] However, in the above-mentioned conventional spray-type coating device, even if the highly viscous adhesive targeted by the present invention is used, it is difficult to form a well-dispersed adhesive mist. The problem arises that it is difficult to apply the adhesive uniformly over the entire surface of the substrate. There is also the problem that spray-type coating devices contaminate the surrounding environment.
本発明はかかる観点に基づいてなされたものであり、基
体表面全域に亘る均一な粘着剤塗布が可能であると共に
、周囲環境を汚染しない粘着剤塗布装置を提供すること
と目的とする。The present invention has been made based on this viewpoint, and an object of the present invention is to provide an adhesive coating device that can uniformly apply an adhesive over the entire surface of a substrate and does not contaminate the surrounding environment.
[課題を解決する為の手段]
上記目的を達成する為、本発明塗布装置にあっては、高
粘度の粘着剤の浴と、展張した格子状フィルタ基体を上
記浴の液面に沿って前進させる搬送部材と、上記基体を
順次上記粘着剤浴中に強制的に浸漬する押込み部材と、
上記粘着剤の余分を排除する為に浸漬後の上記基体にエ
アを吹付ける吹払い部材と、を具備することを特徴とす
る。[Means for Solving the Problems] In order to achieve the above object, in the coating device of the present invention, a bath of a high viscosity adhesive and a stretched lattice-shaped filter substrate are advanced along the liquid surface of the bath. a pushing member that forcibly immerses the substrate in the adhesive bath in order;
The present invention is characterized by comprising a blowing member that blows air onto the substrate after immersion in order to remove excess adhesive.
望ましい態様において、上記押込み部材は回転バーであ
り、また上記粘着剤の初期粘度は約10〜50ポイズ、
上記エアの風速は約30〜250 m/secである。In a preferred embodiment, the pushing member is a rotating bar, and the adhesive has an initial viscosity of about 10 to 50 poise,
The speed of the air is about 30 to 250 m/sec.
[作 用]
上記構成により本発明に係る装置によれば、フィルタ基
体は、押込み部材(回転バー)によって、高粘度の粘着
剤の浴中に強制的に浸漬される。上記浸漬は、基体の格
子の開口方向に沿って概ね平行に行われ、気泡が形成さ
れることなく、基体の全体に亘って厚い高粘度の粘着剤
層が形成される。[Function] According to the device according to the present invention having the above configuration, the filter base is forcibly immersed in a bath of high viscosity adhesive by the pushing member (rotary bar). The above dipping is performed generally parallel to the opening direction of the lattice of the substrate, and a thick, highly viscous adhesive layer is formed over the entire substrate without forming bubbles.
粘着剤塗布後、基体の格子に膜を張っているような余分
な粘着剤が、吹払い部材のエアによって除去される。After the adhesive is applied, the excess adhesive that forms a film on the grid of the base is removed by air from a blowing member.
[実施例]
フィルタの構造及び材質
第2図は本発明に係る装置により処理する脱臭フィルタ
ー0の一例を示す平面図である。このフィルタは、格子
状のフィルタ基体12と、フィルタ基体12に接着され
たガス吸着剤粒子14とからなる。[Example] Filter Structure and Materials FIG. 2 is a plan view showing an example of a deodorizing filter 0 processed by the apparatus according to the present invention. This filter consists of a grid-like filter base 12 and gas adsorbent particles 14 adhered to the filter base 12.
脱臭フィルター0は開口率(第2図の紙面に対して平行
な平面における)が約50−約80%で、この値は後述
する種々の条件に従う結果として得られる。またフィル
ター0の厚さ(第2図の紙面に対して垂直な方向)は1
5nv以下で望ましくは約3nun以上となっている。Deodorizing filter 0 has an aperture ratio (in a plane parallel to the paper plane of FIG. 2) of about 50 to about 80%, and this value is obtained as a result of complying with various conditions described below. Also, the thickness of filter 0 (in the direction perpendicular to the paper surface of Fig. 2) is 1
It is 5 nv or less, preferably about 3 nun or more.
本フィルター0は、第2図図示の如くガス吸着剤粒子1
4の寸法が比較的大きく、またフィルター0の厚さが小
さい点で、従来のフィルタと異なる。これらの特徴は、
ニアコンディショナ用の脱臭フィルタとして、低圧力損
失、適当な脱臭能力、長寿命等の条件を満たす為の鍵と
なる。This filter 0 has gas adsorbent particles 1 as shown in FIG.
It differs from conventional filters in that the dimensions of filter 4 are relatively large and the thickness of filter 0 is small. These characteristics are
As a deodorizing filter for near conditioners, it is the key to meeting the requirements of low pressure loss, appropriate deodorizing ability, and long life.
基体12は、紙、アルミ、プラスチック等の薄肉の材料
からなる。紙を材料として用いる場合は、フェノール樹
脂等を含浸させて強度を補強することもできる。また基
体12には不燃化処理を施すこともできる。基体12の
厚さは実質的に本フィルタ10の厚さとなるから、約1
5n+m以下で望ましくは3n+m以上となる。この厚
さは、本フィルター0が最終的にニアコンディショナの
筐体内に収納されることから決定される。The base 12 is made of a thin material such as paper, aluminum, or plastic. When paper is used as a material, it can be impregnated with phenol resin or the like to strengthen the paper. Further, the base body 12 can also be subjected to a non-combustible treatment. The thickness of the base 12 is substantially the same as that of the present filter 10, so it is approximately 1
It is preferably 5n+m or less, preferably 3n+m or more. This thickness is determined because the present filter 0 is finally housed in the casing of the near conditioner.
図示例において、基体12の格子のパターン形状は6角
形のいわゆるハニカム状となっているが、このパターン
形状は、例えば矩形、3角形等いかなる形状とすること
もできる。但し、格子の1つのセル16の平面積(第2
図の紙面に対して平行な平面における)は約0.20−
約0.35cm2となる。この数値は、ガス吸着剤粒子
14を支持する為の区画壁18の密度を実質的に意味す
ることとなる。In the illustrated example, the pattern shape of the lattice of the base body 12 is a hexagonal so-called honeycomb shape, but the pattern shape can be any shape such as a rectangle or a triangle. However, the planar area of one cell 16 of the grid (second
) is approximately 0.20-
It will be about 0.35 cm2. This value essentially means the density of the partition wall 18 for supporting the gas adsorbent particles 14.
ガス吸着剤粒子14は活性炭からなるが、添着活性炭等
能のタイプのものを使用することも可能である。また石
油ストーブ等室内のCO発生源に対処する為、COを接
触酸化処理できる触媒を脱臭剤と併用することができる
。この触媒としては、水分があっても死活しない金/酸
化物触媒(特開昭60−238148等で開示される)
が望ましい。ガス吸着剤粒子14の寸法は約20−約B
ロメ・ソシュ、基体12の平面単位面積当りのガス吸着
剤粒子14の使用量は約400−約2[100g /
m 2である。The gas adsorbent particles 14 are made of activated carbon, but it is also possible to use a type of impregnated activated carbon or the like. Further, in order to deal with indoor CO generation sources such as oil stoves, a catalyst capable of catalytically oxidizing CO can be used in combination with a deodorizer. This catalyst is a gold/oxide catalyst that does not become inactive even in the presence of moisture (disclosed in JP-A-60-238148, etc.)
is desirable. The size of the gas adsorbent particles 14 is about 20 to about B.
Lomé Soche, the amount of gas adsorbent particles 14 used per planar unit area of the substrate 12 is about 400 to about 2 [100 g /
m2.
ガス吸着剤粒子14を基体12に接着する為のバインダ
は、粒子の脱落を防止する為に粘着剤が使用されること
が望ましい。粘着剤としては、アクリル系、天然ゴム系
、合成ゴム系、シリコーン系等公知のものが使用可能で
あるが、活性炭の脱落がないように強くフィルタ基体に
接着する為には、濃度の濃い粘着剤が使用され、且つそ
の層厚がある程度厚くなることが要求される。従って、
使用される粘着剤液は高粘度(約10〜50ポイズ)で
、その塗布方法は厚い層厚の得られる方法によらなけれ
ばならない。As the binder for adhering the gas adsorbent particles 14 to the substrate 12, an adhesive is preferably used to prevent the particles from falling off. Known adhesives such as acrylic, natural rubber, synthetic rubber, and silicone adhesives can be used, but in order to strongly adhere to the filter base so that the activated carbon does not fall off, it is necessary to use a highly concentrated adhesive. agent is used and the layer thickness is required to be thick to some extent. Therefore,
The adhesive fluid used has a high viscosity (approximately 10 to 50 poise) and the method of application must be such that a large layer thickness is obtained.
製造システム全容
第3図は本発明に係る塗布装置を組込むニアコンディシ
ョナ用脱臭フィルタの製造システムの一例の全体を示す
平面図である。Overall view of manufacturing system FIG. 3 is a plan view showing an entire example of a manufacturing system for a near conditioner deodorizing filter incorporating the coating device according to the present invention.
本システムの入口には、未展張状態のフィルタ基体、即
ち、格子が潰れた状態のフィルタ基体を、本システム内
に導入する為の導入部が形成される。An introduction part is formed at the entrance of the system for introducing the filter base in an unexpanded state, that is, the filter base in which the lattice is collapsed, into the system.
本システムでは、未展張状態の材料ブロックがそのまま
導入及び処理可能である為、材料の運搬、貯蔵において
手間や費用を削減することが可能となる。With this system, unexpanded material blocks can be introduced and processed as they are, making it possible to reduce the labor and costs involved in transporting and storing materials.
導入部には、フリーローラコンベア(導入機)22.2
3が配設され、これらは第2図の紙面と平行な方向に基
体12を連続的に導入する。コンベア22.23の中間
には展張機24が設置され、これは水分及び熱の作用に
より、基体を展張、即ち、格子が開いた状態とする。コ
ンベア23に続いて、ピンコンベア26が配設され、こ
れは展張後の基体の格子にピンを引掛けることにより基
体を搬送する。In the introduction section, there is a free roller conveyor (introduction machine) 22.2
3 are arranged, which successively introduce the substrate 12 in a direction parallel to the plane of the paper of FIG. A spreading machine 24 is installed in the middle of the conveyors 22, 23, which spreads the substrates, ie, opens the grid, by the action of moisture and heat. A pin conveyor 26 is disposed following the conveyor 23, and this conveys the substrate by hooking pins on a grid of the expanded substrate.
コンベア26に続いて、展張状態の基体に高粘度の粘着
剤を供給する為の浸漬機28が配設される。浸漬機28
は高粘度(約10〜50ポイズ)の粘着剤洛中に基体1
2を強制的に浸漬し、該基体の全域に亘って厚い粘着剤
層を形成するタイプからなる。この際、粘着剤は高粘度
である為、格子内に膜を張る場合が多いと考えられる。Following the conveyor 26, a dipping machine 28 is disposed for supplying a high viscosity adhesive to the stretched substrate. Soaking machine 28
The substrate 1 is coated with a high viscosity (approximately 10 to 50 poise) adhesive.
2 is forcibly immersed to form a thick adhesive layer over the entire area of the substrate. At this time, since the adhesive has a high viscosity, it is thought that a film is often applied within the grid.
従って、このまま乾燥させると、完成フィルタの圧力損
失、の増大、脱臭性能の低下、寿命の短縮等の原因とな
る。これを回避する為、本システムでは、粘着剤の余分
をエアにより排除する吹払い機32が、浸漬機28の後
に配設される。粘着剤は高粘度である為、粘着剤に当た
るエアの風速は相当速い(約30〜250 m/sec
)ことが望ましい。Therefore, if the filter is allowed to dry as it is, it will cause an increase in pressure loss, a decrease in deodorizing performance, and a shortened service life of the finished filter. In order to avoid this, in this system, a blower 32 for removing excess adhesive with air is disposed after the dipping machine 28. Since the adhesive has a high viscosity, the air velocity hitting the adhesive is quite high (approximately 30 to 250 m/sec).
) is desirable.
吹払い機32の後にはコンベア26と同様なピンコンベ
ア34が配設され、これは、次の乾燥機36のピンコン
ベアに基体12を引渡す。上述のような構成である為、
図示のシステムにおいては、新たな基体材料ブロックを
使用する際は、基体先端の格子が乾燥機36のピンコン
ベアのピンに引掛かるまで、手作業で基体材料を入口側
から導入することとなる。A pin conveyor 34 similar to conveyor 26 is arranged after the blower 32, which transfers the substrate 12 to the pin conveyor of the next dryer 36. Since the configuration is as described above,
In the illustrated system, when using a new block of substrate material, the substrate material is manually introduced from the inlet side until the grid at the tip of the substrate catches the pins of the pin conveyor of the dryer 36.
乾燥機36は基体]2を加熱することにより、該基体に
塗布された粘着剤の水分含量を所定量まで低下させる。The dryer 36 heats the substrate 2 to reduce the moisture content of the adhesive applied to the substrate to a predetermined amount.
これにより、粘着剤に所定の粘性が付与されると共に、
溶剤の匂いが飛ばされる。This gives the adhesive a predetermined viscosity, and
The smell of solvent is blown away.
−膜内には、粘着剤の初期水分含量は70重量%程度で
あり、これを乾燥機36の出口では10重量%以下、望
ましくは3重量%程度まで低下させる。- In the membrane, the initial moisture content of the adhesive is around 70% by weight, which is reduced to less than 10% by weight, preferably around 3% by weight at the outlet of the dryer 36;
また、粘着剤の塗布層が厚い程、乾燥工程中での発泡が
生じやすいので、この乾燥は、中程度の温度(約60〜
100℃)で、長時間(約10〜30分)かけて行われ
ることが望ましい。In addition, the thicker the adhesive coating layer, the more likely it is that foaming will occur during the drying process, so drying should be carried out at a moderate temperature (approximately 60 - 60℃).
100° C.) for a long period of time (about 10 to 30 minutes).
乾燥後、基体12は完成ニアコンディショナ用フィルタ
の為の所定寸法に裁断される。粘着剤が乾燥した基体は
、それ自体がかなりの強度を有するようになる為、裁断
は正確に行うことが可能となる。また活性炭の添着前に
裁断を行うことは、裁断刃の寿命を長めるという利点が
ある。しかし、活性炭の添着後に基体の裁断を行うよう
にすることも可能である。After drying, the substrate 12 is cut to size for the finished near conditioner filter. The substrate after the adhesive has dried has considerable strength, so it is possible to cut it accurately. Furthermore, cutting before impregnating activated carbon has the advantage of extending the life of the cutting blade. However, it is also possible to cut the substrate after impregnating the activated carbon.
より具体的には、乾燥機36の山口には、第1の裁断機
38が設置され、これはコンベア22から乾燥機36ま
での長手軸方向を直角に横断する方向に基体]2を裁断
する。これに続いて方向変換機構44か配設され、裁断
機38により裁断された基体12を、ローラコンベア4
2から、これと直角な搬送方向のローラコンベア46に
移管する。コンベア46の終端には、第2の裁断機48
が設置され、これはコンベア46の長手軸方向を直角に
横断する方向に基体]2を裁断し、該基体を上述の所定
寸法とする。More specifically, a first cutting machine 38 is installed at the top of the dryer 36, and this cuts the substrate 2 in a direction perpendicularly crossing the longitudinal axis direction from the conveyor 22 to the dryer 36. . Following this, a direction changing mechanism 44 is disposed, and the substrate 12 cut by the cutter 38 is transferred to a roller conveyor 4.
2 to a roller conveyor 46 in a conveying direction perpendicular to this. At the end of the conveyor 46, a second cutting machine 48 is installed.
is installed, which cuts the base body] 2 in a direction perpendicularly transverse to the longitudinal axis direction of the conveyor 46, and makes the base body have the above-mentioned predetermined dimensions.
第2裁断機48に続いて、所定寸法の基体12に上記粘
着剤を介して活性炭を添着する添着機54が配置される
。添着機54は、その底壁を構成する振動コンベア機構
により基体12を前進させる。添着機54の側部には、
添着機54に対して上方から降注ぐように活性炭を基体
12に向けて供給する為の活性炭供給機52が配設され
る。Following the second cutting machine 48, an impregnating machine 54 is disposed to apply activated carbon to the substrate 12 of a predetermined size via the adhesive. The applicator 54 advances the base body 12 by means of a vibrating conveyor mechanism that constitutes its bottom wall. On the side of the applicator 54,
An activated carbon feeder 52 is provided to feed activated carbon toward the base 12 so as to fall from above onto the impregnation device 54 .
添着機54の後部には活性炭の一部を脱落させるふるい
部56が設置される。A sieve part 56 is installed at the rear of the impregnation machine 54 to remove a part of the activated carbon.
添着機54の出口には、ベルトコンベア58がコンベア
44に対して直角に配設される。コンベア58の終端に
は、活性炭の一部を摩擦作用により脱落させる摩擦機6
2が設置され、更にその後に振動ふるい機64が設置さ
れる。At the outlet of the applicator 54, a belt conveyor 58 is arranged at right angles to the conveyor 44. At the end of the conveyor 58, there is a friction machine 6 that causes part of the activated carbon to fall off due to frictional action.
2 is installed, and then a vibrating sieve 64 is installed.
基体12上に添着された活性炭には、基体に強固に固定
されたものと、弱<(=1着しているものとが存在する
。弱く付着している活性炭は、その後の接触、振動等に
より容易に脱落して、環境を汚染するおそれがある為、
製造工程中に脱落させることが望ましいものとなる。そ
の脱落方法は、振動コンベア等の衝撃力による方法、遠
心力による方法、或いはブラシ、粗目のやすり等の摩擦
による方法等があり、これらの一つ或いは複数を任意に
選択することが可能となる。図示のシステムにおいて、
ふるい部56及びふるい機64は振動コンベアの衝撃力
により、また摩擦機62はやすりの回転摩擦力により不
要な活性炭を脱落させる。There are two types of activated carbon attached to the base 12: those that are firmly fixed to the base and those that are weakly attached. Activated carbon that is weakly attached is susceptible to subsequent contact, vibration, etc. It may fall off easily and contaminate the environment.
It is desirable that they fall off during the manufacturing process. The falling off method includes a method using an impact force such as a vibrating conveyor, a method using a centrifugal force, a method using a friction method such as a brush or a coarse file, etc., and it is possible to arbitrarily select one or more of these methods. . In the illustrated system,
The sieving unit 56 and the sieving machine 64 remove unnecessary activated carbon by the impact force of the vibrating conveyor, and the friction machine 62 uses the rotating friction force of the file.
ふるい機64に続いて公知の態様の梱包部66が配設さ
れる。不要な活性炭を落とされたフィルタ基体は、ここ
で、完成ニアコンディショナ用脱臭フィルタとして、出
荷に相応しい姿に、袋、段ボール或いはそれらの併用に
より梱包される。またここで、ヒーI・シール等の手段
を用い、完成)ィルタの周囲を不織布、網等の通気材料
で包囲し、外観及び品質を向上させることもできる。Following the sieving machine 64, a packaging section 66 in a known manner is arranged. The filter base from which unnecessary activated carbon has been removed is then packaged as a completed near conditioner deodorizing filter in a form suitable for shipping in a bag, cardboard, or a combination thereof. In addition, it is also possible to improve the appearance and quality by surrounding the completed filter with a ventilation material such as a non-woven fabric or a net using a heat seal or the like.
塗布装置
第1図は本発明に係る塗布装置の要部を拡大して示す概
略側面図、第4図はその平面図である。Coating Apparatus FIG. 1 is a schematic side view showing an enlarged main part of the coating apparatus according to the present invention, and FIG. 4 is a plan view thereof.
浸漬機28及び吹払い機32は、隔壁144で分割され
た共通のケーシング142を具備し、浸漬機28側には
高粘度(約lO〜50ポイズ)の粘着剤143が貯液さ
れる。ケーシング142の下部には、各分割槽内のドレ
インを排除する為の配管166、配管168が夫々取付
けられる。The dipping machine 28 and the blowing machine 32 have a common casing 142 divided by a partition wall 144, and a high-viscosity adhesive 143 (approximately 10 to 50 poise) is stored on the dipping machine 28 side. Piping 166 and piping 168 are attached to the lower part of the casing 142, respectively, for removing the drain in each divided tank.
粘着剤浴の上部には、90°間隔で4つの矩形枠を軸支
した態様の回転バー152が配設され、これはモータ1
54によって、第1図中矢印方向に、連続的に駆動され
る。基体12は、浸漬機28人口のローラ146、吹払
い機32のガイド]56及び出口ローラ148の間を架
橋状態で移動する。A rotary bar 152 having four rectangular frames pivoted at 90° intervals is disposed above the adhesive bath, and this is connected to the motor 1.
54, it is continuously driven in the direction of the arrow in FIG. The substrate 12 moves in a bridge between the rollers 146 of the dipper 28, the guides 56 of the blower 32, and the exit rollers 148.
回転バー152は押込み部材として機能し、これによっ
て基体12が粘着剤浴中に強制的に浸漬される。The rotating bar 152 functions as a pusher, thereby forcing the substrate 12 into the adhesive bath.
吹払い機32において、ガイド156の上部には2本の
高圧エア配管162が配設される。6管162には千鳥
状配列に複数(例えば14個)の下向きジェットノズル
]64が付設され、ここから、ガイド156を通過する
基体]2に対して高速のエア(約30〜250 m/s
ec )か連続的に吹付けられる。第5図及び第6図図
示の如く、各エアノズル164は室状の本体166の先
端に14箇所の噴用口168が形成された構造をなす。In the blower 32, two high pressure air pipes 162 are arranged above the guide 156. A plurality of (for example, 14) downward jet nozzles] 64 are attached to the pipe 162 in a staggered arrangement, and from here, high-speed air (about 30 to 250 m/s
ec) or sprayed continuously. As shown in FIGS. 5 and 6, each air nozzle 164 has a structure in which 14 injection ports 168 are formed at the tip of a chamber-shaped main body 166.
本体166の根元にはねじ部172が形成され、これを
介してノズル]64がエア配管162に付設された枝管
163に接続される。A threaded portion 172 is formed at the base of the main body 166, through which the nozzle 64 is connected to a branch pipe 163 attached to the air pipe 162.
上記塗布装置にあっては、基体12は、ピンコンベア3
4(第3図参照)の引張り作用により、粘着剤浴の液面
上を前進し、回転バー152によって順次粘着剤浴中に
強制的に浸漬される。この浸漬は、基体12の格子の開
口方向に沿って概ね平行に行われ、従って、気泡が形成
されないように基体12の全体に亘って厚い粘着剤層が
速やかに形成可能となる。また浸漬に続き、基体12に
対して高速のエアが吹付けられ、これによって、基体1
2の格子に膜を張ったような余分な粘着剤が除去される
。In the coating device described above, the base 12 is connected to the pin conveyor 3.
4 (see FIG. 3), they are moved forward on the liquid surface of the adhesive bath, and are forced to be sequentially immersed into the adhesive bath by the rotating bar 152. This dipping is performed generally parallel to the opening direction of the lattice of the substrate 12, so that a thick adhesive layer can be quickly formed over the entire substrate 12 without forming air bubbles. Further, following the immersion, high-speed air is blown against the base 12, thereby causing the base 12 to
The excess adhesive that was covered with a film on the lattice in step 2 is removed.
以上、本発明は図示の望ましい実施例に沿って詳述した
が、本発明装置が属する技術分野の当業者によれば、本
発明の思想の範囲において、上記実施例に対して種々変
更か可能となるであろう。Although the present invention has been described in detail in accordance with the preferred embodiments shown in the drawings, those skilled in the art to which the present invention pertains will appreciate that various modifications can be made to the above embodiments within the scope of the spirit of the present invention. It will be.
[発明の効果]
本発明によれば、フィルタ基体を、粘着剤浴中に強制的
に浸漬して粘着剤を塗布した後、基体の格子に膜を張っ
ているような余分な粘着剤をエアにより吹払うようにし
た為、高粘度の粘着剤を使用することが可能となる。[Effects of the Invention] According to the present invention, after a filter substrate is forcibly immersed in an adhesive bath to apply an adhesive, excess adhesive that forms a film on the grid of the substrate is removed by air. Since the adhesive is blown away, it is possible to use a highly viscous adhesive.
また上記浸漬は、基体の格子の開口方向に沿って概ね平
行に行われる為、高粘度の粘着剤を使用しても、気泡が
形成されることなく、基体の全体に亘って厚い粘着剤層
を速やかに形成可能となる。In addition, since the above dipping is performed generally parallel to the opening direction of the lattice of the substrate, even if a high viscosity adhesive is used, no air bubbles will be formed and a thick adhesive layer will be formed over the entire substrate. can be formed quickly.
また更に浸漬式である為、従来のスプレー式の塗布装置
と比べ、周囲環境を汚染する可能性も少なくなる。Furthermore, since it is a dipping type coating device, there is less possibility of contaminating the surrounding environment compared to conventional spray type coating equipment.
第1図は本発明に係る塗布装置の要部を拡大して示す概
略側面図である。
第2図は本発明に係る装置により処理する脱臭フィルタ
の一例を示す平面図である。
第3図は本発明に係る塗布装置を絹込むニアコンディシ
ョナ用脱臭フィルタの製造システムの一例の全体を示す
平面図である。
第4図は本発明に係る塗布装置の要部を拡大して示す概
略平面図である。
第5図及び第6図はエアジェツトノズルを拡大して示す
正面図及び側面図である。
22.23・・・フリーローラコンベア、24・・・展
張機、26・・・ピンコンベア、28・・・浸漬機、3
2・・・吹払い機、36・・乾燥機、38・・・第1裁
断機、44・・・方向変換機構、48・・・第2裁断機
、52・・・活性炭供給機、54・・・添着機、62・
・・摩擦機、64・・・ふるい機、66・・梱包部、1
42・・・ケーシング、143・・・粘着剤、152・
・回転バ164・・・エアノズル。
第
図
=439FIG. 1 is a schematic side view showing an enlarged main part of a coating device according to the present invention. FIG. 2 is a plan view showing an example of a deodorizing filter processed by the apparatus according to the present invention. FIG. 3 is a plan view showing the entirety of an example of a manufacturing system for a deodorizing filter for a near conditioner in which a coating device according to the present invention is installed. FIG. 4 is a schematic plan view showing an enlarged main part of the coating device according to the present invention. FIGS. 5 and 6 are front and side views showing an enlarged view of the air jet nozzle. 22.23... Free roller conveyor, 24... Expanding machine, 26... Pin conveyor, 28... Soaking machine, 3
2... Blowing machine, 36... Dryer, 38... First cutting machine, 44... Direction changing mechanism, 48... Second cutting machine, 52... Activated carbon supply machine, 54...・・Applying machine, 62・
... Friction machine, 64 ... Sieving machine, 66 ... Packing department, 1
42...Casing, 143...Adhesive, 152.
- Rotating bar 164...Air nozzle. Figure = 439
Claims (1)
体を上記浴の液面に沿って前進させる搬送部材と、上記
基体を順次上記粘着剤浴中に強制的に浸漬する押込み部
材と、上記粘着剤の余分を排除する為に浸漬後の上記基
体にエアを吹付ける吹払い部材と、を具備することを特
徴とする格子状基体の粘着剤塗布装置 2、上記押込み部材が回転バーである請求項1記載の装
置。 3、上記粘着剤の初期粘度が約10〜50ポイズである
請求項1または2記載の装置。 4、上記エアの風速が約30〜250m/secである
請求項1乃至3のいずれかに記載の装置。[Claims] 1. A conveying member that advances a bath of a high viscosity adhesive and a stretched grid-like filter substrate along the liquid surface of the bath, and forcibly moves the substrate sequentially into the adhesive bath. An adhesive coating device for a lattice-shaped substrate 2, characterized in that it is equipped with a pushing member that is immersed in the adhesive, and a blowing member that blows air onto the substrate after being immersed in order to remove excess adhesive. 2. The device of claim 1, wherein said pushing member is a rotating bar. 3. The device of claim 1 or 2, wherein the adhesive has an initial viscosity of about 10 to 50 poise. 4. The apparatus according to any one of claims 1 to 3, wherein the air velocity is about 30 to 250 m/sec.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2164080A JP2948871B2 (en) | 1990-06-25 | 1990-06-25 | Adhesive coating device for lattice-like substrate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2164080A JP2948871B2 (en) | 1990-06-25 | 1990-06-25 | Adhesive coating device for lattice-like substrate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0459070A true JPH0459070A (en) | 1992-02-25 |
| JP2948871B2 JP2948871B2 (en) | 1999-09-13 |
Family
ID=15786402
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2164080A Expired - Fee Related JP2948871B2 (en) | 1990-06-25 | 1990-06-25 | Adhesive coating device for lattice-like substrate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2948871B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108704394A (en) * | 2018-05-25 | 2018-10-26 | 江苏鼎盛滤袋有限公司 | A kind of non-woven filter bag processing equipment of nonwoven |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5417311B2 (en) | 2010-12-14 | 2014-02-12 | リンナイ株式会社 | Cooking equipment |
-
1990
- 1990-06-25 JP JP2164080A patent/JP2948871B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108704394A (en) * | 2018-05-25 | 2018-10-26 | 江苏鼎盛滤袋有限公司 | A kind of non-woven filter bag processing equipment of nonwoven |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2948871B2 (en) | 1999-09-13 |
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