JPS6055282B2 - Method for manufacturing air cleaner cover seal packing - Google Patents

Method for manufacturing air cleaner cover seal packing

Info

Publication number
JPS6055282B2
JPS6055282B2 JP52054577A JP5457777A JPS6055282B2 JP S6055282 B2 JPS6055282 B2 JP S6055282B2 JP 52054577 A JP52054577 A JP 52054577A JP 5457777 A JP5457777 A JP 5457777A JP S6055282 B2 JPS6055282 B2 JP S6055282B2
Authority
JP
Japan
Prior art keywords
discharge
seal packing
amount
air cleaner
dispensing
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
Application number
JP52054577A
Other languages
Japanese (ja)
Other versions
JPS53139673A (en
Inventor
一弘 宮本
隆 山岸
茂樹 山下
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TSUCHA SEISAKUSHO KK
Original Assignee
TSUCHA SEISAKUSHO KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by TSUCHA SEISAKUSHO KK filed Critical TSUCHA SEISAKUSHO KK
Priority to JP52054577A priority Critical patent/JPS6055282B2/en
Publication of JPS53139673A publication Critical patent/JPS53139673A/en
Publication of JPS6055282B2 publication Critical patent/JPS6055282B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、内燃機関用に用いられるエアクリーナカバの
シールパッキンの製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a seal packing for an air cleaner cover used for an internal combustion engine.

本発明の対象とするエアクリーナは、円筒ボディおよび
皿状カバで形成したハウジング内に、フィルタエレメン
トを配設し、前記ボディとカバとの間に環状シールパッ
キンを装着した構成のものである。この環状シールパッ
キンは、実公昭51一15855公報に示されたように
、皿状カバの外周に形成した環状溝内に発泡性の樹脂た
とえばポリウレタンフォーム原料を環状溝上を移動し、
一回転するノズルあるいは回転するカバの環状溝上に配
置したノズルから吐出させ、そしてこれを発泡させてカ
バ外周に形成される。この方法においては、たとえば環
状溝上を一回転するノズルからカバの環状溝内に吐出さ
せた樹脂が第1図に示すように、その吐出始点と吐出終
点で重なり合い、高さの不整いを生起させたりあるいは
不連続になつたり、この結果、シールパッキンとしての
シール特性を損なうといつた欠点を有していた。
The air cleaner to which the present invention is directed has a structure in which a filter element is disposed within a housing formed of a cylindrical body and a dish-shaped cover, and an annular seal packing is installed between the body and the cover. As shown in Japanese Utility Model Publication No. 51-15855, this annular seal packing is made by moving a foamable resin, such as a polyurethane foam raw material, into an annular groove formed on the outer periphery of a dish-shaped cover over the annular groove.
It is discharged from a nozzle that rotates once or from a nozzle placed on the annular groove of the rotating cover, and is foamed to form on the outer periphery of the cover. In this method, for example, resin discharged into the annular groove of the cover from a nozzle that rotates once on the annular groove overlaps at its discharge start point and discharge end point, causing height irregularities, as shown in Figure 1. This has the drawback that the sealing properties of the sealing packing are impaired as the sealing properties of the sealing packing are impaired.

なお、吐出する樹脂が低粘度でかつ反応が緩慢なものの
場合には、吐出後所定時間放置しておけば液面が平担化
し、このような欠点は生じないのであるが、反面、量産
性が悪化することになる。量産性を高めるためには、高
粘度でかつ反応性に富む発泡性樹脂を用いる必要がある
ので、上記欠点は、この場合、残存することになる。し
たがつて、本発明は、ノズルから樹脂を吐出・させて形
成する環状シールパッキンの製造方法において、発泡性
樹脂混合液の吐出始時に吐出量を連続的に増加させ、そ
の後所定の一定量とし、吐出終時に吐出量を連続的に減
少させ、吐出始時における吐出量と吐出終時における吐
出量との和をフ前記一定量とすることにより、均一高さ
に発泡性樹脂混合液を吐出できるようにしシール性の低
下しないエアクリーナカバシールパツキンの製法を提供
させたものである。
Note that if the resin to be discharged has a low viscosity and a slow reaction, if the resin is left to stand for a certain period of time after discharge, the liquid level will flatten and this problem will not occur. will get worse. In order to increase mass productivity, it is necessary to use a foamable resin with high viscosity and high reactivity, so the above drawbacks will remain in this case. Therefore, the present invention provides a method for manufacturing an annular seal packing formed by discharging resin from a nozzle, in which the discharge amount is continuously increased at the start of discharging the foamable resin mixture, and then the discharge amount is maintained at a predetermined constant amount. The foamable resin mixture is discharged to a uniform height by continuously decreasing the discharge amount at the end of the discharge and setting the sum of the discharge amount at the beginning of the discharge and the discharge amount at the end of the discharge to the above-mentioned constant amount. To provide a method for manufacturing an air cleaner cover seal packing that does not reduce sealing performance.

実施例により説明すると、まず、第2図におい5て1は
本発明によるシールパッキンの製造方法に用いられる形
成装置であり、2は、外周に環状溝4を有するエアクリ
ーナの皿状カバ、そして3は該カバを回転させる回転台
である。
To explain by way of an example, first, in FIG. 2, 5 and 1 are a forming device used in the seal packing manufacturing method according to the present invention, 2 is a dish-shaped cover of an air cleaner having an annular groove 4 on the outer periphery, and 3 is a forming device used in the seal packing manufacturing method according to the present invention. is a rotating table for rotating the cover.

形成装置1は、発泡樹脂の原料A,Bを内蔵するタンク
5,6を有し、これらがそれぞれポンプ7,8を介して
導管9,10,11,12により吐出制御装置13に接
続されている。同時に、吐出制御装置13には、導管1
4により溶剤タンク33が連結される。吐出制御装置1
3は、後述するように、タンク内の原料AとBを十分に
混合させる働きをなすとともに、これを所定量かつ適正
に制御する作用を兼備した機能を有する。皿状カバ2は
、その外周に、原料が混合吐出されシールパッキンが形
成される環状溝4を有している。
The forming device 1 has tanks 5 and 6 containing foamed resin raw materials A and B, which are connected to a discharge control device 13 by conduits 9, 10, 11, and 12 via pumps 7 and 8, respectively. There is. At the same time, the discharge control device 13 has a conduit 1
4 connects the solvent tank 33. Discharge control device 1
3 has the function of sufficiently mixing the raw materials A and B in the tank, and also controlling the mixture in a predetermined amount and appropriately, as will be described later. The dish-shaped cover 2 has an annular groove 4 on its outer periphery, in which raw materials are mixed and discharged to form a seal packing.

また、回転台3は、モータ等の回転駆動部34を有し、
この上に配置した前記カバを回転させるためのものであ
る。吐出制御装置13および回転台3は、作動制御装置
(図示せず)によつて、前記カバがはぼ一回転する間に
、前記装置13のプランジア31,32が上動→下動の
1サイクルし、ノズル40から発泡性樹脂混合液力幼パ
2の環状溝4内の一個所からほぼ3600にわたり供給
されるように制御されている。
Further, the rotary table 3 has a rotation drive unit 34 such as a motor,
This is for rotating the cover placed thereon. The discharge control device 13 and the rotary table 3 are controlled by an operation control device (not shown) to cause the plungers 31 and 32 of the device 13 to move up and down for one cycle while the cover rotates approximately once. The foaming resin mixture is controlled to be supplied from the nozzle 40 to one location in the annular groove 4 of the foamable resin mixture liquid powder 2 over approximately 3600 mm.

次に、上記吐出装置13について、その構造を説明する
Next, the structure of the discharge device 13 will be explained.

第3図、第4図、第5図において、15はボディであつ
て、ぞの中心部を貫通する中芯孔16を有し、さらにこ
の周囲に第1環状室17およびこれに連らなる、より小
径の第2環状室18,19が設けられている。また、ボ
ディ15外周には、前記環状室17に連通する空気流通
口260,21、そして前記環状室18,19におのお
の連通する原料流通口22,23,24,25があり、
底部にも環状室18,19と連絡する流通路26,27
がある。中芯孔16内には、一端にインペラ28を、他
端にプーリ30を固着した口!ツド29が挿設される。
プーリ30は、ベルトを介して駆動源へ連絡される(図
示せず)。第2環状室18,19内には、プランジア3
1,32が摺動自在に配置されている。プランジア31
,32は、それぞれ同形で、下端部はバルブを形成1し
、上端は第1環状室17内に挿設されたディスク35と
連結している。また、プランジアの中間部は、円周にそ
つて切削られた切欠き部36を形成し、第2環状室内壁
との間で空間を造りこれが流路をなす。原料連通口23
,25より下方のプランジア下端部は、逆さい頭円錐形
のバルブ体になつていて、その外周と第2環状室内壁と
て断面形状が三角形の密封空間37を形成している。プ
ランジアの下端がボディ15の第2環状室底部に装置し
ている状態では、原料流通口23と流通路16間、そし
て原料流通口25と流通路27間はいずれも連通しない
。ディスク35は、第1環状室17内に配置され、空気
流通口20,21間を)上下に摺動する。以上のように
構成されたボディ15の上方部には、蓋体38が取付け
られ、さらに下方部にはインペラハウジング39が固定
され、同時に該ハウジング39の先端にノズル40が装
着されて吐出・制御装置13が形成される。
In FIGS. 3, 4, and 5, 15 is a body, which has a central hole 16 passing through the center of the body, and a first annular chamber 17 and a first annular chamber 17 connected thereto around the central hole 16. , second annular chambers 18, 19 of smaller diameter are provided. Further, on the outer periphery of the body 15, there are air flow ports 260, 21 communicating with the annular chamber 17, and raw material flow ports 22, 23, 24, 25 communicating with the annular chambers 18, 19, respectively,
There are also flow passages 26 and 27 at the bottom that communicate with the annular chambers 18 and 19.
There is. Inside the core hole 16 is a port with an impeller 28 fixed to one end and a pulley 30 fixed to the other end! A tube 29 is inserted.
Pulley 30 is connected to a drive source via a belt (not shown). Inside the second annular chambers 18 and 19, a plunger 3 is provided.
1 and 32 are slidably arranged. Plungia 31
, 32 are each of the same shape, with a lower end forming a valve 1 and an upper end connected to a disk 35 inserted into the first annular chamber 17. Moreover, the middle part of the plunger forms a notch part 36 cut along the circumference, and creates a space between it and the second annular indoor wall, which forms a flow path. Raw material communication port 23
, 25 is an inverted truncated conical valve body, and its outer periphery and the second annular interior wall form a sealed space 37 having a triangular cross-section. When the lower end of the plunger is installed at the bottom of the second annular chamber of the body 15, there is no communication between the raw material flow port 23 and the flow path 16, and between the raw material flow port 25 and the flow path 27. The disk 35 is arranged within the first annular chamber 17 and slides up and down (between the air flow openings 20, 21). A lid 38 is attached to the upper part of the body 15 configured as described above, and an impeller housing 39 is fixed to the lower part.At the same time, a nozzle 40 is attached to the tip of the housing 39 for discharge and control. A device 13 is formed.

吐出制御装置13は、原料流通口22,23に導管9,
10が、また原料流通口24,25に導管11,12が
それぞれ連結され、空気流通口20,21には圧縮空気
供給管41,42が接続されて使用に供され”る。なお
、圧縮空気供給管41,42は、流量調節弁43,44
および電磁弁45を介して圧縮空気供給源(図示せず)
に至る。
The discharge control device 13 connects the raw material flow ports 22 and 23 with conduits 9,
10, conduit pipes 11 and 12 are connected to the raw material distribution ports 24 and 25, respectively, and compressed air supply pipes 41 and 42 are connected to the air distribution ports 20 and 21 for use. The supply pipes 41 and 42 have flow rate control valves 43 and 44.
and a compressed air supply (not shown) via a solenoid valve 45
leading to.

電磁弁45は、タイマ46により制御され空気流路を反
転させる。2液タイプ発泡ポリウレタン樹脂を用いたエ
アクリーナカバへのシールパッキンの製法は次の通りで
ある。
The solenoid valve 45 is controlled by a timer 46 to reverse the air flow path. The method for manufacturing a seal packing for an air cleaner cover using a two-component foamed polyurethane resin is as follows.

ポンプ7を始動させると、ポリウレタン樹脂の原料成分
である液状原料Aは、タンク5から導管9を通つて吐出
制御装置13の原料流通口23へ至り、ここからプラン
ジア31の切欠き部36と第2環状室内壁との間に形成
された流路を経て流通口22からタンク5内に回流する
。同様にして、原料Bもポンプ8を始動とともに回流す
る。電磁弁45を操作して圧縮空気供給源から圧縮空気
を導管42を通して空気流通口21に流入させると、流
体圧が第1環状室17内に配置したディスク35下面に
作用してこれを上昇させ、同時にディスク35に連結し
たプランジア31,32をも上昇させる。これにともな
い、第2環状室底部に接置していたプランジア下端は、
前記底部を離れ、原料流通口23と流通路26、および
原料流通口25と流通路27とを連通させ、原料A,B
は、ハウジング39内に送付される。所定時間経過する
と、タイマ46か電磁弁45を作動させて圧縮空気の流
れを反転させる。これによつて、圧縮空気は空気流通口
20から流入し、これがディスク35上面に作用してデ
ィスク35したがつてこれに連結しているプランジア3
1,32を下降させて流通路26,27を閉塞させ、ハ
ウジング39内への、原料A,Bの供給を止める。ハウ
ジング39内の原料A,Bは、回転しているインペラ2
8によつて十分に混合されて発泡性樹脂混合液を形成し
、ノズル40からエアクリーナカバ2に設けた環状溝4
内に吐出される。エアクリーナカバ2は、回転台3上に
水平に配置され、前記混合液の吐出時間に応じほぼ36
0置回転する。混合液の吐出は、第6図のように、プラ
ンジア32が上昇してその下端がa点を越えるにつれ開
口断面積は連続的に増加し、これに応じた量となり、プ
ランジア32下端位置がc点を越えると一定量となる。
When the pump 7 is started, the liquid raw material A, which is a raw material component of the polyurethane resin, flows from the tank 5 through the conduit 9 to the raw material distribution port 23 of the discharge control device 13, and from there flows through the notch 36 of the plunger 31 and the It circulates into the tank 5 from the flow port 22 through a flow path formed between the two annular interior walls. Similarly, raw material B is also circulated through the pump 8 upon startup. When the solenoid valve 45 is operated to cause compressed air to flow from the compressed air supply source through the conduit 42 and into the air flow port 21, fluid pressure acts on the lower surface of the disk 35 disposed in the first annular chamber 17 and raises it. At the same time, the plungers 31 and 32 connected to the disk 35 are also raised. Along with this, the lower end of the plunger, which was in contact with the bottom of the second annular chamber,
Leaving the bottom part, the raw material distribution port 23 and the flow path 26, and the raw material distribution port 25 and the flow path 27 are communicated with each other, and the raw materials A and B are connected to each other.
is sent into the housing 39. When a predetermined period of time has elapsed, the timer 46 or the solenoid valve 45 is operated to reverse the flow of compressed air. As a result, compressed air flows in from the air flow opening 20 and acts on the upper surface of the disk 35, thereby causing the plunger 3 connected thereto to act on the upper surface of the disk 35.
1 and 32 are lowered to close the flow passages 26 and 27, and the supply of raw materials A and B into the housing 39 is stopped. The raw materials A and B in the housing 39 are transported by the rotating impeller 2.
8 to form a foamable resin mixture, and the mixture is thoroughly mixed by the nozzle 40 to the annular groove 4 provided in the air cleaner cover 2.
discharged inside. The air cleaner cover 2 is arranged horizontally on the rotary table 3, and the air cleaner cover 2 is arranged horizontally on the rotary table 3, and the air cleaner cover 2 is arranged horizontally on the rotary table 3.
Rotate to 0 position. As shown in FIG. 6, as the plunger 32 rises and its lower end exceeds point a, the opening cross-sectional area increases continuously, and the amount of discharge of the mixed liquid increases accordingly, so that the lower end position of the plunger 32 reaches c Once the point is exceeded, it becomes a constant amount.

逆に、プランジア32の下降にともない開口断面積は、
連続的に減少しこれに応じた吐出量となり、プランジア
32が前記底部に接置するに至つて流路は完全に遮断さ
れる。また、プランジア32下端が位置a−b間にある
場合には、原料の一部はバイパスしてタンク内へ戻され
、ハウジング39内へ送付される量は、プランジア32
の上昇、下降に応じて、その分だけ増減することになる
。この結果、発泡性樹脂混合液の吐出始時すなわち、第
6図において、上昇するプランジア32下端がaに位置
するときから、それがbに至るまでの間には、吐出量が
連続的に増加し、c以降は一定量となり、また吐出終時
すなわち下降するプランジア32の下端がcに位置する
ときから、それがa以降に至るまでの間には、吐出量が
連続的に減少することになる。したがつて、発泡性樹脂
混合液の上記吐出始時および吐出終時において吐出され
る量は、プランジア32の下端がc以上にある場合に吐
出される量とほぼ等しい値となり、吐出混合液の高さは
均一化する(第7図)。したがつて、プランジア31,
32が1サイクル(上昇一下降)する間に前記回転台3
は、ほぼ360昇つまり360間よりわずかに大きい値
だけ回転することになる。この値は、吐出速度あるいは
回転台3の回転速度に応じ適宜、最適に定められる。エ
アクリーナカバの環状溝4内の発泡性樹脂混合液は、そ
のままの状態で放置すると、化学反応により発泡し、弾
性に富むシールパッキンを形成する。
Conversely, as the plunger 32 descends, the opening cross-sectional area becomes
The discharge amount decreases continuously, and the flow path is completely blocked when the plunger 32 comes into contact with the bottom. Further, when the lower end of the plunger 32 is between positions a and b, a part of the raw material is bypassed and returned into the tank, and the amount sent into the housing 39 is
It will increase or decrease according to the rise or fall of . As a result, from the start of discharging the foamable resin mixture, that is, from when the lower end of the rising plunger 32 is located at point a in FIG. 6 until it reaches point b, the discharge amount increases continuously. However, after c, the amount is constant, and from the end of the discharge, that is, when the lower end of the descending plunger 32 is located at c, until it reaches after a, the discharge amount decreases continuously. Become. Therefore, the amount of the foamable resin mixture to be discharged at the start and end of the discharge is approximately equal to the amount to be discharged when the lower end of the plunger 32 is above c, The height becomes uniform (Figure 7). Therefore, Plungia 31,
32 during one cycle (ascent and descent), the rotating table 3
will be rotated by approximately 360 degrees or slightly more than 360 degrees. This value is optimally determined depending on the discharge speed or the rotational speed of the rotary table 3. If the foamable resin mixture in the annular groove 4 of the air cleaner cover is left as it is, it will foam due to a chemical reaction and form a highly elastic seal packing.

その後、必要に応じ、加熱しシールパッキンをキユアす
る。以上のように本発明は、発泡性樹脂混合液をノズル
からカバの環状溝内に吐出させる工程において、吐出始
時および吐出終時に吐出量を各々連続的に増減させ、吐
出始時における吐出量と吐出終時における吐出量との和
を、吐出始時と吐出終時との間に吐出される吐出量と同
量値としたものであるから、カバの環状溝内の全区間で
発泡性樹脂混合液が均一高さとなり、シール特性の優れ
たエアクリーナカバシールパツキンを提供する。
Then, if necessary, heat the seal packing to cure it. As described above, in the process of discharging the foamable resin mixture from the nozzle into the annular groove of the cover, the discharge amount is continuously increased and decreased at the start and end of the discharge, and the discharge amount at the beginning of the discharge is Since the sum of the sum of the discharge amount and the discharge amount at the end of discharge is the same value as the discharge amount discharged between the start of discharge and the end of discharge, foaming is achieved in the entire area within the annular groove of the cover. To provide an air cleaner cover seal packing with a resin mixture having a uniform height and excellent sealing properties.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、従来製法により形成されたシールパッキンの
一部断面図、第2図は本発明の製法を説明するための装
置図、第3図は本発明による製法に用いられる吐出制御
装置断面図、第4図、第5図は、第3図におけるC−C
断面図およびD−D断面図、第6図は第3図の一部拡大
図そして第7図は本発明により得られるシールパッキン
の一部断面図、をおのおの示す。 13・・・・・・吐出制御装置、22,23,24,2
5・・・・・・原料流通口、15・・・・・・ボディ、
26,27・・・・・・流通路、17・・・・・・第1
環状室、31,32・・・・・・プランジア、18,1
9・・・・・・第2環状室、355・・・・・・ディス
ク、20,21・・・・・・空気流通口、38・・・・
・・蓋体。
FIG. 1 is a partial cross-sectional view of a seal packing formed by a conventional manufacturing method, FIG. 2 is a diagram of an apparatus for explaining the manufacturing method of the present invention, and FIG. 3 is a cross-sectional view of a discharge control device used in the manufacturing method of the present invention. Figures 4 and 5 are C-C in Figure 3.
6 is a partially enlarged view of FIG. 3, and FIG. 7 is a partially sectional view of the seal packing obtained according to the present invention. 13... Discharge control device, 22, 23, 24, 2
5... Raw material distribution port, 15... Body,
26, 27... Distribution path, 17... First
Annular chamber, 31, 32... Plunger, 18, 1
9...Second annular chamber, 355...Disk, 20, 21...Air circulation port, 38...
...Lid body.

Claims (1)

【特許請求の範囲】[Claims] 1 外周に環状溝を設けた皿状カバの環状溝内の一個所
から順次発泡性樹脂混合液を吐出し、これを発泡させて
弾性のシールパッキンを形成させるエアクリーナカバシ
ールパツキンの製造方法において、発泡性樹脂混合液の
吐出始時に吐出量を連続的に増加させ、その後所定の一
定量とし、吐出終時に吐出量を連続的に減少させ吐出始
時における吐出量と吐出終時における吐出量との和を前
記一定量とした吐出工程を特徴とするエアクリーナカバ
シールパツキンの製造方法。
1. A method for manufacturing an air cleaner cover seal packing, in which a foamable resin mixture is sequentially discharged from one location in the annular groove of a dish-shaped cover provided with an annular groove on the outer periphery, and the mixture is foamed to form an elastic seal packing, The discharge amount of the foamable resin mixture is continuously increased at the beginning of dispensing, then maintained at a predetermined constant amount, and the discharge amount is continuously decreased at the end of dispensing, so that the dispensing amount at the beginning of dispensing and the dispensing amount at the end of dispensing are changed. A method for manufacturing an air cleaner cover seal packing, characterized by a discharge step in which the sum of the above is set to the fixed amount.
JP52054577A 1977-05-11 1977-05-11 Method for manufacturing air cleaner cover seal packing Expired JPS6055282B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52054577A JPS6055282B2 (en) 1977-05-11 1977-05-11 Method for manufacturing air cleaner cover seal packing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52054577A JPS6055282B2 (en) 1977-05-11 1977-05-11 Method for manufacturing air cleaner cover seal packing

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP59062002A Division JPS6034816A (en) 1984-03-29 1984-03-29 Control device for ejecting mixed liquid for molding annular seal packing

Publications (2)

Publication Number Publication Date
JPS53139673A JPS53139673A (en) 1978-12-06
JPS6055282B2 true JPS6055282B2 (en) 1985-12-04

Family

ID=12974545

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52054577A Expired JPS6055282B2 (en) 1977-05-11 1977-05-11 Method for manufacturing air cleaner cover seal packing

Country Status (1)

Country Link
JP (1) JPS6055282B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6270532B2 (en) * 2014-02-24 2018-01-31 Towa株式会社 Resin molding apparatus and resin molding method

Also Published As

Publication number Publication date
JPS53139673A (en) 1978-12-06

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