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JP3354913B2 - Method and apparatus for dehumidifying and drying synthetic resin particles - Google Patents
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JP3354913B2 - Method and apparatus for dehumidifying and drying synthetic resin particles - Google Patents

Method and apparatus for dehumidifying and drying synthetic resin particles

Info

Publication number
JP3354913B2
JP3354913B2 JP36728899A JP36728899A JP3354913B2 JP 3354913 B2 JP3354913 B2 JP 3354913B2 JP 36728899 A JP36728899 A JP 36728899A JP 36728899 A JP36728899 A JP 36728899A JP 3354913 B2 JP3354913 B2 JP 3354913B2
Authority
JP
Japan
Prior art keywords
synthetic resin
main body
drying
drying device
device main
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 - Lifetime
Application number
JP36728899A
Other languages
Japanese (ja)
Other versions
JP2000167831A (en
Inventor
典次 関戸
裕國 山田
良啓 大沼
浩 今井
智 高木
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.)
GOYO CO., LTD.
Takagi Industrial Co Ltd
Original Assignee
GOYO CO., LTD.
Takagi Industrial Co Ltd
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
Priority claimed from JP19897991A external-priority patent/JP3233419B2/en
Application filed by GOYO CO., LTD., Takagi Industrial Co Ltd filed Critical GOYO CO., LTD.
Priority to JP36728899A priority Critical patent/JP3354913B2/en
Publication of JP2000167831A publication Critical patent/JP2000167831A/en
Application granted granted Critical
Publication of JP3354913B2 publication Critical patent/JP3354913B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、合成樹脂成形機に
供給すべき合成樹脂粉粒体の除湿乾燥方法及びその装置
に関する。
The present invention relates to a method and an apparatus for dehumidifying and drying synthetic resin particles to be supplied to a synthetic resin molding machine.

【0002】[0002]

【従来の技術】合成樹脂成形に用いる原材料には吸湿し
易いものがあり、水分は成形に悪影響を及ぼし、製品の
品質を低下させる。一般に、材料の乾燥には、熱によっ
て水分の蒸発を促し、その水蒸気を吸着剤等により排出
処理する方法がある。また、乾燥処理にマイクロ波を用
いるものがある。また、水分の蒸発を促進させる方法と
して、真空を使用するものもある。
2. Description of the Related Art Some raw materials used in synthetic resin molding tend to absorb moisture, and moisture has an adverse effect on molding and lowers product quality. In general, there is a method of drying a material in which heat is used to promote evaporation of water and the water vapor is discharged using an adsorbent or the like. In some cases, microwaves are used for drying. There is also a method of using a vacuum as a method of promoting the evaporation of water.

【0003】[0003]

【発明が解決しようとする課題】従来の熱循環方式で
は、外部からの空気を熱風に変換するため、効率が悪
く、乾燥に長時間を要するとともに、熱風に晒された合
成樹脂粉粒体を劣化させるおそれがあり、運転経費、設
備規模等に問題がある。また、マイクロ波方式において
も、同様に改善すべき不都合がある。
In the conventional heat circulation system, since the air from the outside is converted into hot air, the efficiency is low, the drying takes a long time, and the synthetic resin powder particles exposed to the hot air are removed. There is a risk of deterioration, and there are problems in operating costs, equipment scale, and the like. In the microwave system, there is also a disadvantage to be improved.

【0004】また、真空乾燥は、高真空度を実現する場
合、真空ポンプが大きくなる等の問題があり、従来、実
用性に乏しいとされてきた。
[0004] In addition, vacuum drying has a problem in that a large vacuum pump is required when a high degree of vacuum is realized, and it has heretofore been regarded as poor in practical use.

【0005】そこで、本発明は、真空処理と加熱処理と
の併用により、除湿乾燥の高効率化を実現した合成樹脂
粉粒体の除湿乾燥方法及びその装置を提供することを目
的とする。
Accordingly, an object of the present invention is to provide a method and an apparatus for dehumidifying and drying synthetic resin powder and granules which realize high efficiency of dehumidifying and drying by using both vacuum treatment and heat treatment.

【0006】[0006]

【課題を解決するための手段】本発明は、合成樹脂成形
機に供給される合成樹脂粉粒体の除湿乾燥方法及びその
装置であって、合成樹脂粉粒体の除湿乾燥後、乾燥装置
本体(真空除湿乾燥装置本体7)の真空を解除して合成
樹脂粉粒体の所定量を排出し、乾燥装置本体に除湿乾燥
前の合成樹脂粉粒体の所定量を補給し、加熱及び真空処
理を行って合成樹脂粉粒体の除湿乾燥を繰り返すことに
より、合成樹脂粉粒体の除湿乾燥の高効率化を実現して
いる。
SUMMARY OF THE INVENTION The present invention relates to a method and an apparatus for dehumidifying and drying synthetic resin particles supplied to a synthetic resin molding machine. The vacuum of the (vacuum dehumidifying / drying device main body 7) is released to discharge a predetermined amount of the synthetic resin powder, and a predetermined amount of the synthetic resin powder before dehumidifying and drying is supplied to the drying device, and heating and vacuum treatment are performed. By repeating the dehumidification and drying of the synthetic resin particles, the efficiency of the dehumidification and drying of the synthetic resin particles is improved.

【0007】請求項1に係る本発明は、合成樹脂成形機
に供給される合成樹脂粉粒体を真空下で加熱して除湿乾
燥させる、合成樹脂粉粒体の除湿乾燥方法であって、合
成樹脂粉粒体の除湿乾燥の後、乾燥装置本体(真空除湿
乾燥装置本体7)の真空を解除する工程と、前記乾燥装
置本体から除湿乾燥を施した前記合成樹脂粉粒体の所定
量を排出する工程と、前記乾燥装置本体に除湿乾燥前の
前記合成樹脂粉粒体の所定量を補給する工程と、前記乾
燥装置本体を閉鎖して前記合成樹脂粉粒体を加熱する工
程と、前記加熱中、前記乾燥装置本体内から空気を排出
させて前記乾燥装置本体内を真空状態に維持するととも
に、適当量の空気を前記乾燥装置本体内に導入させ、前
記合成樹脂粉粒体の加熱により発生した蒸気を前記空気
とともに外部へ排出させる工程と、除湿乾燥の後、前記
乾燥装置本体の排出口から排出させた前記合成樹脂粉粒
体を一時的に貯蔵手段に貯蔵させる工程と、前記貯蔵手
段に前記合成樹脂粉粒体が満たされたことを検出して前
記乾燥装置本体の前記排出口を閉じるとともに、前記乾
燥装置本体に所定量の前記合成樹脂粉粒体を搬送する工
程と、前記貯蔵手段から前記合成樹脂粉粒体を前記合成
樹脂成形機に供給する工程とを備えたことを特徴とす
る。即ち、合成樹脂粉粒体の除湿乾燥の後、乾燥装置本
体の真空状態を解除することにより、合成樹脂粉粒体の
排出が可能となる。除湿乾燥を施した合成樹脂粉粒体の
所定量を乾燥装置本体から排出し、その排出分に対応し
て除湿乾燥前の合成樹脂粉粒体の所定量を補給し、乾燥
装置本体を閉鎖して加熱処理を行うとともに、加熱中、
乾燥装置本体内から空気を排出させて乾燥装置本体内を
真空状態に維持する。加熱中、乾燥装置本体を真空化す
ると、乾燥装置本体内の水分の蒸発が促進されるととも
に、真空処理により蒸気が外気に放出される。即ち、真
空処理と加熱処理との併用で短時間で効率の良い除湿乾
燥が実現できるとともに、乾燥装置本体から排出させた
合成樹脂粉粒体を一時的に貯蔵手段に貯蔵させて待機し
ているので、合成樹脂成形機側の要求に即座に応ずるこ
とができ、合成樹脂成形機に合成樹脂粉粒体の連続的供
給が可能である上、合成樹脂成形機に供給される合成樹
脂粉粒体の品質を高めることができる。また、貯蔵手段
に合成樹脂粉粒体が満たされたことを検出して乾燥装置
本体の排出口を閉じ、乾燥装置本体に所定量の合成樹脂
粉粒体を供給するので、乾燥処理の迅速化を図ることが
できる。しかも、真空加熱処理では、適当量の空気を乾
燥装置本体内に導入し、合成樹脂粉粒体から発生する蒸
気を前記空気とともに乾燥装置本体外に排出させるの
で、水分流出が良好となり、合成樹脂粉粒体の乾燥効率
が高められる。
The present invention according to claim 1 is a method for dehumidifying and drying synthetic resin particles, wherein the synthetic resin particles supplied to the synthetic resin molding machine are heated and dried under vacuum. After dehumidifying and drying the resin particles, a step of releasing the vacuum of the drying device body (vacuum dehumidifying / drying device body 7), and discharging a predetermined amount of the dehumidified and dried synthetic resin powder particles from the drying device body. Performing a step of: supplying a predetermined amount of the synthetic resin particles before dehumidifying and drying to the drying device main body; closing the drying device main body to heat the synthetic resin particles; among, maintaining Then together the drying apparatus body in a vacuum state by discharging air from the drying apparatus body
Then, an appropriate amount of air was introduced into the drying device main body,
The steam generated by heating the synthetic resin powder is converted to the air
And a step of temporarily storing the synthetic resin particles discharged from the outlet of the drying device main body in a storage unit after dehumidifying and drying, and storing the synthetic resin powder in the storage unit. Detecting that the granules are filled, closing the discharge port of the drying device main body, and transporting a predetermined amount of the synthetic resin powder granules to the drying device main body; and And supplying a powder to the synthetic resin molding machine. That is, after the synthetic resin powder is dehumidified and dried, the vacuum state of the drying device body is released, so that the synthetic resin powder can be discharged. A predetermined amount of the synthetic resin particles subjected to the dehumidification and drying is discharged from the drying device main body, and a predetermined amount of the synthetic resin powder before the dehumidification and drying is replenished corresponding to the discharged amount, and the drying device main body is closed. Heat treatment, and during heating,
Air is discharged from the inside of the drying device main body to maintain the inside of the drying device main body in a vacuum state. When the drying device main body is evacuated during the heating, the evaporation of the water in the drying device main body is promoted, and the steam is released to the outside air by the vacuum processing. That is, efficient dehumidification and drying can be realized in a short time by the combined use of the vacuum treatment and the heat treatment, and the synthetic resin powder discharged from the drying device main body is temporarily stored in the storage means and is on standby. Therefore, it is possible to immediately respond to the demands of the synthetic resin molding machine side, and it is possible to continuously supply the synthetic resin granules to the synthetic resin molding machine, and further, the synthetic resin granules supplied to the synthetic resin molding machine. Quality can be improved. In addition, since it is detected that the storage means is filled with the synthetic resin particles, the outlet of the drying device main body is closed, and a predetermined amount of the synthetic resin particles is supplied to the drying device main body, so that the drying process is speeded up. Can be achieved. In addition, in the vacuum heat treatment, an appropriate amount of air is dried.
Introduced into the drying equipment main body and the steam generated from the synthetic resin powder
Of air to the outside of the drying device together with the air.
The water outflow is good, and the drying efficiency of the synthetic resin powder
Is enhanced.

【0008】請求項2に係る本発明は、合成樹脂成形機
に供給される合成樹脂粉粒体を真空下で加熱して除湿乾
燥させる、合成樹脂粉粒体の除湿乾燥装置であって、合
成樹脂粉粒体(原材料31)が供給される乾燥装置本体
(真空除湿乾燥装置本体7)と、この乾燥装置本体に前
記合成樹脂粉粒体を供給する樹脂供給手段(吸上げ機構
2)と、前記乾燥装置本体内の前記合成樹脂粉粒体を加
熱する加熱手段(熱交換器8、ヒートパイプ11)と、
前記合成樹脂粉粒体の加熱中、前記乾燥装置本体を空気
の排出により真空化する真空形成手段(真空ポンプ5)
と、前記乾燥装置本体の排出口を開閉する開閉手段(下
自動開閉バルブ22)と、この開閉手段により前記排出
口を閉じるとともに前記真空形成手段前記空気排出
時、前記乾燥装置本体内に適当量の空気を導入させる空
気導入手段と、前記乾燥装置本体から排出させた前記合
成樹脂粉粒体を前記合成樹脂成形機に供給する前に一時
的に貯蔵する貯蔵手段(貯蔵タンク12)と、この貯蔵
手段に前記合成樹脂粉粒体が満たされたことを検出して
前記開閉手段を作動させるとともに、前記樹脂供給手段
によって前記乾燥装置本体に所定量の前記合成樹脂粉粒
体を供給させる制御手段(本体スイッチ6、上限スイッ
チ13)とを備えたことを特徴とする。即ち、本発明
は、上記方法を装置として実現したものであり、所定量
の合成樹脂粉粒体を入れた乾燥装置本体には加熱手段が
設置されており、これによって合成樹脂粉粒体が加熱さ
れ、水分を蒸発させる。真空処理は、真空形成手段であ
る真空ポンプで行われ、合成樹脂粉粒体の加熱処理と乾
燥装置本体の真空処理との併用により、短時間で効率の
良い除湿乾燥が得られる。そして、乾燥装置本体からの
合成樹脂粉粒体の所定量の排出に伴い、その排出分に対
応した合成樹脂粉粒体を乾燥装置本体に補給して加熱処
理及び真空処理を行い、供給及び排出の繰り返しによ
り、短時間で効率の良い除湿乾燥が実現できるととも
に、乾燥装置本体から排出させた合成樹脂粉粒体を一時
的に貯蔵手段に貯蔵させて待機しているので、合成樹脂
成形機側の要求に即座に応ずることができ、合成樹脂成
形機に合成樹脂粉粒体の連続的供給が可能である上、合
成樹脂成形機に供給される合成樹脂粉粒体の品質を高め
ることができる。しかも、貯蔵手段に合成樹脂粉粒体が
満たされたことを検出して乾燥装置本体の排出口を閉
じ、乾燥装置本体に所定量の合成樹脂粉粒体を供給する
ので、乾燥処理の迅速化が図られる。この合成樹脂粉粒
体の除湿乾燥装置においても、真空加熱処理中に適当量
の空気を乾燥装置本体内に導入し、合成樹脂粉粒体から
発生する蒸気を前記空気とともに乾燥装置本体外に排出
させるので、水分流出が良好となり、合成樹脂粉粒体の
乾燥効率が高められる。
According to a second aspect of the present invention, there is provided an apparatus for dehumidifying and drying synthetic resin particles, wherein the synthetic resin particles supplied to the synthetic resin molding machine are heated and dried under vacuum. A drying device main body (vacuum dehumidifying / drying device main body 7) to which the resin powder (raw material 31) is supplied; a resin supply means (suction mechanism 2) for supplying the synthetic resin powder to the drying device main body; Heating means (heat exchanger 8, heat pipe 11) for heating the synthetic resin particles in the drying device main body;
Vacuum forming means (vacuum pump 5) for evacuating the drying device body by discharging air during heating of the synthetic resin particles.
When the drying device closing means for opening and closing the discharge port of the main body (lower automatic opening and closing valve 22), the discharge by the opening and closing means
Wherein when air discharge of the vacuum forming means closes the mouth, the drying device and an air introduction means for introducing a suitable amount of air into the body, the drying apparatus the synthetic resin the synthetic resin powder or granular material which is discharged from the main body A storage means (storage tank 12) for temporarily storing before supplying to the molding machine, and detecting that the synthetic resin powder is filled in the storage means
Control means (main body switch 6, upper limit switch 13) for operating the opening / closing means and supplying a predetermined amount of the synthetic resin powder to the drying device main body by the resin supply means. . That is, in the present invention, the above method is realized as an apparatus, and a heating unit is provided in a drying apparatus main body in which a predetermined amount of synthetic resin powder is put, whereby the synthetic resin powder is heated. And evaporate the water. The vacuum processing is performed by a vacuum pump as a vacuum forming means, and efficient dehumidification and drying can be obtained in a short time by using both the heat treatment of the synthetic resin particles and the vacuum treatment of the drying device body. Then, with the discharge of a predetermined amount of the synthetic resin particles from the main body of the drying apparatus, the synthetic resin particles corresponding to the discharge amount are supplied to the main body of the drying apparatus to perform a heating process and a vacuum process, and supply and discharge By repeating this process, efficient dehumidification and drying can be realized in a short time, and the synthetic resin powder discharged from the drying device main body is temporarily stored in the storage means and is on standby. Can immediately respond to the requirements of (1), and it is possible to continuously supply the synthetic resin particles to the synthetic resin molding machine, and to improve the quality of the synthetic resin particles supplied to the synthetic resin molding machine. . In addition, since it is detected that the storage means is filled with the synthetic resin particles, the discharge port of the drying device main body is closed, and a predetermined amount of the synthetic resin particles is supplied to the drying device main body, so that the drying process is speeded up. Is achieved. Also in this dehumidifying and drying apparatus for synthetic resin particles, an appropriate amount of air is introduced into the main body of the drying apparatus during the vacuum heating process, and steam generated from the synthetic resin particles is discharged to the outside of the main body of the drying apparatus together with the air. As a result, the outflow of water becomes good, and the drying efficiency of the synthetic resin particles is enhanced.

【0009】[0009]

【発明の実施の形態】図1ないし図4は本発明の合成樹
脂粉粒体の除湿乾燥方法及びその装置の実施の形態を示
し、図1は除湿乾燥装置の全体構成を略示した縦断面
図、図2は下自動開閉バルブが開いた状態を略示した断
面図、図3は下自動開閉バルブが閉じた状態を略示した
断面図、図4は貯蔵タンクを分離可能にした状態を略示
した断面図である。
1 to 4 show an embodiment of a method and an apparatus for dehumidifying and drying synthetic resin particles according to the present invention. FIG. 1 is a longitudinal sectional view schematically showing the entire structure of a dehumidifying and drying apparatus. Fig. 2 is a sectional view schematically showing a state in which the lower automatic opening and closing valve is open, Fig. 3 is a sectional view schematically showing a state in which the lower automatic opening and closing valve is closed, and Fig. 4 is a state in which the storage tank is separable. FIG. 2 is a schematic sectional view.

【0010】この除湿乾燥装置は、合成樹脂粉粒体であ
る原材料31を吸込み空気とともに吸い上げる吸い上げ
機構2と、原材料31と吸込み空気とを分離する空気分
離機構3とを有する供給受け口1が上自動開閉バルブ4
を介して連結した真空除湿乾燥装置本体7を設け、除湿
乾燥時における真空除湿乾燥装置本体7から外部への放
熱を極力抑えるため、真空除湿乾燥装置本体7に内壁9
を設け、外面部に襞が設けられたヒートパイプ11、
P.T.C内蔵襞付きパイプ10を備える熱交換器8を
設け、真空除湿乾燥装置本体7の底面側の排出口を開閉
する下自動開閉バルブ22を設け、その下側に除湿乾燥
された原材料31を蓄える貯蔵タンク12を設け、最下
端に設けられたフランジ14を合成樹脂成形機の原材料
受け口15に連結して原材料31を供給するようにした
ものである。即ち、この除湿乾燥装置において、真空除
湿乾燥装置本体7への所定量の原材料31の供給するた
めに設置された吸い上げ機構2、空気分離機構3、上自
動開閉バルブ4又は供給受け口1は真空除湿乾燥装置本
体7への原材料31の供給手段を構成し、空気分離機構
3は同時に搬送される原材料31及び吸込み空気から原
材料31の合成樹脂粉粒体を分離する分離手段を構成し
ている。また、熱交換器8及びヒートパイプ11は、原
材料31の加熱手段であり、熱交換器8は発熱手段、ヒ
ートパイプ11は放熱手段を構成している。そして、下
自動開閉バルブ22は真空除湿乾燥装置本体7の底面側
の原材料排出口とともに排出手段を構成している。
In this dehumidifying and drying apparatus, a supply port 1 having a suction mechanism 2 for sucking up a raw material 31, which is a synthetic resin powder, together with suction air, and an air separating mechanism 3 for separating the raw material 31 from the suction air, is automatically mounted. Open / close valve 4
The vacuum dehumidifying / drying device main body 7 is connected to the vacuum dehumidifying / drying device main body 7 in order to minimize heat radiation from the vacuum dehumidifying / drying device main body 7 to the outside during dehumidifying / drying.
And a heat pipe 11 provided with folds on its outer surface,
P. T. C. A heat exchanger 8 having a foldable pipe 10 with a built-in fold is provided, and a lower automatic opening / closing valve 22 for opening and closing a discharge port on the bottom side of the vacuum dehumidifying / drying apparatus main body 7 is provided. A storage tank 12 is provided, and a raw material 31 is supplied by connecting a flange 14 provided at the lowermost end to a raw material receiving port 15 of a synthetic resin molding machine. That is, in this dehumidifying / drying apparatus, the suction mechanism 2, the air separation mechanism 3, the upper automatic opening / closing valve 4, or the supply port 1 provided for supplying a predetermined amount of the raw material 31 to the vacuum dehumidifying / drying apparatus main body 7 are vacuum dehumidified. The raw material 31 is supplied to the main body 7 of the drying apparatus, and the air separating mechanism 3 is configured to separate the synthetic resin powder of the raw material 31 from the raw material 31 and the sucked air which are conveyed at the same time. The heat exchanger 8 and the heat pipe 11 are heating means for the raw material 31, the heat exchanger 8 is a heat generating means, and the heat pipe 11 is a heat radiating means. The lower automatic opening / closing valve 22 constitutes a discharging means together with a raw material discharging port on the bottom side of the vacuum dehumidifying / drying apparatus main body 7.

【0011】真空除湿乾燥装置本体7には、従来、加熱
装置として多用されてきたニクロム線の欠点である断線
のし易さ、設定温度保持のための自動温度調節器の必要
性、成形機の振動による故障等を補う加熱手段として、
P.T.Cセラミックス発熱体を内蔵し、かつ、外壁の
表面積を増大するために適当な位置に襞を設けたP.
T.C内蔵襞付きパイプ10を縦方向に数本適宜配置し
た物で構成された熱交換器8を設置している。従来、原
材料の種類毎に加熱設定温度を変える必要があると考え
られていたが、特定の温度と加熱時間によって、原材料
の種類毎に温度設定をする必要はない。
The vacuum dehumidifying / drying apparatus main body 7 has disadvantages of the nichrome wire, which has been frequently used as a heating device, such as the easiness of disconnection, the necessity of an automatic temperature controller for maintaining a set temperature, and the use of a molding machine. As a heating means to compensate for failures due to vibration,
P. T. The P.C. ceramic heating element is built in, and a fold is provided at an appropriate position to increase the surface area of the outer wall.
T. A heat exchanger 8 composed of a plurality of pipes 10 with built-in folds 10 arranged appropriately in the vertical direction is installed. Conventionally, it has been considered that it is necessary to change the heating set temperature for each type of raw material, but it is not necessary to set the temperature for each type of raw material according to a specific temperature and heating time.

【0012】P.T.C内蔵襞付きパイプ10の熱を更
に遠い位置まで早く伝えることが可能な熱伝導係数が大
きいヒートパイプ11を使用し、更に外壁の表面積を増
大するため、適当な位置に襞を設けた物で構成された熱
交換器8が使用されている。
P. T. C Use a heat pipe 11 having a large heat conduction coefficient capable of transmitting the heat of the pipe 10 with a built-in fold to a farther position quickly, and further providing a fold at an appropriate position to increase the surface area of the outer wall. The configured heat exchanger 8 is used.

【0013】原材料31へ熱を早く伝える手段として、
熱交換器8の外壁には遠赤外線を放射する塗料がコーテ
ィングされており、この塗料のコーティングによって熱
交換器8自体の放熱による熱の伝導及び対流に加え、遠
赤外線の放射を利用することができる。
As a means for quickly transferring heat to the raw material 31,
The outer wall of the heat exchanger 8 is coated with a paint that emits far-infrared rays, and the coating of the paint makes it possible to use far-infrared radiation in addition to heat conduction and convection due to heat radiation of the heat exchanger 8 itself. it can.

【0014】真空除湿乾燥装置本体7に設置した内壁9
は、その内壁9と真空除湿乾燥装置本体7との間に空間
を形成し、熱交換器8からの熱を真空除湿乾燥装置本体
7に閉じ込め、外部への放熱防止を図ることができる。
The inner wall 9 installed in the vacuum dehumidifying / drying device main body 7
Can form a space between the inner wall 9 and the vacuum dehumidifying / drying apparatus main body 7 to confine heat from the heat exchanger 8 to the vacuum dehumidifying / drying apparatus main body 7 to prevent heat radiation to the outside.

【0015】真空形成手段としての真空ポンプ5が設置
されており、この真空ポンプ5の使用により、真空除湿
乾燥装置本体7の下方より貯蔵タンク12内の高温乾燥
空気をバルブを通して吸引し、空気とともに水分を大気
中に放出する。即ち、バイパスと空気量を適宜調節でき
るバルブを通して適当量の空気を真空ポンプ5に吸引
し、所定の真空度を保持したまま吸引された高温乾燥空
気が真空除湿乾燥装置本体7内の下方より原材料31の
表面に触れながら、真空除湿乾燥装置本体7の上方より
真空ポンプ5を通して大気中に放出され、最大限の水分
放出が可能となっている。
A vacuum pump 5 as a vacuum forming means is provided. By using the vacuum pump 5, high-temperature dry air in the storage tank 12 is sucked from below the vacuum dehumidifying / drying apparatus main body 7 through a valve, and is together with the air. Releases moisture into the atmosphere. That is, an appropriate amount of air is sucked into the vacuum pump 5 through a bypass and a valve that can appropriately adjust the amount of air, and the high-temperature dry air sucked while maintaining a predetermined degree of vacuum is supplied to the raw material from below in the vacuum dehumidifying and drying apparatus main body 7. While touching the surface of 31, the vacuum dehumidifying / drying device is discharged into the atmosphere from above the main body 7 through the vacuum pump 5 so that the maximum water release is possible.

【0016】上自動開閉バルブ4及び排出手段としての
下自動開閉バルブ22は、除湿乾燥された原材料31を
合成樹脂成形機に自動供給する目的で設置されたもので
あり、真空除湿乾燥装置本体7に原材料31が滞留する
時間を一定にさせ、また、先入れ傘20及び先出し傘2
1は、真空除湿乾燥装置本体7に先入れされた原材料3
1を順序よく先出しするために設けられている。先入れ
傘20は原材料31を真空除湿乾燥装置本体7に乾燥後
のものの上に乾燥前のものが重なるように順序よく入れ
るための案内手段であり、先出し傘21は樹脂乾燥後の
原材料31を真空除湿乾燥装置本体7から乾燥したもの
を先に順序よく排出させるための案内手段を構成してい
る。
The upper automatic opening / closing valve 4 and the lower automatic opening / closing valve 22 as discharging means are provided for the purpose of automatically supplying the dehumidified and dried raw material 31 to the synthetic resin molding machine. The time during which the raw material 31 stays is constant, and the first umbrella 20 and the first umbrella 2
1 is a raw material 3 pre-loaded into a vacuum dehumidifying / drying device main body 7
It is provided to advance 1 in order. The first umbrella 20 is a guiding means for putting the raw material 31 into the vacuum dehumidifying / drying apparatus main body 7 in order so that the raw material 31 overlaps the one after the drying on the one after the drying, and the first umbrella 21 applies the vacuum to the raw material 31 after the resin is dried. The guide means for discharging the dried product from the dehumidifying / drying device main body 7 in order first.

【0017】除湿乾燥装置においては、所定の真空度を
保持することが必要であるが、下自動開閉バルブ22の
閉鎖作動時に原材料31の咬み込みがあると所定の真空
度を保持することができないので、仕切作動板24にて
先に原材料31を咬み込むことにより、真空除湿乾燥装
置本体7から貯蔵タンク12への原材料31の流れを止
め、その後、中板26にて完全にバルブを閉める機構を
併用し、下自動開閉バルブ22による密閉性を高めてい
る。
In the dehumidifying and drying apparatus, it is necessary to maintain a predetermined degree of vacuum. However, if the raw material 31 is bitten when the lower automatic opening / closing valve 22 is closed, the predetermined degree of vacuum cannot be maintained. Therefore, the raw material 31 is first bitten by the partitioning operation plate 24 to stop the flow of the raw material 31 from the vacuum dehumidifying / drying device main body 7 to the storage tank 12, and then the valve is completely closed by the middle plate 26. Are used together to enhance the tightness of the lower automatic opening / closing valve 22.

【0018】真空除湿乾燥装置本体7や貯蔵タンク12
の掃除の際に、上蓋16を真空除湿乾燥装置本体7より
分離させることにより真空除湿乾燥装置本体固定スプリ
ング32に加わる重量を減少させている。このため、下
蓋板27を上側に持ち上げることができ、貯蔵タンク1
2を容易に真空除湿乾燥装置本体7より分離することが
でき、真空除湿乾燥装置本体7や貯蔵タンク12の掃除
を容易に行うことができる。なお、17は表示手段とし
てのパトライト、19は真空圧力ゲージ、23は上蓋
板、25は仕切作動板スプリング、28は小Oリング、
29は大Oリング、30はエアーシリンダである。
The vacuum dehumidifying and drying apparatus main body 7 and the storage tank 12
During the cleaning, the upper lid 16 is separated from the vacuum dehumidifying / drying device main body 7 to reduce the weight applied to the vacuum dehumidifying / drying device main body fixing spring 32. For this reason, the lower lid plate 27 can be lifted upward, and the storage tank 1
2 can be easily separated from the vacuum dehumidifying / drying apparatus main body 7, and the vacuum dehumidifying / drying apparatus main body 7 and the storage tank 12 can be easily cleaned. In addition, 17 is a patrol light as a display means, 19 is a vacuum pressure gauge, 23 is an upper cover plate, 25 is a partition operating plate spring, 28 is a small O-ring,
29 is a large O-ring and 30 is an air cylinder.

【0019】次に、本発明の合成樹脂粉粒体の除湿乾燥
方法を説明する。
Next, the method for dehumidifying and drying the synthetic resin particles of the present invention will be described.

【0020】吸込み空気と共に送られる所定量の原材料
31が供給受け口1で吸込み空気と分離されて上自動開
閉バルブ4を通過後、真空除湿乾燥機本体7へと供給さ
れる。所定量の原材料31が真空除湿乾燥機本体7に入
れられると、上自動開閉バルブ4が閉まり、同時に熱交
換器8のP.T.C内蔵襞付きパイプ10に電圧が印加
される。表面積を大きくするために襞を設けたヒートパ
イプ11と、P.T.C内蔵襞付きパイプ10とで構成
された熱交換器8は、P.T.Cセラミックス発熱体の
特性として初期突入電流が大きく、理想的な定温発熱体
であって、電源投入後、数分間という極めて短時間で熱
的平衡状態に達し、その後はP.T.Cセラミックス発
熱体自体が自動的にそれ自体を流れる電流を調節する機
能を備えていることから、その周囲を一定温度で加熱し
続ける。そして、真空除湿乾燥装置本体7の本体スイッ
チ6によって制御された所定量の原材料31は、この熱
交換器8の熱伝導により速やかに一定温度に加熱され
る。この場合、熱交換器8にコーティングされた塗料が
発する遠赤外線の放射効果により熱交換器8自体の表面
温度は約1割程度推移するが、その温度差分の熱エネル
ギーが放射エネルギーになって合成樹脂粉粒体である原
材料31の各粉粒体の内部加熱を行うことができ、除湿
乾燥効率の向上が図られる。
A predetermined amount of raw material 31 sent together with the suction air is separated from the suction air at the supply port 1, passes through the upper automatic opening / closing valve 4, and is supplied to the vacuum dehumidifier / dryer body 7. When a predetermined amount of the raw material 31 is put into the vacuum dehumidifier / dryer main body 7, the upper automatic opening / closing valve 4 is closed, and at the same time, the P.V. T. A voltage is applied to the pipe 10 with a built-in fold C. A heat pipe 11 provided with folds to increase the surface area; T. C built-in pleated pipe 10 and heat exchanger 8 are P.C. T. As a characteristic of the C ceramic heating element, the initial inrush current is large, and it is an ideal constant temperature heating element. It reaches a thermal equilibrium state in a very short time of several minutes after the power is turned on. T. Since the C-ceramic heating element itself has a function of automatically adjusting the current flowing through itself, the surrounding area is continuously heated at a constant temperature. A predetermined amount of the raw material 31 controlled by the main body switch 6 of the vacuum dehumidifying / drying apparatus main body 7 is quickly heated to a constant temperature by the heat conduction of the heat exchanger 8. In this case, the surface temperature of the heat exchanger 8 itself changes by about 10% due to the radiation effect of the far-infrared ray emitted from the paint coated on the heat exchanger 8, but the heat energy of the temperature difference becomes radiant energy and is synthesized. The internal heating of each granular material of the raw material 31 that is the resin granular material can be performed, and the dehumidifying and drying efficiency can be improved.

【0021】このような加熱処理と並行して真空処理が
行われる。即ち、加熱中、真空ポンプ5の作用により、
下自動開閉バルブ22に装備したバイパス回路を通して
貯蔵タンク12内の高温乾燥空気を所定の真空度を保持
しながら真空除湿乾燥装置本体7内を連続的に通過させ
る。下方より上方へと空気が通過する際、真空除湿乾燥
装置本体7内の原材料31の表面に通過する空気が接触
して移動することから、その空気は原材料31の付着水
と触れて拡散する結合水を含んで徐々に湿潤化し、最大
飽和水蒸気量となって大気中に放出され、その結果、原
材料31の除湿乾燥が行われる。この間、合成樹脂成形
機は成形処理を行い原材料31を消費するが、その成形
中に原材料31が除湿乾燥される。
A vacuum process is performed in parallel with such a heating process. That is, during the heating, by the action of the vacuum pump 5,
The high temperature dry air in the storage tank 12 is continuously passed through the vacuum dehumidifying and drying apparatus main body 7 while maintaining a predetermined degree of vacuum through a bypass circuit provided in the lower automatic opening / closing valve 22. When air passes from below to above, the air passing through the surface of the raw material 31 in the vacuum dehumidifying / drying device main body 7 comes into contact and moves, so that the air comes into contact with the water adhering to the raw material 31 and is diffused. The water is gradually moistened to contain water, and is released to the atmosphere as a maximum saturated water vapor amount. As a result, the raw material 31 is dehumidified and dried. During this time, the synthetic resin molding machine performs the molding process and consumes the raw material 31, but the raw material 31 is dehumidified and dried during the molding.

【0022】電気制御部18に設置したタイマーの指示
により下自動開閉バルブ22が開き、除湿乾燥された原
材料31は真空除湿乾燥装置本体7から自然落下により
排出され、貯蔵タンク12側に供給される。貯蔵タンク
12が原材料31で満たされると、上限スイッチ13の
指示により二段締めの構造を有する下自動開閉バルブ2
2が原材料31を咬み込むことなく閉められる。このと
き、上自動開閉バルブ4が開かれ、供給受け口1の作動
により所定の原材料31が真空除湿乾燥装置本体7に供
給され、その供給量は本体スイッチ6により制御され
る。以上の制御を1つの制御サイクルとして実行し、除
湿乾燥の処理は短時間で行うことができるため、合成樹
脂成形機側の成形処理の原材料31の消費に比較して除
湿乾燥の処理量が多いので、除湿乾燥された原材料31
を合成樹脂成形機に連続的に供給することができる。
The lower automatic opening / closing valve 22 is opened by an instruction of a timer installed in the electric control unit 18, and the raw material 31 having been dehumidified and dried is discharged from the vacuum dehumidifying / drying apparatus main body 7 by natural fall and supplied to the storage tank 12 side. . When the storage tank 12 is filled with the raw material 31, the lower automatic opening / closing valve 2 having a two-stage tightening structure is instructed by the instruction of the upper limit switch 13.
2 is closed without biting the raw material 31. At this time, the upper automatic opening / closing valve 4 is opened, and a predetermined raw material 31 is supplied to the vacuum dehumidifying / drying apparatus main body 7 by the operation of the supply receiving port 1, and the supply amount is controlled by the main body switch 6. Since the above control is executed as one control cycle, and the dehumidifying and drying process can be performed in a short time, the amount of the dehumidifying and drying process is larger than the consumption of the raw material 31 in the molding process on the synthetic resin molding machine side. Therefore, the raw material 31 which has been dehumidified and dried
Can be continuously supplied to a synthetic resin molding machine.

【0023】このように真空加熱方式による合成樹脂粉
粒体の除湿乾燥装置は、下自動開閉バルブ22の使用に
よる原材料31の咬み込み防止、除湿乾燥の処理時間の
短縮、高効率化を図って、合成樹脂成形機に原材料31
の連続的な供給等、優れた特徴を有するものである。
As described above, the apparatus for dehumidifying and drying synthetic resin particles by the vacuum heating method is intended to prevent the raw material 31 from being bitten by using the lower automatic opening / closing valve 22, to shorten the processing time for dehumidifying and drying, and to increase the efficiency. Raw material 31 to synthetic resin molding machine
It has excellent features such as continuous supply of

【0024】除湿乾燥は、加熱処理に真空処理を併用し
たことにより、低温での水の沸騰現象を活用でき、原材
料31の表面に付着している付着水、原材料31内部に
ある結合水を気化蒸発させ、真空ポンプ5の吸引力によ
り強制的に原材料31と分離し、真空ポンプ5を介して
大気中に放出させることができる。この除湿効果を助長
するため、下自動開閉バルブ22に設けたバイパスより
連続的に貯蔵タンク12の高温乾燥空気を吸引し、真空
除湿乾燥装置本体7内に滞留している原材料31と接触
させて最大飽和水蒸気量を大気に放出される結果、気化
蒸発させた水分を短時間に排出でき、効率的な除湿乾燥
を行うことができる。その際、加熱された原材料31か
ら気化蒸発で奪われた熱量は、P.T.Cセラミックス
発熱体を用いて連続供給される。即ち、熱交換器8とし
てP.T.C内蔵襞付きパイプ10を用いて表面積を増
大し、更に遠い位置まで熱を早く伝えることが可能な襞
を設けたヒートパイプ11を設けているので、原材料3
1との接触面積を増加させて熱伝導率を高め、原材料3
1の急速に均一加熱を図ることができ、高効率の除湿乾
燥を実現している。更に、定温特性を有するP.T.C
セラミックス発熱体を用いた熱交換器8の表面には、真
空中においても性能を発揮する遠赤外線を放射する塗料
がコーティングされており、付着水、結合水の気化蒸発
を促進させることができると同時に、熱交換器8表面の
温度を低温化させることができ、低温化と加熱時間の短
縮化を図ることができ、加熱による原材料31の劣化防
止を図ることができる。
In the dehumidification drying, the boiling treatment of water at a low temperature can be utilized by using a vacuum treatment in combination with the heat treatment, and the attached water adhering to the surface of the raw material 31 and the bound water inside the raw material 31 are vaporized. It can be evaporated, forcibly separated from the raw material 31 by the suction force of the vacuum pump 5, and released into the atmosphere via the vacuum pump 5. In order to promote this dehumidifying effect, high-temperature dry air in the storage tank 12 is continuously sucked from the bypass provided in the lower automatic opening / closing valve 22 and brought into contact with the raw material 31 staying in the vacuum dehumidifying / drying apparatus main body 7. As a result of releasing the maximum amount of saturated water vapor to the atmosphere, the vaporized and evaporated water can be discharged in a short time, and efficient dehumidification and drying can be performed. At that time, the amount of heat deprived of the heated raw material 31 by vaporization and evaporation is P.P. T. It is continuously supplied using a C ceramic heating element. That is, as heat exchanger 8, P.I. T. C Since the heat pipe 11 provided with a fold capable of increasing the surface area using the built-in folded pipe 10 and transmitting heat quickly to a farther position is provided, the raw material 3
1 to increase the thermal conductivity by increasing the contact area with
1 enables rapid and uniform heating and achieves highly efficient dehumidification and drying. Furthermore, P.P. T. C
The surface of the heat exchanger 8 using the ceramic heating element is coated with a paint that emits far-infrared rays that exhibits performance even in a vacuum, and can promote the vaporization and evaporation of attached water and bound water. At the same time, the temperature of the surface of the heat exchanger 8 can be lowered, the temperature can be lowered and the heating time can be shortened, and the deterioration of the raw material 31 due to heating can be prevented.

【0025】更に、真空除湿乾燥装置本体7を二重構造
にしているので、熱交換器8の熱を真空除湿乾燥装置本
体7に閉じ込め、真空除湿乾燥装置本体7からの放熱を
極力抑えることができ、P.T.Cセラミックス発熱体
の熱を原材料31に効率よく伝達させ、熱効率を高める
ことができる。
Further, since the vacuum dehumidifying / drying apparatus main body 7 has a double structure, the heat of the heat exchanger 8 is confined in the vacuum dehumidifying / drying apparatus main body 7, and heat radiation from the vacuum dehumidifying / drying apparatus main body 7 can be suppressed as much as possible. Yes, P. T. The heat of the C ceramic heating element can be efficiently transmitted to the raw material 31, and the thermal efficiency can be increased.

【0026】また、原材料31の供給は、真空除湿乾燥
装置本体7の熱交換器8に除湿乾燥された原材料31の
先入れ先出しを可能にした原材料31の案内手段として
の先入れ傘20及び先出し傘21を設けたので、真空除
湿乾燥装置本体7に原材料31を乾燥前後の原材料31
が混じることなく供給できるとともに、除湿乾燥された
原材料31を順序よく、むらなく合成樹脂成形機に供給
できる。
The raw material 31 is supplied by a first-in umbrella 20 and a first-out umbrella 21 as guide means for the raw material 31 which enables the first-in first-out of the raw material 31 which has been dehumidified and dried in the heat exchanger 8 of the vacuum dehumidifying / drying apparatus main body 7. Is provided, the raw material 31 is placed in the vacuum dehumidifying and drying apparatus main body 7 before and after drying.
Can be supplied without being mixed, and the raw materials 31 that have been dehumidified and dried can be supplied to the synthetic resin molding machine evenly and in order.

【0027】また、原材料31の交換時における掃除の
し易さ等の装置の取り扱いについては、真空除湿乾燥装
置本体7の上蓋16に熱交換器8を一体化し、簡単な止
め金具で取り外しを行えるようにしたので、熱交換器8
にP.T.C内蔵襞付きパイプ10を縦方向に配列して
原材料31の残留を抑制できる。しかも、上蓋16を真
空除湿乾燥装置本体7から開き、貯蔵タンク12と真空
除湿乾燥装置本体7とを簡単に分離でき、これら貯蔵タ
ンク12及び真空除湿乾燥装置本体7の掃除を容易に行
うことができる。
As for the handling of the apparatus such as ease of cleaning when replacing the raw material 31, the heat exchanger 8 is integrated with the upper lid 16 of the vacuum dehumidifying / drying apparatus main body 7, and can be removed with a simple stopper. So that heat exchanger 8
P. T. By arranging the C-folded pipes 10 with a built-in fold in the longitudinal direction, the remaining of the raw material 31 can be suppressed. In addition, the upper lid 16 is opened from the vacuum dehumidifying / drying device main body 7, and the storage tank 12 and the vacuum dehumidifying / drying device main body 7 can be easily separated from each other, so that the storage tank 12 and the vacuum dehumidifying / drying device main body 7 can be easily cleaned. it can.

【0028】このように、真空方式による除湿乾燥装置
によれば、合成樹脂粉粒体の除湿乾燥の短時間、高効率
化に加えて省スペース化、軽量化、省エネルギー化を図
ることができ、成形製品の精密化、小型成形機用の原材
料の除湿乾燥装置の製品化等の要請に応じることがで
き、成形機毎に除湿乾燥装置を設置する理想的な成形シ
ステムの構築に寄与することができる。
As described above, according to the dehumidifying and drying apparatus using a vacuum system, space saving, weight saving, and energy saving can be achieved in addition to the short time and high efficiency of dehumidifying and drying of synthetic resin particles. We can respond to the demands for refinement of molded products and commercialization of dehumidifying and drying equipment for raw materials for small molding machines, contributing to the construction of an ideal molding system where dehumidifying and drying equipment is installed for each molding machine. it can.

【0029】[0029]

【発明の効果】以上説明したように、本発明によれば、
次の効果が得られる。 a 合成樹脂粉粒体を乾燥装置本体内に搬送し、乾燥装
置本体内でその合成樹脂粉粒体の除湿乾燥を真空処理と
加熱処理とを併用して行うので、合成樹脂粉粒体の除湿
乾燥処理の短時間化、高効率化を実現することができ
る。 b 乾燥装置本体に対する合成樹脂粉粒体の供給の効率
化、除湿乾燥処理の迅速化、乾燥後の合成樹脂粉粒体の
乾燥装置本体からの排出の迅速化、成形処理に比較して
除湿乾燥処理高速化を図ることができる。合成樹脂成形機側の処理量に対して除湿乾燥の処理
量を増大させることができ、貯蔵手段に合成樹脂粉粒体
を貯蔵して待機させて合成樹脂成形機に連続的に供給で
き、しかも、貯蔵手段への合成樹脂粉粒体の排出に応じ
て乾燥装置本体に所定量の合成樹脂粉粒体を供給でき、
乾燥処理の迅速化とともに樹脂成形の高品質化に寄与す
ることができる。
As described above, according to the present invention,
The following effects are obtained. a. Since the synthetic resin particles are conveyed into the drying device main body, and the synthetic resin particles are dehumidified and dried in the drying device main body by using both the vacuum treatment and the heat treatment, the synthetic resin powder is dehumidified. Shortening of the drying process and high efficiency can be realized. b Drying device efficiency supply of the synthetic resin powder or granular material for the body, faster dehumidifying and drying process, faster elimination from the drying apparatus main body of the synthetic resin powder granules after drying, as compared to the adult form processing dehumidification The speed of the drying process can be increased. c Dehumidifying and drying treatment for the processing amount of the synthetic resin molding machine
The amount can be increased and storage means of synthetic resin powder
Storage and waiting for continuous supply to the synthetic resin molding machine
And according to the discharge of the synthetic resin particles into the storage means
Can supply a predetermined amount of synthetic resin particles to the drying device body,
It is possible to contribute to the high quality of resin molding as well as the quick drying process .

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の合成樹脂粉粒体の除湿乾燥方法及びそ
の装置の実施の形態として全体構成を略示した縦断面図
である。
FIG. 1 is a longitudinal sectional view schematically showing an overall configuration as an embodiment of a method and an apparatus for dehumidifying and drying synthetic resin particles of the present invention.

【図2】下自動開閉バルブが開いた状態を略示した断面
図である。
FIG. 2 is a sectional view schematically showing a state in which a lower automatic opening / closing valve is opened.

【図3】下自動開閉バルブが閉じた状態を略示した断面
図である。
FIG. 3 is a sectional view schematically showing a state in which a lower automatic opening / closing valve is closed.

【図4】貯蔵タンクを分離可能にした状態を略示した断
面図である。
FIG. 4 is a sectional view schematically showing a state in which a storage tank is made separable.

【符号の説明】 2 吸上げ機構(樹脂供給手段) 5 真空ポンプ(真空形成手段) 7 真空除湿乾燥装置本体 8 熱交換器(加熱手段) 11 ヒートパイプ(加熱手段) 22 下自動開閉バルブ(樹脂排出手段)[Description of Signs] 2 Suction mechanism (resin supply means) 5 Vacuum pump (vacuum forming means) 7 Vacuum dehumidifying / drying apparatus main body 8 Heat exchanger (heating means) 11 Heat pipe (heating means) 22 Lower automatic opening / closing valve (resin) Discharge means)

───────────────────────────────────────────────────── フロントページの続き (72)発明者 大沼 良啓 静岡県富士市西柏原新田201番地 高木 産業株式会社内 (72)発明者 今井 浩 静岡県富士市西柏原新田201番地 高木 産業株式会社内 (72)発明者 高木 智 静岡県富士市西柏原新田201番地 高木 産業株式会社内 (56)参考文献 特開 平1−286806(JP,A) 特開 昭59−22711(JP,A) 特開 平2−127006(JP,A) 特開 平4−85008(JP,A) 特開 昭55−128442(JP,A) (58)調査した分野(Int.Cl.7,DB名) B29B 13/06 F26B 5/04 - 5/16 F26B 17/16 - 17/34 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Yoshihiro Onuma 201 Nishi-Kashiwara Nitta 201, Fuji City, Shizuoka Prefecture Inside Takagi Sangyo Co., Ltd. (72) Inventor Hiroshi Imai 201 Nishi-Kashiwara Nitta 201, Fuji City, Shizuoka Prefecture Takagi Sangyo Stock In-company (72) Inventor Satoshi Takagi 201 Nishi-Kashiwara Nitta, Fuji City, Shizuoka Prefecture Inside Takagi Sangyo Co., Ltd. (56) References JP-A-1-286806 (JP, A) JP-A-59-22711 (JP, A JP-A-2-127006 (JP, A) JP-A-4-85008 (JP, A) JP-A-55-128442 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B29B 13/06 F26B 5/04-5/16 F26B 17/16-17/34

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 合成樹脂成形機に供給される合成樹脂粉
粒体を真空下で加熱して除湿乾燥させる、合成樹脂粉粒
体の除湿乾燥方法であって、 合成樹脂粉粒体の除湿乾燥の後、乾燥装置本体の真空を
解除する工程と、 前記乾燥装置本体から除湿乾燥を施した前記合成樹脂粉
粒体の所定量を排出する工程と、 前記乾燥装置本体に除湿乾燥前の前記合成樹脂粉粒体の
所定量を補給する工程と、 前記乾燥装置本体を閉鎖して前記合成樹脂粉粒体を加熱
する工程と、 前記加熱中、前記乾燥装置本体内から空気を排出させて
前記乾燥装置本体内を真空状態に維持するとともに、適
当量の空気を前記乾燥装置本体内に導入させ、前記合成
樹脂粉粒体の加熱により発生した蒸気を前記空気ととも
に外部へ排出させる工程と、 除湿乾燥の後、前記乾燥装置本体の排出口から排出させ
た前記合成樹脂粉粒体を一時的に貯蔵手段に貯蔵させる
工程と、 前記貯蔵手段に前記合成樹脂粉粒体が満たされたことを
検出して前記乾燥装置本体の前記排出口を閉じるととも
に、前記乾燥装置本体に所定量の前記合成樹脂粉粒体を
搬送する工程と、 前記貯蔵手段から前記合成樹脂粉粒体を前記合成樹脂成
形機に供給する工程と、 を備えたことを特徴とする合成樹脂粉粒体の除湿乾燥方
法。
1. A method for dehumidifying and drying synthetic resin particles, wherein the synthetic resin particles supplied to a synthetic resin molding machine are heated under vacuum to dehumidify and dry, and wherein the synthetic resin particles are dehumidified and dried. After that, a step of releasing the vacuum of the drying device main body; a step of discharging a predetermined amount of the synthetic resin particles subjected to dehumidification and drying from the drying device main body; and a step of performing the synthesis before the dehumidification drying to the drying device main body. A step of replenishing a predetermined amount of the resin particles, a step of closing the drying device body and heating the synthetic resin particles, and discharging the air from the drying device body during the heating to dry the synthetic resin particles. While maintaining a vacuum inside the
An equivalent amount of air is introduced into the drying device main body, and the
The steam generated by heating the resin particles is combined with the air.
Discharging the synthetic resin powder granules discharged from the outlet of the drying device main body after dehumidifying and drying; and temporarily storing the synthetic resin powder particles in a storage means. Detecting that the granules are filled, closing the discharge port of the drying device main body, and transporting a predetermined amount of the synthetic resin powder granules to the drying device main body; and Supplying a powder to the synthetic resin molding machine. A method for dehumidifying and drying a synthetic resin powder.
【請求項2】 合成樹脂成形機に供給される合成樹脂粉
粒体を真空下で加熱して除湿乾燥させる、合成樹脂粉粒
体の除湿乾燥装置であって、 合成樹脂粉粒体が供給される乾燥装置本体と、 この乾燥装置本体に前記合成樹脂粉粒体を供給する樹脂
供給手段と、 前記乾燥装置本体内の前記合成樹脂粉粒体を加熱する加
熱手段と、 前記合成樹脂粉粒体の加熱中、前記乾燥装置本体を空気
の排出により真空化する真空形成手段と、 前記乾燥装置本体の排出口を開閉する開閉手段と、 この開閉手段により前記排出口を閉じるとともに 前記真
空形成手段前記空気排出時、前記乾燥装置本体内に適
当量の空気を導入させる空気導入手段と、 前記乾燥装置本体から排出させた前記合成樹脂粉粒体を
前記合成樹脂成形機に供給する前に一時的に貯蔵する貯
蔵手段と、 この貯蔵手段に前記合成樹脂粉粒体が満たされたことを
検出して前記開閉手段を作動させるとともに、前記樹脂
供給手段によって前記乾燥装置本体に所定量の前記合成
樹脂粉粒体を供給させる制御手段と、 を備えたことを特徴とする合成樹脂粉粒体の除湿乾燥装
置。
2. A dehumidifying and drying apparatus for a synthetic resin powder, wherein the synthetic resin powder supplied to a synthetic resin molding machine is heated under vacuum to dehumidify and dry, wherein the synthetic resin powder is supplied. A drying device main body, a resin supply means for supplying the synthetic resin powder to the drying device main body, a heating means for heating the synthetic resin powder in the drying device main body, and the synthetic resin powder. during heating, and vacuum forming means for evacuating the drying apparatus main body by the discharge of air, and closing means for opening and closing the outlet of the drying apparatus main body, of the vacuum forming means is closed the discharge opening by the opening and closing means At the time of discharging the air, air introducing means for introducing an appropriate amount of air into the drying device main body, and temporarily supplying the synthetic resin powder discharged from the drying device main body to the synthetic resin molding machine. Storage to store Means for detecting that the storage means is filled with the synthetic resin particles , operating the opening / closing means, and supplying a predetermined amount of the synthetic resin particles to the drying device main body by the resin supply means. A dehumidifying / drying device for synthetic resin particles, comprising: a control unit for supplying.
JP36728899A 1991-05-08 1999-12-24 Method and apparatus for dehumidifying and drying synthetic resin particles Expired - Lifetime JP3354913B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP36728899A JP3354913B2 (en) 1991-05-08 1999-12-24 Method and apparatus for dehumidifying and drying synthetic resin particles

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP19897991A JP3233419B2 (en) 1991-05-08 1991-05-08 Dehumidifying and drying device for synthetic resin powder by vacuum heating method
JP36728899A JP3354913B2 (en) 1991-05-08 1999-12-24 Method and apparatus for dehumidifying and drying synthetic resin particles

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP19897991A Division JP3233419B2 (en) 1991-05-08 1991-05-08 Dehumidifying and drying device for synthetic resin powder by vacuum heating method

Publications (2)

Publication Number Publication Date
JP2000167831A JP2000167831A (en) 2000-06-20
JP3354913B2 true JP3354913B2 (en) 2002-12-09

Family

ID=26511278

Family Applications (1)

Application Number Title Priority Date Filing Date
JP36728899A Expired - Lifetime JP3354913B2 (en) 1991-05-08 1999-12-24 Method and apparatus for dehumidifying and drying synthetic resin particles

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Country Link
JP (1) JP3354913B2 (en)

Also Published As

Publication number Publication date
JP2000167831A (en) 2000-06-20

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