JPH0592426A - Particle feed hopper for pre-expander - Google Patents

Particle feed hopper for pre-expander

Info

Publication number
JPH0592426A
JPH0592426A JP28364491A JP28364491A JPH0592426A JP H0592426 A JPH0592426 A JP H0592426A JP 28364491 A JP28364491 A JP 28364491A JP 28364491 A JP28364491 A JP 28364491A JP H0592426 A JPH0592426 A JP H0592426A
Authority
JP
Japan
Prior art keywords
hopper
drying tower
hot air
drying
hopper part
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
Application number
JP28364491A
Other languages
Japanese (ja)
Other versions
JP3001309B2 (en
Inventor
Kinzo Masuda
欣三 増田
Kazuhiro Tsuneto
和寛 常藤
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry 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
Application filed by Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP28364491A priority Critical patent/JP3001309B2/en
Publication of JPH0592426A publication Critical patent/JPH0592426A/en
Application granted granted Critical
Publication of JP3001309B2 publication Critical patent/JP3001309B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Auxiliary Methods And Devices For Loading And Unloading (AREA)
  • Feeding Of Articles To Conveyors (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PURPOSE:To perform efficient drying by obtaining a particle feed hopper fitted with a dryer constituted so that foamable resin particles are pre-expanded to be received in a hopper part and the pre-expanded particles are sucked up by a particle feed blower to be blown in the drying tower provided to the upper surface of the hopper part along with hot air and returned to the hopper part to be circulated and dried to be fed to a next process. CONSTITUTION:A hopper part 3 is provided to the feed-out port 2 of a pre-expander 1 and pre-expanded resin particles with low expanding magnification of about 3-10 times are received in the hopper part 3. A lid 5 is provided to the open upper surface of the hopper part 3 and a drying tower 6 is erected on the lid 5. The lid 5 and the drying tower 6 are formed of an air permeable metal net not permitting the resin particles to pass. The resin particles are sucked from the bottom part of the hopper part 3 by a particle feed blower 13 to be struck by the internal blades of the blower 13 and blown up into the drying tower 6 from the inner pipe 10 of a blowoff nozzle 8 composed of a double pipe and hot air is blown up from an outer pipe 11. Evaporated moisture is discharged from the side surface of the drying tower along with hot air and the resin particles return to the hopper part 3. This operation is repeated and a damper 15 is changed over after drying and the dried resin particles are sent to an ageing silo by the particle feed blower 13.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、予備発泡機用送粒ホッ
パに関し、詳しくは予備発泡機により発泡性樹脂粒子を
3〜10倍程度の低発泡倍率で予備発泡(以下、「低倍
発泡」と略称する)させて得た予備発泡粒子を乾燥する
装置を設けた送粒ホッパに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a granulating hopper for a pre-expanding machine, and more specifically, a pre-expanding machine for pre-expanding expandable resin particles at a low expansion ratio of about 3 to 10 times (hereinafter referred to as "low expansion foaming" (Hereinafter abbreviated as “.”).

【0002】[0002]

【従来の技術】従来より、予備発泡機で発泡性樹脂粒子
を水蒸気により加熱発泡させて得た予備発泡粒子を乾燥
する場合には、下記3種類の方法が採用されている。第
1の方法は、予備発泡完了後、予備発泡機内に冷風、温
風又は熱風を吹き込んで乾燥するものである。第2の方
法は、前記第1の方法で乾燥した後、予備発泡粒子を温
風又は熱風により熟成サイロに圧送することにより更に
乾燥するものである。第3の方法は、予備発泡完了後、
予備発泡機内での乾燥を行なわずに排出し、排出した予
備発泡粒子を貯留槽又はトンネル状容器内に収納して熱
風を吹き込むことにより乾燥するものである。
2. Description of the Related Art Conventionally, the following three types of methods have been employed to dry pre-expanded particles obtained by heating and expanding foamable resin particles with steam in a pre-expanding machine. The first method is to blow cold air, warm air, or hot air into the pre-foaming machine to dry it after the completion of pre-foaming. In the second method, after the drying in the first method, the pre-expanded particles are pressure-fed to the aged silo with hot air or hot air to further dry the particles. The third method is that after pre-foaming is completed,
It is discharged without being dried in the pre-foaming machine, and the discharged pre-foamed particles are stored in a storage tank or a tunnel-shaped container and blown with hot air to dry.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記従来の方
法の内、第1の方法によれば、予備発泡機の1サイクル
(原料投入→予備発泡→乾燥→排出)に要する時間が長
くなって、予備発泡機の処理能力が低下する。また、第
2の方法によれば、予備発泡粒子が低倍発泡の場合、予
備発泡粒子の比重が大きいので圧送により送粒すること
ができない。また、第3の方法によれば、収納状態の予
備発泡粒子に熱風を吹き込むので乾燥に長時間を要し、
しかも予備発泡粒子が低倍発泡で比重が大きい場合には
更に長時間を要し、さらに乾燥設備の設置場所が広くな
る。
However, according to the first method of the above-mentioned conventional methods, the time required for one cycle of the prefoaming machine (feeding of raw material → preliminary foaming → drying → discharging) becomes long. , The processing capacity of the pre-foaming machine decreases. Further, according to the second method, when the pre-expanded particles have a low expansion ratio, the specific gravity of the pre-expanded particles is large, and therefore the particles cannot be fed by pressure feeding. Further, according to the third method, since hot air is blown into the pre-expanded particles in the stored state, it takes a long time to dry,
Moreover, when the pre-expanded particles have a low expansion ratio and a large specific gravity, it takes a longer time, and the installation place of the drying equipment becomes wider.

【0004】本発明は、従来の送粒ホッパを改良して、
上述のような問題点を取り除くことを目的とする。
The present invention is an improvement over the conventional grain feeding hopper,
The purpose is to eliminate the above-mentioned problems.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
に、本発明の予備発泡機用送粒ホッパは、予備発泡機の
予備発泡粒子排出口に設けたホッパ部の開放上面に予備
発泡粒子を通過させない蓋体を取り付け、該蓋体上に通
気性を有するが予備発泡粒子を通過させない筒状の乾燥
塔を立設し、前記ホッパ部の底部の払出口に送粒ブロア
を接続するとともに、前記ホッパ部の側壁に内外二重管
構造の吹出ノズルを前記乾燥塔に向けて取り付け、前記
吹出ノズルの内管を切替ダンパを介して前記送粒ブロア
の吐出口側に接続するとともに、前記吹出ノズルの外管
に熱風発生装置を接続してなるものである。
In order to achieve the above object, a granulating hopper for a pre-expanding machine of the present invention comprises a pre-expanding particle on an open upper surface of a hopper portion provided at a pre-expanding particle discharge port of the pre-expanding machine. A lid that does not pass through, a standing cylindrical drying tower that has air permeability but does not allow the pre-expanded particles to pass through is installed on the lid, and a granulation blower is connected to the outlet of the bottom of the hopper. A blow-out nozzle having an inner-outer double-pipe structure is attached to the side wall of the hopper portion toward the drying tower, and the inner pipe of the blow-out nozzle is connected to the discharge port side of the granulating blower through a switching damper, and A hot air generator is connected to the outer tube of the blowout nozzle.

【0006】[0006]

【作用】上記構成の送粒ホッパは、低倍発泡用予備発泡
機に取り付けられ、予備発泡機から排出された低倍発泡
の予備発泡粒子を一旦内部に収納する。送粒ブロアは、
ホッパ部の底部の払出口から予備発泡粒子を吸引し、内
部の羽根で予備発泡粒子を叩いて吐出口から切替ダンパ
を介して吹出ノズルの内管に送粒し、乾燥塔に向けて吹
き上げる。その際、予備発泡粒子は、低倍発泡のため、
羽根で叩かれても砕けるようなことはない。他方、熱風
発生装置は、乾燥用熱風を吹出ノズルの外管に送気し、
乾燥塔に向けて吹き上げる。吹出ノズルから吹き上げら
れた予備発泡粒子及び熱風は混合して乾燥塔内に入り、
熱風が予備発泡粒子を乾燥させる。これにより、蒸発し
た水分は熱風とともに乾燥塔の壁面から大気中に放出さ
れ、予備発泡粒子は落下してホッパ部の底部に戻る。上
記乾燥循環を所要回数繰り返して乾燥が完了すると切替
ダンパが切り替わり、送粒ブロアは乾燥した予備発泡粒
子を次の設備、例えば熟成サイロに送粒する。
The granulating hopper having the above construction is attached to the low-expansion pre-expanding machine, and temporarily stores the low-expansion pre-expanded particles discharged from the pre-expanding machine. Grain blower,
The pre-expanded particles are sucked from the outlet at the bottom of the hopper, the pre-expanded particles are beaten by the inner blade, and the pre-expanded particles are sent from the discharge port to the inner tube of the blowout nozzle through the switching damper and blown up toward the drying tower. At that time, since the pre-expanded particles are low-expansion foam,
It won't shatter even if it is hit with the wings. On the other hand, the hot air generator sends hot air for drying to the outer tube of the blowing nozzle,
Blow up towards the drying tower. The pre-expanded particles and hot air blown up from the blowing nozzle are mixed and enter the drying tower,
Hot air dries the pre-expanded particles. As a result, the evaporated water is released into the atmosphere from the wall surface of the drying tower together with the hot air, and the pre-expanded particles fall back to the bottom of the hopper. When the drying cycle is repeated a required number of times and the drying is completed, the switching damper is switched, and the granulation blower transfers the dried pre-expanded particles to the next facility, for example, an aged silo.

【0007】[0007]

【実施例】以下、本発明の一実施例を図1に基づいて説
明する。本実施例の送粒ホッパでは、図1に示すよう
に、低倍発泡用予備発泡機1の予備発泡粒子排出口2に
ホッパ部3を設けている。このホッパ部3は、内部に整
粒用ふるい4を張設し、開放上面に蓋体5を取り付けて
蓋体5上に筒状の乾燥塔6を立設し、底部に払出口7を
設けるとともに、側壁に吹出ノズル8を乾燥塔6に向け
て取り付けたものである。蓋体5及び乾燥塔6は、通気
性を有するが予備発泡粒子を通過させない金網等からな
っており、払出口7には金網を張り付けた空気吸込口9
を設けてあり、吹出ノズル8は内管10及び外管11か
らなる内外二重管構造となっている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. In the particle feeding hopper of this embodiment, as shown in FIG. 1, a hopper portion 3 is provided at a pre-expanded particle discharge port 2 of a low-expansion pre-expanding machine 1. The hopper 3 has a sieving sieve 4 stretched inside, a lid 5 is attached to the open upper surface, a cylindrical drying tower 6 is erected on the lid 5, and a discharge port 7 is provided at the bottom. At the same time, the blowing nozzle 8 is attached to the side wall toward the drying tower 6. The lid 5 and the drying tower 6 are made of wire mesh or the like that has air permeability but does not allow pre-expanded particles to pass through, and the outlet 7 has an air suction port 9 attached with the wire mesh.
Is provided, and the blowout nozzle 8 has an inner-outer double pipe structure including an inner pipe 10 and an outer pipe 11.

【0008】そして、払出口7に接続した送粒管12に
送粒ブロア13を設け、送粒ブロア13の吐出口14側
に切替ダンパ15及び循環管16を介して吹出ノズル8
の内管10を接続している。切替ダンパ15は、循環管
16を送粒管12に導通させる「循環」位置と、循環管
16を送粒管12から遮断する「送粒」位置とを有する
三方向ダンパである。また、吹出ノズル8の外管11に
は、乾燥管17を介して熱風発生装置18を接続してい
る。熱風発生装置18は、ヒータ19に送風ブロア20
を接続してなり、温度が室温〜最高80℃程度の乾燥用
熱風を供給する。
Then, a granulation blower 13 is provided in the granulation pipe 12 connected to the outlet 7, and a blowing nozzle 8 is provided on the discharge port 14 side of the granulation blower 13 via a switching damper 15 and a circulation pipe 16.
The inner pipe 10 of is connected. The switching damper 15 is a three-way damper having a “circulation” position where the circulation pipe 16 is brought into conduction with the granulation pipe 12 and a “granulation” position where the circulation pipe 16 is cut off from the granulation pipe 12. Further, a hot air generator 18 is connected to the outer tube 11 of the blowing nozzle 8 via a drying tube 17. The hot air generator 18 sends a blower 20 to the heater 19.
Is connected, and hot air for drying having a temperature of room temperature to a maximum of about 80 ° C. is supplied.

【0009】上記構成の送粒ホッパにおいては、予備発
泡機1の予備発泡粒子排出口2から排出された低倍発泡
の予備発泡粒子21をホッパ部3内のふるい4で整粒し
た後、一旦ホッパ部3の底部に収納する。続いて、送粒
ブロア13及び熱風発生装置18が運転状態に入り、切
替ダンパ15が「循環」位置になる。これにより、送粒
ブロア13は、ホッパ部3の払出口7から送粒管12を
介して予備発泡粒子21を吸引し、内部の羽根で予備発
泡粒子21を叩いて吐出口14から送粒管12、切替ダ
ンパ15及び循環管16を介して吹出ノズル8の内管1
0に送粒し、乾燥塔6に向けて吹き上げる。その際、予
備発泡粒子21は、低倍発泡であるので、羽根で叩かれ
ても砕けるようなことはない。他方、熱風発生装置18
は、乾燥用熱風を乾燥管17を介して吹出ノズル8の外
管11に送気し、乾燥塔6に向けて吹き上げる。吹出ノ
ズル8から吹き上げられた予備発泡粒子21及び熱風は
混合して乾燥塔6内に入り、熱風が予備発泡粒子21を
乾燥させる。これにより、蒸発した水分は熱風とともに
乾燥塔6の壁面から大気中に放出され、予備発泡粒子2
1は落下してホッパ部3の底部に戻る。上記乾燥循環を
所要回数繰り返して乾燥が完了すると、切替ダンパ15
が「送粒」位置に切り替わるとともに、熱風発生装置1
8が停止し、送粒ブロア13は乾燥した予備発泡粒子2
1をホッパ部3の払出口7から吸引して、吐出口14か
ら切替ダンパ15及び送粒管12を介して次の設備、例
えば熟成サイロに送粒する。予備発泡粒子21は、熱風
で乾燥されているので、熟成サイロにおける養生が促進
される。
In the granulating hopper having the above construction, the low-expansion pre-expanded particles 21 discharged from the pre-expanded particle discharge port 2 of the pre-expander 1 are sized by the sieve 4 in the hopper section 3 and then once It is stored in the bottom of the hopper unit 3. Subsequently, the particle-sending blower 13 and the hot air generator 18 enter the operating state, and the switching damper 15 is set to the “circulation” position. As a result, the particle-sending blower 13 sucks the pre-expanded particles 21 from the outlet 7 of the hopper 3 through the particle-sending tube 12, hits the pre-expanded particles 21 with the internal blade, and discharges the pre-expanded particles 21 from the discharge port 14. The inner pipe 1 of the blow-out nozzle 8 via the switching damper 15, the switching damper 15, and the circulation pipe 16.
The particles are fed to 0 and blown up toward the drying tower 6. At this time, since the pre-expanded particles 21 are low-expansion foam, they do not break even if they are hit with a blade. On the other hand, the hot air generator 18
Sends the hot air for drying to the outer pipe 11 of the blowing nozzle 8 through the drying pipe 17 and blows it up toward the drying tower 6. The pre-foamed particles 21 blown up from the blow-out nozzle 8 and the hot air are mixed and enter the drying tower 6, and the hot air dries the pre-foamed particles 21. As a result, the evaporated water is released into the atmosphere from the wall surface of the drying tower 6 together with the hot air, and the pre-expanded particles 2
1 drops and returns to the bottom of the hopper 3. When the drying cycle is repeated a required number of times to complete the drying, the switching damper 15
Is switched to the "granulation" position and the hot air generator 1
8 is stopped, and the granulation blower 13 is dried pre-expanded particles 2
1 is sucked from the discharge port 7 of the hopper unit 3 and is fed from the discharge port 14 to the next facility, for example, an aged silo via the switching damper 15 and the grain feeding pipe 12. Since the pre-expanded particles 21 are dried with hot air, curing in the aged silo is promoted.

【0010】ちなみに、本発明の送粒ホッパにおける乾
燥時間と従来の方法における乾燥時間との測定結果を表
1に示す。この場合、本発明では、発泡スチレンビーズ
「カネパールHDB」(商品名、鐘淵化学工業株式会社
製)を低倍発泡用予備発泡機内で加熱蒸気により発泡倍
率10倍及び5倍に予備発泡させた後直ちに送粒ホッパ
内に排出し、予備発泡粒子の表面しめりがなくなるま
で、即ち表面水分が約0.5%になるまで乾燥循環さ
せ、その乾燥時間を測定した。
Incidentally, Table 1 shows the measurement results of the drying time in the granulating hopper of the present invention and the drying time in the conventional method. In this case, in the present invention, expanded styrene beads "Kanepearl HDB" (trade name, manufactured by Kaneka Kagaku Kogyo Co., Ltd.) were pre-expanded to a expansion ratio of 10 times and 5 times by heating steam in a low-expansion pre-expansion machine. Immediately after that, the granules were discharged into a granulating hopper and dried and circulated until the pre-expanded particles had no surface tightness, that is, until the surface water content was about 0.5%, and the drying time was measured.

【0011】また、従来の方法では、上記と同じ条件で
発泡スチレンビーズを予備発泡させた後加熱蒸気を停止
し、予備発泡機内に冷却空気を送気して乾燥させ、予備
発泡粒子の表面しめりがなくなるまでの乾燥時間を測定
した。
Further, in the conventional method, after the expanded styrene beads are pre-expanded under the same conditions as described above, the heating steam is stopped, cooling air is blown into the pre-expanding machine to dry the pre-expanded particles, and the surface shrinkage of the pre-expanded particles is suppressed. The drying time until disappearance was measured.

【0012】[0012]

【表1】 [Table 1]

【0013】表1から明らかなように、本発明における
乾燥時間は従来法における乾燥時間の1/4以下に短縮
されている。
As is clear from Table 1, the drying time in the present invention is shortened to 1/4 or less of the drying time in the conventional method.

【0014】[0014]

【発明の効果】本発明は、以上説明したように、予備発
泡粒子を乾燥用熱風とともに吹出ノズルから乾燥塔内に
吹き上げて乾燥するので、極めて短時間で乾燥すること
ができる。また、予備発泡機内での乾燥が不要であるの
で、予備発泡機の1サイクルに要する時間が短縮され、
予備発泡機の処理能力が向上する。また、乾燥装置を送
粒ホッパに設けるので、設置スペースが狭くてすむ。さ
らに、予備発泡粒子を熱風により乾燥するので、予備発
泡粒子の熟成サイロにおける養生が促進される。
INDUSTRIAL APPLICABILITY As described above, according to the present invention, the pre-expanded particles are blown up from the blowing nozzle into the drying tower together with the hot air for drying, so that the pre-expanded particles can be dried in an extremely short time. Further, since the drying in the pre-foaming machine is unnecessary, the time required for one cycle of the pre-foaming machine is shortened,
The processing capacity of the pre-foaming machine is improved. Further, since the drying device is provided in the grain feeding hopper, the installation space is small. Further, since the pre-expanded particles are dried by hot air, the curing of the pre-expanded particles in the aging silo is promoted.

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

【図1】本発明の一実施例を示す送粒ホッパの全体構成
図である。
FIG. 1 is an overall configuration diagram of a grain feeding hopper showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 予備発泡機 2 予備発泡粒
子排出口 3 ホッパ部 5 蓋体 6 乾燥塔 7 払出口 8 吹出ノズル 10 内管 11 外管 13 送粒ブロ
ア 14 吐出口 15 切替ダン
パ 18 熱風発生装置 21 予備発泡
粒子
1 Pre-foaming machine 2 Pre-foamed particle discharge port 3 Hopper part 5 Lid body 6 Drying tower 7 Discharge port 8 Outflow nozzle 10 Inner tube 11 Outer tube 13 Grain blower 14 Discharge port 15 Switching damper 18 Hot air generator 21 Pre-foamed particle 21

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 B29K 105:04 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Internal reference number FI technical display location B29K 105: 04

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 予備発泡機の予備発泡粒子排出口に設け
たホッパ部の開放上面に予備発泡粒子を通過させない蓋
体を取り付け、該蓋体上に通気性を有するが予備発泡粒
子を通過させない筒状の乾燥塔を立設し、前記ホッパ部
の底部の払出口に送粒ブロアを接続するとともに、前記
ホッパ部の側壁に内外二重管構造の吹出ノズルを前記乾
燥塔に向けて取り付け、前記吹出ノズルの内管を切替ダ
ンパを介して前記送粒ブロアの吐出口側に接続するとと
もに、前記吹出ノズルの外管に熱風発生装置を接続して
なる予備発泡機用送粒ホッパ。
1. A lid that does not allow pre-expanded particles to pass through is attached to an open upper surface of a hopper portion provided at a pre-expanded particle discharge port of the pre-expanding machine, and the pre-expanded particles do not pass through the cover having air permeability. A cylindrical drying tower is erected, and a grain-blowing blower is connected to the outlet of the bottom of the hopper, and a blow-out nozzle having an inner and outer double pipe structure is attached to the sidewall of the hopper toward the drying tower, A granulating hopper for a pre-foaming machine, in which an inner tube of the blowout nozzle is connected to a discharge port side of the particle feeding blower through a switching damper, and a hot air generator is connected to an outer tube of the blowout nozzle.
JP28364491A 1991-10-02 1991-10-02 Feeding hopper for prefoaming machine Expired - Fee Related JP3001309B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28364491A JP3001309B2 (en) 1991-10-02 1991-10-02 Feeding hopper for prefoaming machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28364491A JP3001309B2 (en) 1991-10-02 1991-10-02 Feeding hopper for prefoaming machine

Publications (2)

Publication Number Publication Date
JPH0592426A true JPH0592426A (en) 1993-04-16
JP3001309B2 JP3001309B2 (en) 2000-01-24

Family

ID=17668191

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28364491A Expired - Fee Related JP3001309B2 (en) 1991-10-02 1991-10-02 Feeding hopper for prefoaming machine

Country Status (1)

Country Link
JP (1) JP3001309B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05287114A (en) * 1992-04-10 1993-11-02 Kanegafuchi Chem Ind Co Ltd Method for drying and feeding particle for preexpanding machine and its apparatus
JP2007238321A (en) * 2006-03-13 2007-09-20 Joban Kyodo Karyoku Kk Dust flying preventing device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05287114A (en) * 1992-04-10 1993-11-02 Kanegafuchi Chem Ind Co Ltd Method for drying and feeding particle for preexpanding machine and its apparatus
JP2007238321A (en) * 2006-03-13 2007-09-20 Joban Kyodo Karyoku Kk Dust flying preventing device

Also Published As

Publication number Publication date
JP3001309B2 (en) 2000-01-24

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