JPH06262625A - Bulk density adjusting method for ground foamed resin and device therefor - Google Patents

Bulk density adjusting method for ground foamed resin and device therefor

Info

Publication number
JPH06262625A
JPH06262625A JP5578493A JP5578493A JPH06262625A JP H06262625 A JPH06262625 A JP H06262625A JP 5578493 A JP5578493 A JP 5578493A JP 5578493 A JP5578493 A JP 5578493A JP H06262625 A JPH06262625 A JP H06262625A
Authority
JP
Japan
Prior art keywords
foamed resin
product
bulk density
stirring
crushed
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
JP5578493A
Other languages
Japanese (ja)
Other versions
JP2840518B2 (en
Inventor
Juichi Omori
寿一 大森
Tsuyoshi Yamashita
剛志 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.)
Sekisui Kasei Co Ltd
Original Assignee
Sekisui Plastics 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 Sekisui Plastics Co Ltd filed Critical Sekisui Plastics Co Ltd
Priority to JP5578493A priority Critical patent/JP2840518B2/en
Publication of JPH06262625A publication Critical patent/JPH06262625A/en
Application granted granted Critical
Publication of JP2840518B2 publication Critical patent/JP2840518B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

PURPOSE:To easily adjust the bulk density of ground foamed resin product to desired value by a method wherein the predetermined amount of the ground foamed resin product is agitated under the predetermined heating condition and, during the agitation, the ground foamed resin product is partially heat-shrunk. CONSTITUTION:Ground foamed resin article is fed through an opening 35 in an agitating tank 40 so as to be gradually moved along the slope of a guide plate 3 in order to be fallen in the agitating tank 40. The interior of the agitating tank has heated atmosphere having the temperature of about 100-200 deg.C by the heat emitted from heaters 48. Under the above-mentioned state, by turning a rotary disc 41, the ground article is homogeneously agitated by the interaction of agitating bars 44 and 45 and fixed bars 46 and, as the same time, heated. By the agitation under the above-mentioned heated atmosphere, the surface of the ground article are partially heat-shrunk. Next, by transferring treated matter through guide funnels 51 and 52 to a metering hopper 53 through an opened shutter 37 so as to measure the bulk density of the treated matter with a load cell. The metered treated matter is transferred to a conveyor 56 and then transferred outside the device concerned through a blower 55.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は発泡樹脂粉砕品の嵩密度
調整方法及び装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for adjusting the bulk density of foamed resin crushed products.

【0002】[0002]

【従来の技術】従来より、廃材発泡スチロール等の樹脂
発泡材を再利用する方法として、樹脂発泡材を適宜粉砕
した後に一次発泡した新規材料と混合し、加熱加湿下で
新規材料を2次発泡させることにより発泡成形品として
一体成形することが行われている。このような再製品
は、例えば、軟弱地盤での築堤の際あるいはプラットフ
ォームの構築の際等に土中に埋設される比較的大型の発
泡樹脂製ブロックとして、あるいはフロートの芯材等と
して有効に用いられている。
2. Description of the Related Art Conventionally, as a method of reusing a resin foam material such as waste polystyrene foam, the resin foam material is appropriately crushed and then mixed with a newly foamed primary material, and the novel material is secondarily foamed under heating and humidification. As a result, they are integrally molded as a foam-molded product. Such remanufactured products are effectively used, for example, as relatively large foamed resin blocks that are buried in the soil when building embankments on soft ground or when constructing platforms, or as core materials for floats. Has been.

【0003】成形に際しては、粉砕機により1次粉砕さ
らに必要に応じて2次粉砕された廃材発泡樹脂材をその
まま新規材料と共に成形機に投入し加熱蒸気を注入し発
泡成形しているのが現状である。
At the time of molding, the current state is that the waste foam resin material which has been subjected to primary crushing by a crusher and, if necessary, secondary crushing is put into a molding machine as it is together with a new material, and heated steam is injected to perform foam molding. Is.

【0004】[0004]

【発明が解決しようとする課題】通常、発泡成形品の製
造に際しては加熱蒸気の温度やその供与量を調整して発
泡条件を調整してその嵩密度(発泡倍率)を変えること
により所望の製品重量を得るようにしている。新規な材
料のみにより発泡成形を行う場合にはこの方法により容
易に所望の嵩密度を得ることができ初期の調整目的を達
成することができる。しかし、廃材樹脂発泡材を破砕し
たものは粉砕前の状態よりも嵩密度が低くなるのが通常
であり粉砕条件によってその変化率も変動することか
ら、そのような粉砕品を新規材料に混入して成形する場
合に、その混合率を調整して成形される最終製品を求め
られる平均嵩密度(単位体積当たりの重量)に常時管理
することが困難であった。また、粉砕後の樹脂材料は必
ずしもすべてが等しい粒径に粉砕されることはなく嵩密
度の異なった集合の混合体となるのが普通であり、連続
して多数の発泡成形品を成形する場合に、すべてを同じ
重量ものとすることは事実上不可能であった。
Generally, in the production of foamed molded articles, desired temperature is controlled by adjusting the temperature of heated steam and its supply amount to adjust the foaming conditions to change its bulk density (foaming ratio). Trying to gain weight. When foam molding is performed using only a new material, this method can easily obtain a desired bulk density and achieve the initial adjustment purpose. However, the bulk density of crushed waste resin foam is usually lower than that before crushing, and the rate of change also changes depending on the crushing conditions. It has been difficult to always control the final product to be molded to a desired average bulk density (weight per unit volume) by adjusting the mixing ratio. In addition, after crushing, all resin materials are not always crushed to the same particle size and usually become a mixture of aggregates with different bulk densities. Moreover, it was virtually impossible to make them all the same weight.

【0005】さらに、混入する廃材樹脂材料の嵩密度と
同程度あるいはそれよりも高い嵩密度の成形品を得よう
とする場合には、廃材樹脂材料粉砕品の混合割合を低下
させざるを得ず、十分なコストメリットを上げることが
できなかった。また、樹脂製品を粉砕機により粉砕した
場合、ブロック状の粉砕品に加えて、気泡が破壊して薄
膜状となったものあるいは長繊維状となりわた状に集合
したもの等が含まれるのを避けることができない。この
種のものは比重がブロック状の粉砕品よりも小さいこと
から、粉砕物を新規材料と混合して発泡成形機に投入し
た場合に浮遊状態となる。長期間にわたり成形を行った
ときに、この浮遊物が成形機の蒸気供給口に目詰まりを
起こさせる原因となっていた。
Further, when it is desired to obtain a molded product having a bulk density equal to or higher than the bulk density of the waste resin material mixed in, the mixing ratio of the waste resin material crushed product must be reduced. , I couldn't get enough cost benefit. Also, when crushing resin products with a crusher, in addition to block-shaped crushed products, avoid including those that break into bubbles to form a thin film or aggregates into a long fiber form. I can't. Since the specific gravity of this kind of product is smaller than that of the block-shaped pulverized product, when the pulverized product is mixed with a new material and put into a foam molding machine, it becomes in a floating state. When molding was carried out for a long period of time, this floating substance caused the steam supply port of the molding machine to be clogged.

【0006】本発明は、廃材樹脂発泡体の粉砕品を新規
材料に混入して新たな発泡成形品を製造する場合の上記
のような粉砕品に起因する不都合を解消することを目的
としており、より具体的には所望の重量の最終製品を容
易に成形することができるように樹脂粉砕品を所望の嵩
比重のものとする方法及び装置を得ることを目的として
いる。
An object of the present invention is to eliminate the above-mentioned inconvenience caused by a crushed product when a crushed product of a waste resin foam is mixed with a new material to produce a new foam molded product. More specifically, it is an object of the present invention to provide a method and apparatus for making a crushed resin product have a desired bulk specific gravity so that a final product having a desired weight can be easily molded.

【0007】[0007]

【課題を解決するための手段】上記の課題を解決しかつ
目的を達成するために、本発明は、所定量の発泡樹脂粉
砕品を所定の加熱条件下で所要時間攪拌し、その間に発
泡樹脂粉砕品を部分的に熱収縮させることにより、全体
の嵩密度を調整することを特徴とする発泡樹脂粉砕品の
嵩密度調整方法を開示する。そこにおいて、所定の加熱
条件下で所定時間攪拌を受けた発泡樹脂粉砕品の一部を
取り出してその嵩密度を測定し、その測定値に基づき加
熱条件及び/又は攪拌時間を調整する工程をさらにもう
けることは好ましい態様である。
In order to solve the above-mentioned problems and to achieve the object, the present invention is to stir a predetermined amount of a foamed resin pulverized product for a required time under a predetermined heating condition, while Disclosed is a method for adjusting the bulk density of a foamed resin crushed product, which comprises adjusting the overall bulk density by partially heat-shrinking the crushed product. Here, a step of taking out a part of the foamed resin pulverized product that has been stirred for a predetermined time under a predetermined heating condition and measuring its bulk density, and adjusting the heating condition and / or the stirring time based on the measured value is further added. Producing is a preferred embodiment.

【0008】本発明はさらに、上記の調整方法を実施す
るための装置として、発泡樹脂粉砕品の定量供給手段、
該定量供給手段からの発泡樹脂粉砕品を受け入れるかつ
攪拌する攪拌槽、該攪拌槽内の発泡樹脂粉砕品を攪拌す
るための攪拌手段、該攪拌槽内の発泡樹脂粉砕品を加熱
するための加熱手段、及び攪拌及び加熱を受けた発泡樹
脂粉砕品を計量するための計量手段、とを有することを
特徴とする発泡樹脂粉砕品の嵩密度調整装置をも開示す
る。
The present invention further provides, as an apparatus for carrying out the above adjusting method, means for quantitatively supplying foamed resin crushed products,
A stirring tank for receiving and stirring the foamed resin crushed product from the quantitative supply means, a stirring means for stirring the foamed resin crushed product in the stirring tank, and a heating for heating the foamed resin crushed product in the stirring tank There is also disclosed a bulk density adjusting device for a crushed foamed resin product, comprising: a means and a measuring means for measuring the crushed foamed resin product that has been stirred and heated.

【0009】本発明でいう「発泡樹脂粉砕品」とは通常
再利用されうる発泡樹脂の粉砕品すべてをいうものであ
り、限定するものではないが、発泡スチロール粉砕品の
場合に本発明は特に有効に機能する。
The term "crushed product of foamed resin" as used in the present invention refers to all crushed products of foamed resin that can be usually reused, and is not limited, but the present invention is particularly effective in the case of crushed polystyrene foam. To function.

【0010】[0010]

【実施例】以下、添付の図面を参照した実施例の説明に
基づき本発明をより詳細に説明する。図1は本発明の処
理方法を実施するのに好適な処理装置の一実施例を示す
部分断面図である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will now be described in more detail based on the description of the embodiments with reference to the accompanying drawings. FIG. 1 is a partial cross-sectional view showing an embodiment of a processing apparatus suitable for carrying out the processing method of the present invention.

【0011】この処理装置は大別して粉砕品収容用手段
10、粉砕品攪拌・加熱手段30、及び計量・搬出手段
50とから構成される。粉砕品収容手段10は、発泡樹
脂材の粉砕品を受入れかつ保持するためのホッパー11
及び定量送り手段20とを有する。ホッパー11は投入
口12及び排出口13を有しかつその下方位置及び上方
位置には光学手段等適宜の手段からなるレベルセンサ1
4、15を有する。前記投入口12には図示しない従来
知られた粉砕機からブロアーを介して樹脂発泡材の粉砕
品が送り込まれる。排出口13の下流には排出される粉
砕品を計量しかつ後記する粉砕品攪拌・加熱手段30に
送り出すための定量送り手段20が位置している。定量
送り手段20はバルブ機能と計量機能を果たすものであ
り、図2に示すように回転軸21の軸方向に配置したU
字樋状の計量マス22及び該計量マス22を回転させる
ためのモータ25とを有する。該モータ25と前記回転
軸とは適宜の調速機構26を介して接続している。
This processing apparatus is roughly divided into a crushed product accommodating means 10, a crushed product stirring / heating means 30, and a weighing / unloading means 50. The crushed product storage means 10 is a hopper 11 for receiving and holding a crushed product of a foamed resin material.
And a fixed amount feeding means 20. The hopper 11 has a charging port 12 and a discharging port 13, and its lower position and upper position are level sensors 1 made of appropriate means such as optical means.
4 and 15. A crushed product of a resin foam material is fed into the input port 12 from a conventionally known crusher (not shown) through a blower. A fixed amount feeding means 20 for measuring the discharged pulverized product and sending it to the pulverized product stirring / heating means 30, which will be described later, is located downstream of the discharge port 13. The fixed amount feeding means 20 has a valve function and a metering function, and is arranged in the axial direction of the rotary shaft 21 as shown in FIG.
It has a gutter-shaped measuring mass 22 and a motor 25 for rotating the measuring mass 22. The motor 25 and the rotary shaft are connected to each other via an appropriate speed control mechanism 26.

【0012】前記計量マス22の送り出し側には、上方
に凸の断面形状を持つ案内板31が位置しており、該案
内板31は粉砕品攪拌・加熱手段30内に延出してい
る。すなわち、攪拌・加熱手段30は、図4に示すよう
に両側壁32、33と該側壁間に位置する円筒ケーシン
グ34とに囲まれた攪拌槽40を有し、一方の側壁33
には該攪拌槽40のほぼ中央部に開口する開口35が形
成されていて、案内板31は前記開口35を通り攪拌槽
40内に延出している。また、円筒ケーシング34は下
方に排出用開口36を持ち、該排出用開口36近傍には
シャッタ37が摺動自在に配置される。該シャッタ37
は側壁32に取り付けた適宜のシャッタ開閉機構38に
より開閉される。
A guide plate 31 having a convex cross-sectional shape is located on the delivery side of the weighing mass 22, and the guide plate 31 extends into the crushed product stirring / heating means 30. That is, the stirring / heating means 30 has a stirring tank 40 surrounded by both side walls 32 and 33 and a cylindrical casing 34 located between the side walls as shown in FIG.
An opening 35 is formed at the center of the stirring tank 40, and the guide plate 31 extends into the stirring tank 40 through the opening 35. Further, the cylindrical casing 34 has a discharge opening 36 below, and a shutter 37 is slidably arranged near the discharge opening 36. The shutter 37
Is opened and closed by an appropriate shutter opening / closing mechanism 38 attached to the side wall 32.

【0013】攪拌槽40内であって側壁32に近接した
位置には円筒ケーシング34の内径より幾分小径の円板
41設けられ、該円板41は側壁32に適宜の軸受けを
介して回転自在に支持された支軸42に固着されてい
る。そして、該支軸42は図示しない適宜の調速手段を
介してモータ43に接続している。さらに、前記円板4
1には、その外周縁近傍に2本及びそれより中心側寄り
に2本の攪拌棒44a、44b及び45a、45bがそ
れぞれ支軸42に対して対称位置に固着されており、各
攪拌棒は図1に示すように対向する側壁33近傍まで延
出している。一方、側壁33には内部に空間を持つ2本
の固定棒46a、46bが前記攪拌棒44と45の回転
軌跡の中間に位置するように固着されている。
A disc 41 having a diameter somewhat smaller than the inner diameter of the cylindrical casing 34 is provided in the stirring tank 40 at a position close to the side wall 32, and the disc 41 is rotatable on the side wall 32 via an appropriate bearing. It is fixed to a support shaft 42 supported by. Further, the support shaft 42 is connected to the motor 43 via an appropriate speed adjusting means (not shown). Further, the disc 4
In Fig. 1, two stirring rods 44a, 44b and 45a, 45b near the outer peripheral edge thereof and two stirring rods closer to the center side thereof are fixed at symmetrical positions with respect to the spindle 42, respectively. As shown in FIG. 1, it extends to the vicinity of the opposing side wall 33. On the other hand, two fixed rods 46a and 46b having a space inside are fixed to the side wall 33 so as to be positioned in the middle of the rotation loci of the stirring rods 44 and 45.

【0014】また、円筒ケーシング34の内周壁及び側
壁32、33の前記円筒ケーシング34により区画され
た壁面には平面ヒータ47が貼着されており、さらに、
前記固定棒46の内部空間には棒状ヒータ48(図1)
が挿入されていて、平面ヒータ47及び棒状ヒータ48
は図示しない電源部に適宜の回路を介して結線されてい
る。
A flat heater 47 is attached to the inner peripheral wall of the cylindrical casing 34 and the wall surfaces of the side walls 32 and 33 defined by the cylindrical casing 34.
A rod-shaped heater 48 (FIG. 1) is provided in the internal space of the fixing rod 46.
The flat heater 47 and the rod-shaped heater 48
Is connected to a power supply unit (not shown) through an appropriate circuit.

【0015】前記円筒ケーシング34に形成した排出用
開口36の下方には計量・搬出手段50が設けられる。
すなわち、前記排出用開口36の下方には案内用漏斗5
1、52が位置しており、該漏斗52の下方には計量ホ
ッパー53が適宜のロードセル54を介して側壁32、
33に支持されている。計量ホッパー53の排出口近傍
にはブロア55に接続したコンベア56が位置してい
る。上記案内漏斗51、52は円筒ケーシング34内の
処理物が計量ホッパー53に一度に纏まって落下しない
ようにする目的で設けられる。
Below the discharge opening 36 formed in the cylindrical casing 34, a measuring / carrying-out means 50 is provided.
That is, the guide funnel 5 is provided below the discharge opening 36.
1, 52 are located below the funnel 52, and a weighing hopper 53 is provided below the funnel 52 via an appropriate load cell 54 to form a side wall 32,
It is supported by 33. A conveyor 56 connected to the blower 55 is located near the discharge port of the weighing hopper 53. The guide funnels 51 and 52 are provided for the purpose of preventing the processed products in the cylindrical casing 34 from collectively dropping into the weighing hopper 53.

【0016】さらに、この装置はコントロールボックス
100を有し、ホッパー11に設けたレベルセンサ1
4、15、モータ25の調速機構26、モータ43の調
速手段、平面ヒータ47及び棒状ヒータ48の電源回
路、計量ホッパー53のロードセル54、及びブロア5
5の駆動回路等と電気的に接続していて、装置の運転制
御を司る。
Further, this apparatus has a control box 100 and a level sensor 1 provided in a hopper 11.
4, 15, the speed control mechanism 26 of the motor 25, the speed control means of the motor 43, the power supply circuit of the flat heater 47 and the rod-shaped heater 48, the load cell 54 of the weighing hopper 53, and the blower 5.
5 is electrically connected to the drive circuit of 5 and controls the operation of the apparatus.

【0017】次に、この装置の作動について説明する。
前記のように、集積された主として廃材である樹脂発泡
材は図示しない粉砕機により適宜の大きさに粉砕され、
ブロアにより投入口12からホッパー11内に供給され
る。供給された粉砕品のレベルが上方レベルセンサ15
により検知された場合には、ブロアの運転を止め供給を
停止する。ホッパー11内の粉砕品はモータ25の駆動
による前記計量マス22の回転により所定量計測され、
計量マス22の送り出し側から案内板31上に落下す
る。落下した粉砕品は側壁33に形成された開口35か
ら攪拌槽40内に送られ、案内板31の斜面に沿って徐
々に移動して、攪拌槽40に落下する。
Next, the operation of this device will be described.
As described above, the accumulated resin foam material, which is mainly waste material, is crushed to an appropriate size by a crusher (not shown),
It is supplied from the inlet 12 into the hopper 11 by a blower. The level of the crushed product supplied is the upper level sensor 15
If it is detected by, the operation of the blower is stopped and the supply is stopped. The crushed product in the hopper 11 is measured by a predetermined amount by the rotation of the measuring mass 22 driven by the motor 25,
It drops on the guide plate 31 from the delivery side of the weighing mass 22. The dropped pulverized product is sent into the stirring tank 40 through the opening 35 formed in the side wall 33, gradually moves along the slope of the guide plate 31, and drops into the stirring tank 40.

【0018】円筒ケーシング34の内周壁及び側壁3
2、33に貼着したヒータ47及び前記固定棒46に挿
入したヒータ48はこの時点で通電されており、該ヒー
タからの熱により攪拌槽40の内部空間は100℃〜2
00℃程度の加熱雰囲気となっている。その状態でモー
タ43の駆動により回転円板41を回動する。それによ
り、投入された樹脂発泡材の粉砕品は攪拌棒44、45
と固定棒46との相互作用によりほぼ均質的に攪拌を受
けると同時に、加熱される。この加熱雰囲気下での攪拌
により粉砕品は部分的その表面から熱収縮を受ける。同
時に、前記した粉砕時に発生した気泡が破壊して薄膜状
となったものあるいは長繊維状となりわた状に集合した
もの等の浮遊物も熱収縮して塊状となる。
Inner peripheral wall and side wall 3 of the cylindrical casing 34
The heater 47 attached to Nos. 2 and 33 and the heater 48 inserted into the fixing rod 46 are energized at this time, and the internal space of the stirring tank 40 is 100 ° C. to 2 ° C. due to the heat from the heater.
The heating atmosphere is about 00 ° C. In this state, the rotating disc 41 is rotated by driving the motor 43. As a result, the crushed product of the resin foam material put in is stirred by the stirring rods 44, 45.
And the fixing rod 46 interacts with each other, so that they are substantially homogeneously stirred and simultaneously heated. Due to the stirring under this heating atmosphere, the ground product is partially subjected to heat shrinkage from its surface. At the same time, suspended matter such as thin film-like ones formed by crushing the bubbles generated during the above-described pulverization or long-fiber-like ones gathered in a cross-linking state is also heat-contracted and becomes lump-like.

【0019】この加熱雰囲気下での攪拌処理を所定時間
行った後に前記シャッタ37を開き処理物を案内漏斗5
1、52を介して計量ホッパー53に移送する。計量ホ
ッパー53においてロードセル54により処理物の嵩密
度が計測され、計測値はコントロールボックス100に
送られる。計量後の処理物は計量ホッパー53からコン
ベア56に移され、ブロアー55から装置外の適宜の処
理物回収箇所に移送される。その後、必要時に新規材料
と混合されて樹脂発泡製品となる。
After the stirring process in this heating atmosphere is performed for a predetermined time, the shutter 37 is opened to guide the processed product to the funnel 5.
It is transferred to the weighing hopper 53 via 1, 52. In the weighing hopper 53, the bulk density of the processed material is measured by the load cell 54, and the measured value is sent to the control box 100. The processed products after the weighing are transferred from the weighing hopper 53 to the conveyor 56, and transferred from the blower 55 to an appropriate processed product collecting location outside the apparatus. After that, when necessary, it is mixed with a new material to form a resin foam product.

【0020】計測値と初期値との間にずれがある場合に
はその偏差を是正する制御を行う。偏差分を是正する方
法は種々存在する。例えば、是正信号をコントロールボ
ックス100からヒータ47、48の温度制御機構に送
り円筒ケーシング34内の温度を高くあるいは低くする
ことにより行ってもよく、あるいはシャッタ37の制御
機構に送りの温度は変えずに攪拌時間を長くあるいは短
くすることによってもよい。さらには、モータ43の回
転速度を制御することにより調整することも可能であ
る。また、上記の各手段を組み合わせて制御してもよ
い。
If there is a deviation between the measured value and the initial value, control is performed to correct the deviation. There are various methods for correcting the deviation. For example, a correction signal may be sent from the control box 100 to the temperature control mechanism of the heaters 47 and 48 to raise or lower the temperature inside the cylindrical casing 34, or the temperature of the feed to the control mechanism of the shutter 37 may not be changed. Alternatively, the stirring time may be lengthened or shortened. Furthermore, it is also possible to make adjustment by controlling the rotation speed of the motor 43. Moreover, you may control by combining each said means.

【0021】特に図示しないが、ブロアー55の吹き出
し口に流路切替え弁を設け、嵩密度が所定値以下のもの
についてその処理物をホッパー11に返送するための返
送路を形成することもできる。処理が進行することによ
り、ホッパー11内の粉砕品のレベルが低下する。下方
センサ14が粉砕品のレベルを検知したときには粉砕機
を作動させてホッパー11内に粉砕品を供給する。
Although not shown in the drawing, a flow path switching valve may be provided at the blow-out port of the blower 55 to form a return path for returning the processed material having a bulk density of a predetermined value or less to the hopper 11. As the treatment progresses, the level of the crushed product in the hopper 11 decreases. When the lower sensor 14 detects the level of the crushed product, the crusher is operated to supply the crushed product into the hopper 11.

【0022】以下、この運転はコントロールボックス1
00からの指令に基づいて繰り返し行われる。この処理
により粉砕された樹脂発泡材は所望の嵩密度に調整され
る。なお、運転の途中に設定嵩比重値を変更することも
可能であることは容易に理解されよう。上記の説明は本
発明の方法及び装置の一実施例の説明にすぎず、他に多
くの変形例が存在する。
Hereinafter, this operation is performed in the control box 1
It is repeatedly performed based on the command from 00. The resin foam material pulverized by this treatment is adjusted to a desired bulk density. It will be easily understood that the set bulk specific gravity value can be changed during the operation. The above description is only one description of one embodiment of the method and apparatus of the present invention, and there are many other variations.

【0023】例えば、ホッパー11に設けるレベルセン
サの形式は任意でありさらにレベルセンサを設けること
自体も任意である。ホッパー11の出口側に設ける定量
送り手段も所定量を繰り返し供給できるものであれば任
意のものを用いることができる。例えは、一定時間間隔
で開閉するシャッタ板による供給手段であってもよい。
上方に凸の断面形状を持つ案内板31は粉砕品が急激に
塊状となって円筒ケーシング内に投入されるのを阻止す
る目的で設けられるが、前記ホッパー11の出口側に設
ける定量送り手段が例えば少量の単位で多数回供給する
ような形態のものの場合には、単に平板状の案内板であ
ってもよい。
For example, the type of level sensor provided in the hopper 11 is arbitrary, and the level sensor itself may be provided. As the fixed amount feeding means provided on the outlet side of the hopper 11, any means can be used as long as it can repeatedly supply a predetermined amount. For example, the supply means may be a shutter plate that opens and closes at regular time intervals.
The guide plate 31 having an upwardly convex cross-sectional shape is provided for the purpose of preventing the crushed product from suddenly forming a lump into the cylindrical casing, and a fixed amount feeding means provided on the outlet side of the hopper 11 is provided. For example, in the case of a form in which a small number of units are supplied multiple times, a flat guide plate may be used.

【0024】攪拌棒及び固定棒の本数及び装着位置も任
意であり、粉砕品のより均一な攪拌が得られるように実
験的に適宜決定すればよい。その形状も図示のように円
筒型の棒状体である必要はなく、矩形や長円形であって
よい。さらに、円筒ケーシング内を加熱雰囲気にするた
めの平面及び棒状ヒータも加熱手段の例示として示され
るものであり、他に乾燥又は加湿の高温空気を送給する
ことによってもよく、攪拌時に生じる粉砕品同志のある
いは攪拌棒と粉砕品との摩擦熱によってもよい。また、
それらを適宜組み合わせて用いることもできる。特に、
平面ヒータ47については、円筒ケーシング34及び側
壁32、33の外側壁部に取りつけることもでき、内外
両側に取りつけることもできる。計量ホッパーでの嵩密
度の測定手段も任意であり、従来公知の嵩密度測定法を
適宜用いうる。このような樹脂発泡材の粉砕品の場合に
は光透過量の測定による嵩密度測定法も有効に用いう
る。
The number of stirring rods and fixed rods and their mounting positions are also arbitrary, and may be appropriately determined experimentally so as to obtain more uniform stirring of the crushed product. The shape does not have to be a cylindrical rod-shaped body as shown in the figure, and may be rectangular or oval. Furthermore, flat and rod-shaped heaters for creating a heating atmosphere in the cylindrical casing are also shown as examples of the heating means, and it is also possible to feed dry or humidified high temperature air to the crushed product, which is generated during stirring. The frictional heat between the same or the stirring rod and the crushed product may be used. Also,
It is also possible to use them in appropriate combination. In particular,
The flat heater 47 can be attached to the cylindrical casing 34 and the outer side wall portions of the side walls 32 and 33, or can be attached to both inner and outer sides. Any means for measuring the bulk density with a weighing hopper can be used, and a conventionally known bulk density measuring method can be appropriately used. In the case of a crushed product of such a resin foam material, a bulk density measuring method by measuring the amount of light transmission can be effectively used.

【0025】〔使用例〕廃材発泡スチロールを粉砕機で
平均粒径3mmとなるように粉砕し、その嵩密度を測定
したところ、約0.01g/ccであった。図示の装置
にその粉砕品を投入し、円筒ケーシング内の温度を15
0℃として5分間攪拌した。攪拌処理品を計量ホッパー
において嵩密度を測定したところ、約0.02g/cc
とすることができた。さらに5分間攪拌を継続して嵩密
度を測定したところ、約0.12g/ccとすることが
できた。
[Example of use] Styrofoam waste material was pulverized with a pulverizer to an average particle size of 3 mm, and its bulk density was measured to be about 0.01 g / cc. The crushed product is put into the apparatus shown in the drawing and the temperature in the cylindrical casing is adjusted to 15
The mixture was stirred at 0 ° C for 5 minutes. When the bulk density of the agitated product was measured with a weighing hopper, it was about 0.02 g / cc.
I was able to When the bulk density was measured by continuing stirring for further 5 minutes, it could be about 0.12 g / cc.

【0026】[0026]

【発明の効果】本発明によれば、粉砕機で粉砕処理した
樹脂発泡体粉砕品の嵩比重を容易に所望の値に調整する
ことができる。また、比重の異なった粉砕物の混合体を
処理する場合には最終的に均一な嵩密度のものに調整す
ることができる。それにより、本発明による処理済の再
利用発泡材と新規発泡材料とを混合した製品を成形する
際の重量管理を確実に行うことが可能となる。また、粉
砕品に含まれる計量な浮遊物を粒状化することもできる
ので、長期間にわたり成形を行っても成形機の蒸気供給
口に目詰まりが生じることもない。
According to the present invention, it is possible to easily adjust the bulk specific gravity of a resin foam pulverized product pulverized by a pulverizer to a desired value. Further, when treating a mixture of pulverized products having different specific gravities, it is possible to finally adjust the mixture to have a uniform bulk density. As a result, it becomes possible to reliably perform weight control when molding a product in which the recycled foam material treated according to the present invention and the novel foam material are mixed. Further, since it is possible to granulate a metered amount of suspended matter contained in the crushed product, the steam supply port of the molding machine will not be clogged even if molding is performed for a long period of time.

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

【図1】本発明による処理装置の断面図。1 is a cross-sectional view of a processing apparatus according to the present invention.

【図2】定量送り手段の一例を示す図。FIG. 2 is a diagram showing an example of a fixed amount feeding means.

【図3】図1の III-III線による断面図。FIG. 3 is a sectional view taken along line III-III in FIG.

【図4】攪拌槽を説明するための一部破断斜視図。FIG. 4 is a partially cutaway perspective view for explaining a stirring tank.

【符号の説明】[Explanation of symbols]

11…ホッパー、20…発泡樹脂粉砕品の定量供給手
段、40…攪拌槽、44、45…攪拌棒、46…固定
棒、47、48…ヒータ、53…計量ホッパー、54…
ロードセル
11 ... Hopper, 20 ... Fixed amount supply means of crushed foamed resin product, 40 ... Stirring tank, 44, 45 ... Stirring rod, 46 ... Fixed rod, 47, 48 ... Heater, 53 ... Measuring hopper, 54 ...
Load cell

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 所定量の発泡樹脂粉砕品を所定の加熱条
件下で所要時間攪拌し、その間に発泡樹脂粉砕品を部分
的に熱収縮させることにより、全体の嵩密度を調整する
ことを特徴とする発泡樹脂粉砕品の嵩密度調整方法。
1. The entire bulk density is adjusted by stirring a predetermined amount of the foamed resin pulverized product under a predetermined heating condition for a required time, and partially shrinking the foamed resin pulverized product during the stirring. A method for adjusting the bulk density of a foamed resin pulverized product.
【請求項2】 所定の加熱条件下で所定時間攪拌を受け
た発泡樹脂粉砕品の一部を取り出してその嵩密度を測定
し、その測定値に基づき加熱条件及び/又は攪拌時間を
調整する工程をさらに有していることを特徴とする請求
項1記載の発泡樹脂粉砕品の嵩密度調整方法。
2. A step of taking out a part of a foamed resin pulverized product which has been stirred for a predetermined time under a predetermined heating condition, measuring the bulk density thereof, and adjusting the heating condition and / or the stirring time based on the measured value. The method for adjusting the bulk density of a crushed foamed resin product according to claim 1, further comprising:
【請求項3】 発泡樹脂粉砕品の定量供給手段、該定量
供給手段からの発泡樹脂粉砕品を受け入れかつ攪拌する
攪拌槽、該攪拌槽内の発泡樹脂粉砕品を攪拌するための
攪拌手段、該攪拌槽内の発泡樹脂粉砕品を加熱するため
の加熱手段、及び攪拌及び加熱を受けた発泡樹脂粉砕品
を計量するための計量手段、とを有することを特徴とす
る発泡樹脂粉砕品の嵩密度調整装置。
3. A fixed amount supply means for the foamed resin crushed product, a stirring tank for receiving and stirring the foamed resin crushed product from the fixed amount supply means, a stirring means for stirring the foamed resin crushed product in the stirring tank, A bulk density of the crushed foamed resin product, comprising: a heating means for heating the crushed foamed resin product in the stirring tank, and a measuring means for measuring the crushed foamed resin product which has been stirred and heated. Adjustment device.
JP5578493A 1993-03-16 1993-03-16 Method and apparatus for adjusting bulk density of pulverized foamed resin Expired - Lifetime JP2840518B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5578493A JP2840518B2 (en) 1993-03-16 1993-03-16 Method and apparatus for adjusting bulk density of pulverized foamed resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5578493A JP2840518B2 (en) 1993-03-16 1993-03-16 Method and apparatus for adjusting bulk density of pulverized foamed resin

Publications (2)

Publication Number Publication Date
JPH06262625A true JPH06262625A (en) 1994-09-20
JP2840518B2 JP2840518B2 (en) 1998-12-24

Family

ID=13008532

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5578493A Expired - Lifetime JP2840518B2 (en) 1993-03-16 1993-03-16 Method and apparatus for adjusting bulk density of pulverized foamed resin

Country Status (1)

Country Link
JP (1) JP2840518B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106284359A (en) * 2016-10-15 2017-01-04 中国铁道科学研究院铁道建筑研究所 A kind of railway pneumatic mortar machine feeding system
WO2017028987A1 (en) * 2015-08-19 2017-02-23 Krones Ag Recycling system and method for processing bulk material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017028987A1 (en) * 2015-08-19 2017-02-23 Krones Ag Recycling system and method for processing bulk material
CN106284359A (en) * 2016-10-15 2017-01-04 中国铁道科学研究院铁道建筑研究所 A kind of railway pneumatic mortar machine feeding system

Also Published As

Publication number Publication date
JP2840518B2 (en) 1998-12-24

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