JPS6348693B2 - - Google Patents
Info
- Publication number
- JPS6348693B2 JPS6348693B2 JP57120117A JP12011782A JPS6348693B2 JP S6348693 B2 JPS6348693 B2 JP S6348693B2 JP 57120117 A JP57120117 A JP 57120117A JP 12011782 A JP12011782 A JP 12011782A JP S6348693 B2 JPS6348693 B2 JP S6348693B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- partition wall
- cylinder
- temperature
- foam
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/32—Mixing; Kneading continuous, with mechanical mixing or kneading devices with non-movable mixing or kneading devices
- B29B7/325—Static mixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/432—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
- B01F25/4322—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa essentially composed of stacks of sheets, e.g. corrugated sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/7404—Mixing devices specially adapted for foamable substances
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/36—Feeding the material to be shaped
- B29C44/46—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
- B29C44/50—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length using pressure difference, e.g. by extrusion or by spraying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/07—Flat, e.g. panels
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/362—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using static mixing devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/36—Feeding the material to be shaped
- B29C44/46—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
- B29C44/468—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length in a plurality of parallel streams which unite during the foaming
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2101/00—Use of unspecified macromolecular compounds as moulding material
- B29K2101/12—Thermoplastic materials
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Molding Of Porous Articles (AREA)
Description
【発明の詳細な説明】
この発明は、合成樹脂発泡体に模様、とくに雲
形又は大理石模様を表わす方法に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a pattern, particularly a cloud or marble pattern, on a synthetic resin foam.
合成樹脂発泡体は押出発泡によつて作られるこ
とが多い。押出発泡では、押出機内で熱可塑性樹
脂を溶融するとともに混練し、発泡剤を含有する
樹脂溶融物を作り、溶融した樹脂をそのまま口金
に導いて口金から押出し、発泡させることを骨子
とする。この方法では、専ら均一な発泡体を作る
ことが志向され、そのために均一な樹脂溶融物を
作ることにのみ注意が払われた。 Synthetic resin foams are often made by extrusion foaming. In extrusion foaming, thermoplastic resin is melted and kneaded in an extruder to create a resin melt containing a foaming agent, and the molten resin is directly introduced into a die and extruded from the die to cause foaming. In this method, the aim was exclusively to produce a homogeneous foam, and therefore only attention was paid to producing a homogeneous resin melt.
発泡体の成形において、均一な樹脂溶融物を作
るためには、樹脂を高温に加熱しよく溶融するこ
とが必要である。ところが、樹脂を口金内に導
き、成形して一定の形を保持させるには、僅かに
軟化している程度に保持することが必要である。
このため、押出発泡では口金に導く前に、高温に
加熱した樹脂を押出機先端部又は押出機と口金と
の間の樹脂通路内で冷却することが行なわれた。
また、このための樹脂の冷却装置も提案された。
このような冷却に際しても、従来は、樹脂を一様
に冷却して、均一な樹脂溶融物とすることだけに
注意が払われた。 In molding a foam, in order to make a uniform resin melt, it is necessary to heat the resin to a high temperature and melt it well. However, in order to guide the resin into the mouthpiece, mold it, and maintain a certain shape, it is necessary to maintain the resin at a slightly softened level.
For this reason, in extrusion foaming, resin heated to a high temperature is cooled at the tip of the extruder or in a resin passage between the extruder and the die before being introduced into the die.
A resin cooling device for this purpose has also been proposed.
Conventionally, even during such cooling, attention has been paid only to uniformly cooling the resin to form a uniform resin melt.
この発明者は、押出機内で一旦高温の発泡性溶
融物を作つたのち、これを冷却する際に故意に溶
融物中に部分的な温度差を与えて、その後口金か
ら押出すことを試みた。そのために、この発明者
は、押出機と口金との間に円筒状の樹脂通路を設
け、この筒を外部より空気を吹き付けて強制冷却
し、筒内を流れる溶融樹脂の温度を円形断面にお
ける外周部ほど低く中心部ほど高くして、これを
口金から押出した。こうして得られた発泡成形体
では、断面において外側に形成された気泡の径が
小さく、内部に形成された気泡の径が大きく、そ
の差が顕著であつた。 This inventor first created a high-temperature foamable melt in an extruder, then intentionally created a partial temperature difference in the melt when cooling it, and then tried to extrude it from a die. . To this end, the inventor provided a cylindrical resin passage between the extruder and the die, forcedly cooled the cylinder by blowing air from the outside, and controlled the temperature of the molten resin flowing inside the cylinder around the outer circumference of the circular cross section. I made it lower in the lower part and higher in the center, and pushed it out of the mouthpiece. In the foamed molded article thus obtained, in the cross section, the diameter of the bubbles formed on the outside was small, and the diameter of the bubbles formed inside was large, and the difference was remarkable.
次に、この発明者は、上記装置に加えて、筒内
の先端部に押出方向に対して斜めに延びる隔壁を
付設し、外がわにある比較的低温度の溶融物を斜
めに交差して進行させ、低温溶融物を内がわに塊
として散在させるようにして、これを押出した。
その結果、この発明者は、低温度の溶融物の存在
する部分が微小気泡の集団となり、その他の部分
が粗大気泡の集団となり、ここに特異な模様の表
われることを見出した。また、上述の隔壁を適当
に存在させると、低温部分が適度に分散し、ここ
に雲形又は大理石模様の表われることを見出し
た。 Next, in addition to the above device, the inventor added a partition wall extending obliquely to the extrusion direction at the tip of the cylinder, so that the relatively low temperature molten material on the outside was diagonally crossed. This was extruded with the low-temperature melt being scattered inside as lumps.
As a result, the inventor found that the part where the low-temperature melt existed became a group of microbubbles, and the other part became a group of coarse bubbles, and a unique pattern appeared here. It has also been found that when the above-mentioned partition walls are appropriately present, the low-temperature portions are appropriately dispersed, and a cloud shape or a marble pattern appears there.
筒内に斜めに延びる隔壁を付設し、隔壁によつ
て流動物を分割するとともに、分割された流動物
部分を異なる方向に進行させ、その後これを集め
る機構のものは、錯綜混合機(又は静止混合機)
として知られている。錯綜混合機は、均一な組成
物を作るのに用いられる。そのために、錯綜混合
機では、上述の隔壁を筒内の長い距離にわたつて
付設し、また隔壁を途中で切断し、切断個所で隔
壁が複雑に交錯し、流動物をジグザグに進行させ
ることを必要としている。 A type of mixed mixer (or static mixer) has a partition wall that extends diagonally inside the cylinder, divides the fluid by the partition wall, causes the divided fluid parts to proceed in different directions, and then collects them. mixer)
known as. A complex mixer is used to create a homogeneous composition. To achieve this, in a complex mixer, the above-mentioned partition walls are attached over a long distance inside the cylinder, and the partition walls are cut in the middle, so that the partition walls intersect in a complicated manner at the cut point, and the fluid moves in a zigzag pattern. In need of.
ところが、隔壁を筒内の短かい距離のところだ
けに付設し、また流動物を単純に斜めに進行させ
るだけのときには、充分な混合は行なわれない。
とくに、溶融樹脂のような粘度が高く、僅かな温
度差を持つに過ぎないものを短かい斜めの隔壁の
間に通すときには、却つてそこに不均一な組成を
生じ、温度差のある部分がところどころに塊とな
つて存在するに至る、という意外な結果の得られ
ることがわかつた。この発明は、このような知見
に基づいてなされたものである。 However, when the partition wall is attached only at a short distance within the cylinder and the fluid is simply allowed to advance diagonally, sufficient mixing is not achieved.
In particular, when something with high viscosity and only a small temperature difference, such as molten resin, is passed between short diagonal partition walls, an uneven composition is created there, and areas with temperature differences are It was found that the unexpected result was that the particles were present in clusters here and there. This invention was made based on such knowledge.
この発明は、押出機内で、熱可塑性樹脂を溶融
するとともに混練して発泡剤を含有する溶融樹脂
を作り、これを外側から冷却された樹脂通路に通
し、その後樹脂通路に対して斜めに延びる隔壁に
より溶融樹脂を分割し、分割された樹脂部分を互
いに異なる方向に進行させ、その後樹脂部分を集
合させ、溶融樹脂全体中に温度の異なる部分を局
部的に存在させ、この状態で樹脂を口金に導き、
口金から押出し発泡させることを特徴とする、合
成樹脂発泡体に模様を表わす方法に関するもので
ある。 This invention involves melting and kneading thermoplastic resin in an extruder to create a molten resin containing a blowing agent, passing this from the outside through a cooled resin passage, and then inserting a partition wall extending diagonally to the resin passage. The molten resin is divided by the molten resin, the divided resin parts are made to proceed in different directions, and then the resin parts are brought together, and parts with different temperatures are locally present in the whole molten resin, and in this state, the resin is transferred to the base. guidance,
The present invention relates to a method of expressing a pattern on a synthetic resin foam, which is characterized by extrusion and foaming from a die.
この発明は、溶融樹脂全体中に温度の異なる部
分を局部的に存在させることを骨子とする。その
ために、この発明は、発泡剤含有の溶融樹脂を外
がわから冷却して樹脂の内外に温度差を生じさ
せ、その後樹脂通路に対して斜めに延びる隔壁を
設け、この隔壁により溶融樹脂を分割し、分割さ
れた樹脂部分を互いに異なる方向に進行させたの
ち、これら樹脂部分を集合させる、という手段を
用いる。従つて、この発明は、特定の装置を用い
ることを必要としている。そこで、まず、この発
明方法で用いられる装置の説明から始める。 The gist of this invention is to locally create portions with different temperatures throughout the molten resin. To this end, this invention cools the molten resin containing a foaming agent from the outside to create a temperature difference between the inside and outside of the resin, and then provides a partition wall that extends obliquely to the resin passage, and divides the molten resin by this partition wall. However, a method is used in which the divided resin parts are advanced in different directions and then brought together. Therefore, the invention requires the use of specific equipment. First, we will begin with a description of the apparatus used in the method of this invention.
図面中、第1図は、この発明方法で用いられる
装置の一部切欠縦断面図である。第2図は、この
発明方法で用いられる隔壁構成用材料の一例を示
している。第3図は、この発明方法で用いられる
他の隔壁構成用材料を示している。第4図は、こ
の発明方法で用いられるさらに別の隔壁構成用材
料である。 In the drawings, FIG. 1 is a partially cut away longitudinal sectional view of the apparatus used in the method of the present invention. FIG. 2 shows an example of the material for forming partition walls used in the method of the present invention. FIG. 3 shows other materials for constructing partition walls that can be used in the method of this invention. FIG. 4 shows yet another partition wall construction material used in the method of the present invention.
第1図において、1は押出機、2はスクリユ、
3はブレーカープレート、4は筒、5は隔壁、6
は口金、7は成形枠である。押出機1は、バレル
内にスクリユ2を回転可能に付設し、その先にブ
レーカープレート3を付設し、さらにその先に筒
4を付設したものである。筒4は樹脂通路を形成
している。筒4は少なくとも押出機がわの部分が
外がわから冷却され、口金がわの内部に隔壁5が
固定され、その先に口金6が付設されている。 In FIG. 1, 1 is an extruder, 2 is a screw,
3 is a breaker plate, 4 is a cylinder, 5 is a partition wall, 6
7 is a base, and 7 is a molding frame. The extruder 1 has a screw 2 rotatably attached within a barrel, a breaker plate 3 attached to the tip thereof, and a cylinder 4 further attached to the tip of the screw 2. The cylinder 4 forms a resin passage. At least the extruder side of the tube 4 is cooled from the outside, a partition wall 5 is fixed inside the nozzle side, and a nozzle 6 is attached to the tip of the partition wall 5.
第1図の方法では、発泡性樹脂が押出機1内で
加熱により溶融されるとともに、スクリユにより
混練され、ブレーカープレート3を通り、筒4内
に入つてまず外がわから冷却され次いで隔壁5に
よつて分割される。隔壁5内では、分割された樹
脂が異なつた方向に進行せしめられる。隔壁5を
通つたのちに樹脂は、口金6内で集合され、口金
6から押出されて発泡し、成形枠7により形を整
えられて、発泡体8となる。 In the method shown in FIG. 1, the foamable resin is melted by heating in an extruder 1, kneaded by a screw, passes through a breaker plate 3, enters a cylinder 4, is first cooled on the outside, and then passes through a partition wall 5. It is divided accordingly. Inside the partition wall 5, the divided resin is made to advance in different directions. After passing through the partition wall 5, the resin is collected in a die 6, extruded from the die 6, foamed, and shaped by a molding frame 7 to form a foamed body 8.
隔壁5としては、隔壁を集合体として構成され
たもの、例えば第2図ないし第4図に示したもの
を用いるのが好都合である。このうち、第2図に
示したものは、多数の波板を集めたものであり、
第3図に示したものは、多数の小平板を交差させ
たものであり、第4図に示したものは、金属塊に
多数の孔を穿設したものである。これらの隔壁の
うち或るものは、既に述べたように、均一な組成
物を得るための混合機の要素として知られてい
る。 As the partition wall 5, it is convenient to use one constructed as an assembly of partition walls, such as those shown in FIGS. 2 to 4. Of these, the one shown in Figure 2 is a collection of many corrugated plates.
The one shown in FIG. 3 has a large number of small flat plates intersecting each other, and the one shown in FIG. 4 has a large number of holes drilled in a metal block. Some of these partitions, as already mentioned, are known as mixer elements for obtaining a homogeneous composition.
第2図の隔壁集合体51は、多数の金属製波板
511,512……………等を重ね合わせ、波板
中の屈曲部分が向きを異いて交差するように、波
板を互いに固定して作られたものである。具体的
には、例えば、波板511の谷及び峰の延びる方
向を矢印aの方向に向けて配置したとすると、そ
のすぐ下方に位置する金属製波板512は、その
谷及び峰の延びる方向が矢印bの方向に向くよう
にこれを配置し、それら波板の接触点を溶接して
交差状態に固定したものである。さらに、金属製
波板512のすぐ下方に位置する金属製波板52
3は、その谷及び峰の延びる方向が矢印aの方向
に向くように配置し、同様に溶接して傾斜隔壁の
集合体51としたものである。傾斜隔壁の集合体
51では、各波板の間に通路が形成されるが、そ
の通路は隣接するものの間で異なつた方向に向
き、また、通路の厚みが色々と変化するものとな
つている。 The bulkhead assembly 51 shown in Fig. 2 consists of a large number of corrugated metal sheets 511, 512, etc., which are stacked on top of each other, and the corrugated sheets are fixed to each other so that the bent portions of the corrugated sheets intersect with each other in different directions. It was made by Specifically, for example, if the corrugated sheet 511 is arranged with its valleys and peaks extending in the direction of arrow a, the metal corrugated sheet 512 located immediately below it will be arranged in the direction in which its valleys and peaks extend. The corrugated plates are arranged so that they face in the direction of arrow b, and the contact points of these corrugated plates are welded to fix them in a crossed state. Furthermore, a metal corrugated plate 52 located immediately below the metal corrugated plate 512
3 is arranged so that the extending direction of its valleys and peaks are in the direction of arrow a, and similarly welded to form an assembly 51 of inclined partition walls. In the assembly 51 of inclined partition walls, passages are formed between each corrugated plate, but the passages are oriented in different directions between adjacent corrugated plates, and the thickness of the passages varies in various ways.
この発明方法では、上述のような傾斜隔壁の集
合体51を筒4すなわち樹脂通路内に挿入しただ
けで、多数の隔壁を斜めに延びるように設けたも
のとすることができる。挿入に際しては、集合体
51を唯1個用いるだけでもよいが、少数、例え
ば2個又は3個の隔壁集合体51,52を直列に
挿入してもよい。 In the method of this invention, simply by inserting the above-mentioned inclined partition wall assembly 51 into the cylinder 4, that is, the resin passage, a large number of partition walls can be provided to extend diagonally. When inserting, only one assembly 51 may be used, but a small number, for example, two or three partition wall assemblies 51 and 52 may be inserted in series.
複数個の集合体51を用いる場合は、1個の集
合体では分散不充分なときであるから、複数個の
集合体51を並べるには、分散がさらに充分とな
るように配置することが好ましい。それには、1
つの集合体51における矢印aとbとに平行な平
面が、これに隣接する他の集合体52における矢
印aとbとに平行な平面と直交するように、2つ
の集合体を並べて連ね、両集合体51と52とに
おける波板の端同志を互いに交差する状態で接触
させ、接触点を溶接して、これら隔壁集合体を直
交状態に一体とする。同様にして、さらに別の集
合体を直交状態に接続する。集合体51又は52
を筒4内に挿入するには、第2図の矢印Xの方向
が筒4の軸線方向と一致するように向けて挿入す
る。 When using a plurality of aggregates 51, one aggregate is insufficient for dispersion, so it is preferable to arrange the plurality of aggregates 51 so that the dispersion is even more sufficient. . For that, 1
Two assemblies are arranged side by side and connected so that a plane parallel to arrows a and b in one assemblage 51 is orthogonal to a plane parallel to arrows a and b in another assemblage 52 adjacent thereto. The ends of the corrugated plates in the assemblies 51 and 52 are brought into contact with each other in a state of crossing each other, and the contact points are welded to integrate these partition wall assemblies in a perpendicular state. In the same way, further aggregates are connected in an orthogonal manner. Aggregate 51 or 52
In order to insert the tube into the tube 4, insert it so that the direction of the arrow X in FIG. 2 coincides with the axial direction of the tube 4.
こうして形成された筒4内では、小板511,
512……………等の峰又は谷の延びる方向a及
びbが、筒4の軸線方向Xに対して斜めに向つて
いる。しかも集合体51内には、小板511,5
12……………等によつて区画された多数の樹脂
通路が形成されている。その樹脂通路は、小板の
屈曲のために障害が多い。だから、集合体51中
を通る樹脂は乱流を形成することとなる。 Inside the cylinder 4 thus formed, the small plates 511,
The directions a and b in which the peaks or valleys such as 512, etc. extend are oblique to the axial direction X of the cylinder 4. Moreover, inside the assembly 51, there are small plates 511, 5.
A large number of resin passages partitioned by 12, etc. are formed. The resin passage is often obstructed due to bending of the platelets. Therefore, the resin passing through the aggregate 51 forms a turbulent flow.
第1図に示した装置は、上述のように構成され
ている。そこで、第1図について、この発明方法
を説明する。押出機1内では、発泡剤を含んだ熱
可塑性樹脂が、溶融された状態でブレーカープレ
ート3を通り、筒4の形成する樹脂通路内へ送り
込まれる。筒4に至るまでは、樹脂は発泡剤を一
様に含み、よく混練させて、全体がほぼ同じ温度
の組成物となつている。筒4は、その外面が大気
中に露出している。そのため、筒4内を通る間に
樹脂は、外がわ部分が内がわ部分よりも低温とな
る。このような樹脂を隔壁5中に通すと、樹脂は
隔壁によつて分割され、隔壁に沿つて斜めに進行
する。その結果、低温の樹脂が外がわから内がわ
に移り、ところどころに分散される。 The apparatus shown in FIG. 1 is constructed as described above. Therefore, the method of the invention will be explained with reference to FIG. Inside the extruder 1, a thermoplastic resin containing a foaming agent is fed in a molten state through a breaker plate 3 into a resin passage formed by a cylinder 4. Up to the cylinder 4, the resin uniformly contains the blowing agent and is thoroughly kneaded to form a composition having approximately the same temperature throughout. The outer surface of the tube 4 is exposed to the atmosphere. Therefore, while the resin passes through the tube 4, the outer part becomes lower in temperature than the inner part. When such resin is passed through the partition wall 5, the resin is divided by the partition wall and advances obliquely along the partition wall. As a result, the low-temperature resin moves from the outside to the inside and is dispersed here and there.
既述のように、集合体51を通る樹脂は乱流を
形成するから、樹脂は隔壁5中を通る間に混合さ
れる。この発明方法では、筒4の中を流れるもの
が粘稠な樹脂溶融物であり、また筒4の先端部の
短かい範囲内に隔壁5が設けられているに過ぎな
いから、上述の混合は全体を均一にするまでに至
らない。しかも筒4は大気に露出しているから、
樹脂は露出面から冷却される。従つて、隔壁5を
通る間に、樹脂はその中の低温部分を内部のとこ
ろどころに塊として分散させた状態となる。 As mentioned above, since the resin passing through the aggregate 51 forms a turbulent flow, the resins are mixed while passing through the partition wall 5. In the method of this invention, what flows through the cylinder 4 is a viscous molten resin, and since the partition wall 5 is only provided within a short range of the tip of the cylinder 4, the above-mentioned mixing is not possible. It is not possible to make the whole thing uniform. Moreover, since cylinder 4 is exposed to the atmosphere,
The resin is cooled from the exposed surface. Therefore, while passing through the partition wall 5, the resin becomes in a state in which the low-temperature portion thereof is dispersed as lumps here and there inside.
この発明方法において、筒4の中の先端部の短
かい範囲内に隔壁5を付設するとは、隔壁5の付
設された領域が、筒4の内径Dを基準として、筒
4の軸方向にDないし5×Dの長さの範囲内にわ
たつていることを意味している。 In the method of this invention, attaching the partition wall 5 within a short range of the tip of the cylinder 4 means that the area where the partition wall 5 is attached is D in the axial direction of the cylinder 4 with reference to the inner diameter D of the cylinder 4. This means that the length ranges from 5×D to 5×D.
隔壁5を出た樹脂は、次いで口金6に入る。こ
のとき、樹脂は、前述のように、低温樹脂が内部
のところどころに塊となつて散在している状態に
ある。従つて、口金6内では、低温樹脂の塊が、
そのまま散在した状態で断面形状が整えられるこ
とになる。形を整えられた樹脂は、口金6を出る
と同時に発泡するが、このとき成形枠7内にあつ
て、枠7により外形を規制される。発泡に際して
は、樹脂中に低温度の塊が散在するので、低温度
部分が小さな気泡を生成して、低倍率に発泡する
が、その余の高温度部分が大きな気泡を生成して
高倍率に発泡することとなる。 The resin exiting the partition wall 5 then enters the cap 6. At this time, as described above, the resin is in a state where the low-temperature resin is scattered here and there in the form of lumps. Therefore, inside the cap 6, the lump of low-temperature resin is
The cross-sectional shape will be arranged in a scattered state as it is. The shaped resin foams at the same time as it exits the cap 6, but at this time it is in a molding frame 7 and its outer shape is regulated by the frame 7. During foaming, low-temperature lumps are scattered in the resin, so the low-temperature parts generate small bubbles and foam at a low magnification, while the remaining high-temperature areas generate large bubbles and foam at a high magnification. This will result in foaming.
上述のようにして得られた発泡体は、高倍率に
発泡した部分と、低倍率に発泡した部分とが、混
在したものとなる。そこで、この発泡体を切断し
て見ると、切断面では低倍率部分が濃色となり、
高倍率部分が淡色となり、濃色と淡色とが不規則
に入り乱れて、恰かも雲形又は大理石のような模
様が表わされている。こうして、雲形又は大理石
のような模様を持つた樹脂発泡体が得られる。 The foam obtained as described above has a mixture of a portion foamed at a high magnification and a portion foamed at a low magnification. Therefore, when this foam is cut and viewed, the low magnification part of the cut surface is dark colored.
The high magnification area is light colored, and dark and light colors are mixed irregularly, creating a cloud-like or marble-like pattern. In this way, a resin foam with a cloud-shaped or marble-like pattern is obtained.
既に述べたように第2図の隔壁集合体51の代
わりに、第3図の隔壁集合体9を用いることがで
きる。第3図の隔壁9は、小平板の交差物91,
92及び93等が組み合わされて作られている。
詳しく云えば、一組の小平板911,912,9
13,914等が等しい間隔をおいて平行に並ん
で一平面上にあり、他の一組の小平板916,9
17,918,919等が等しい間隔をおいて、
平行に並んで別の平面にあり、後者の組が前者の
組の間に入つて交差部が溶接され、こうして小平
板の交差物91が構成される。同様にして、一組
の小板921,922,923等が等しい間隔を
おいて配置され、小板926,927,928等
と交差して交差物92が構成される。さらに同様
にして、交差物93が構成される。その上で、こ
れらの交差物91,92及び93がさらに交差さ
れ、例えば交差物92の小板926が交差物91
の小板911と912との間に入り込んで、その
接点が互いに溶接されて一体となり、集合体9を
構成する。この場合、各交差物の端が一直線上に
来るように、各交差物の配列に注意する。第3図
の集合体9では、小板911ないし928等の間
の隙間が樹脂通路を形成することになる。 As already mentioned, the partition wall assembly 9 of FIG. 3 can be used instead of the partition wall assembly 51 of FIG. 2. The partition wall 9 in FIG.
It is made by combining 92, 93, etc.
To be more specific, a set of small plates 911, 912, 9
13, 914, etc. are arranged in parallel at equal intervals on one plane, and another set of small plates 916, 9
17,918,919, etc. are equally spaced,
They are arranged in parallel in different planes, and the latter set is interposed between the former set and the intersections are welded, thus forming a small plate intersection 91. Similarly, a set of small plates 921, 922, 923, etc. are arranged at equal intervals and intersect with small plates 926, 927, 928, etc. to form an intersection 92. Furthermore, the crossing object 93 is constructed in the same manner. Thereupon, these intersecting objects 91, 92 and 93 are further intersected, for example, the platelet 926 of intersecting object 92 is intersected by intersecting object 91.
The contact points are welded together to form an assembly 9. In this case, pay attention to the arrangement of each intersection so that the ends of each intersection are in a straight line. In the assembly 9 of FIG. 3, the gaps between the small plates 911 to 928, etc., form resin passages.
この発明方法では、第3図に示した隔壁集合体
9を隔壁5の代わりに筒4の構成する樹脂通路の
中に挿入して、発泡体を作ることができる。この
とき、第3図の矢印Xの方向が、筒4の軸と一致
するように集合体9を位置させる。こうして、筒
4の中へ溶融樹脂を通すと、樹脂は小平板911
等により分割されるとともに誘導されて、筒4内
を斜めに進行する。小平板が交差して幾重にも存
在するから、樹脂は分割と斜めの進行と集合とを
繰り返すこととなる。しかも、外周の樹脂は冷却
されて低温にある。そのため、筒4の構成する樹
脂通路内を進行する間に、外周の低温樹脂が内部
へ移行せしめられ、内部に塊となつて散在するこ
ととなる。従つて、この樹脂を口金から押出すと
発泡し、さきに述べたと同様に、低発泡部分と高
発泡部分とが、不規則な模様となつて現れるよう
な発泡体が得られる。 In the method of this invention, a foam can be produced by inserting the partition wall assembly 9 shown in FIG. 3 into the resin passage constituted by the cylinder 4 instead of the partition wall 5. At this time, the assembly 9 is positioned so that the direction of the arrow X in FIG. 3 coincides with the axis of the cylinder 4. In this way, when the molten resin is passed into the cylinder 4, the resin is passed through the small flat plate 911.
etc., and are guided and advance diagonally inside the cylinder 4. Since the small plates intersect and exist in multiple layers, the resin repeats division, diagonal progression, and aggregation. Moreover, the resin on the outer periphery is cooled and at a low temperature. Therefore, while moving through the resin passage formed by the cylinder 4, the low-temperature resin on the outer periphery is transferred to the inside, and becomes scattered inside in the form of lumps. Therefore, when this resin is extruded from the die, it foams, and as described above, a foam is obtained in which low-foaming areas and high-foaming areas appear in an irregular pattern.
第4図の隔壁集合体100は、円柱状金属塊1
01に多数の貫通孔103ないし106を穿設し
たものである。貫通孔103ないし106は、何
れも金属塊101の円柱軸に対して斜めに向いて
いる。しかも、貫通孔103ないし106の円柱
軸に対する傾斜は、隣接する貫通孔の間で異なつ
ている。例えば、第4図のa図における断面cで
表わされる貫通孔103が、c図のように、上ほ
ど左へ傾く傾斜であれば、これに隣る断面bで表
わされる貫通孔104は、b図のように、上ほど
右へ傾く傾斜とする。従つて、樹脂がこれらの貫
通孔103ないし106に分かれて進み、貫通孔
を出たところで集合されると、外周にあつた樹脂
が分割されて斜めに移動し、中央部に来ることに
なり、逆に中央部にあつた樹脂が外周に来ること
になる。こうして、外周の低温樹脂が内部のとこ
ろどころに散在することになる。 The partition wall assembly 100 in FIG.
01 with a large number of through holes 103 to 106. The through holes 103 to 106 are all oriented obliquely to the cylindrical axis of the metal lump 101. Furthermore, the inclinations of the through holes 103 to 106 with respect to the cylinder axis differ between adjacent through holes. For example, if the through hole 103 represented by cross section c in Figure 4a is inclined to the left as it goes up as shown in Figure c, the adjacent through hole 104 represented by cross section b is As shown in the figure, the slope slopes to the right as it goes up. Therefore, when the resin is divided into these through-holes 103 to 106 and collected when it exits the through-holes, the resin that was on the outer periphery is divided and moves diagonally to come to the center. Conversely, the resin that was in the center will be on the outer periphery. In this way, the low-temperature resin on the outer periphery is scattered here and there inside.
なお、この発明方法では、隔壁集合体5の直前
にある溶融樹脂が、出来るだけ広い範囲の温度分
布を持つことが望ましい。なぜならば、高温部と
低温部との温度差が大きいほど、発泡体に顕著な
模様が表われるからである。したがつて、筒4は
大気中に露出させるだけでなく、ジヤケツト式に
し、水、油等の冷却媒体を通すのがよい。 In addition, in the method of this invention, it is desirable that the molten resin immediately before the partition wall assembly 5 has a temperature distribution in as wide a range as possible. This is because the larger the temperature difference between the high-temperature part and the low-temperature part, the more pronounced the pattern appears on the foam. Therefore, it is preferable that the cylinder 4 is not only exposed to the atmosphere, but also of a jacket type, and that a cooling medium such as water or oil is passed therethrough.
この発明方法によれば、内部に低い倍率に発泡
した部分を含み、低い倍率部分が高い倍率部分中
に不規則に分散している樹脂発泡体が容易に得ら
れる。そこで、この発泡体を切断して切断面を露
出させると、切断面は低い倍率部分が雲形又は大
理石様の特異な模様を表わすような樹脂発泡体が
得られる。その模様が美麗であるから、この発泡
体はこれを切断して断面を露出させ、外観が美麗
な発泡体として使用することができる。また、こ
の発泡体は断熱性にもすぐれているので、スライ
スして障子、襖等に使用すると、美麗で商品価値
の高いものが得られる。この点で、この発明方法
は実用上の効果が大きい。 According to the method of this invention, it is easy to obtain a resin foam that includes a foamed portion with a low magnification inside and in which the low magnification portion is irregularly dispersed in the high magnification portion. Therefore, when this foam is cut to expose the cut surface, a resin foam is obtained in which the cut surface exhibits a unique cloud-shaped or marble-like pattern in the lower magnification portion. Since the pattern is beautiful, this foam can be cut to expose the cross section and used as a foam with a beautiful appearance. In addition, this foam has excellent heat insulation properties, so when sliced and used for shoji screens, sliding doors, etc., beautiful products with high commercial value can be obtained. In this respect, the method of this invention has great practical effects.
次に実施例を挙げて、この発明方法の詳細を説
明する。 Next, the details of the method of this invention will be explained with reference to Examples.
実施例 1
この実施例では、第1図に示した実施態様で、
筒4としてジヤケツト式のもの、隔壁集合体とし
て第2図に示した構造のものを用いた。Example 1 In this example, in the embodiment shown in FIG.
A jacket type tube was used as the cylinder 4, and a structure shown in FIG. 2 was used as the partition wall assembly.
樹脂としてはポリスチレン樹脂を用い、樹脂
100重量部に対して0.5重量部の微粉末タルクを加
えよく混合したのち、この混合物を口径40mmと口
径50mmの二台が連結された押出機に、1時間当り
15Kgの割合で供給した。そして、口径40mmの押出
機途中より、樹脂に対して約15重量%割合でトリ
クロロモノフルオロメタンを供給し、均一に混合
して発泡性樹脂とした。 Polystyrene resin is used as the resin.
After adding 0.5 parts by weight of finely powdered talc to 100 parts by weight and mixing well, the mixture was transferred to an extruder with two connected units, one with a diameter of 40 mm and one with a diameter of 50 mm, for one hour.
It was supplied at a rate of 15Kg. Then, trichloromonofluoromethane was supplied from the middle of an extruder with a diameter of 40 mm at a ratio of about 15% by weight to the resin, and was uniformly mixed to obtain a foamable resin.
押出機先端に設けた筒4は内径が60mmφで、軸
方向に300mmの長さをもつものであり、その先端
部120mmの範囲に第2図に示した隔壁集合体51
及び同一構造の隔壁集合体52を直列に挿入し
た。この隔壁集合体51,52における波板51
1,512……………は、それぞれ1.5mm厚みの
もの7枚で構成され、両集合体の連結部は波板の
端同志が互いに交差する状態で接触し、接触点が
溶接され一体化したものであつた。次に口金6は
先端部の開口が厚み2mm、巾100mmの細狭通路を
持つものであり、成形枠7は口金の樹脂排出面に
接して、樹脂排出通路を囲み、開口が出口ほど広
がり、端部では厚み25mm、巾200mmの寸法となつ
たものであつた。また軸方向の長さは100mmであ
つた。 The cylinder 4 provided at the tip of the extruder has an inner diameter of 60 mmφ and a length of 300 mm in the axial direction, and a partition wall assembly 51 shown in FIG.
and partition wall assemblies 52 having the same structure were inserted in series. Corrugated plate 51 in this partition wall assembly 51, 52
1,512...... is composed of seven pieces each with a thickness of 1.5 mm, and the connecting part of both assemblies is in contact with the edges of the corrugated plates crossing each other, and the contact points are welded and integrated. It was something I did. Next, the cap 6 has an opening at the tip with a narrow passage having a thickness of 2 mm and a width of 100 mm, the molding frame 7 contacts the resin discharge surface of the cap, surrounds the resin discharge passage, and the opening widens toward the exit. The ends were 25 mm thick and 200 mm wide. Moreover, the length in the axial direction was 100 mm.
押出にあたつては、口径40mmの押出機の樹脂供
給部を170℃、溶融部を200℃、口径50mmの押出機
を100〜160℃にそれぞれ設定し、押出機より排出
された溶融樹脂を筒4に導き、この外側にあるジ
ヤケツト内に90℃の温調油を循環させ、筒4内に
設けた隔壁集合体51,52を通した後口金より
押出し、それに続く成形枠7内で発泡させ、外形
規制を行なつた。、その後、発泡体を引取機で連
続的に引取り、発泡成形体を得た。 For extrusion, the resin supply part of the extruder with a diameter of 40 mm was set at 170 °C, the melting part was set at 200 °C, and the extruder with a diameter of 50 mm was set at 100 to 160 °C, and the molten resin discharged from the extruder was The oil is guided into the cylinder 4, and a temperature-controlled oil of 90°C is circulated inside the jacket on the outside of the cylinder, passed through the partition wall assembly 51, 52 provided in the cylinder 4, and then extruded from the die, followed by foaming in the forming frame 7. The external shape was regulated. Thereafter, the foam was continuously taken off with a take-off machine to obtain a foamed molded article.
この発泡成形体は、密度0.07g/cm3で、最大厚
み40mm、最大巾240mmの偏平円断面を持ち、その
あらゆる角度からの切断面では微小気泡群と粗大
気泡群が入りまじり、あたかも大理石様の模様が
表われたものであつた。 This foamed molded product has a density of 0.07 g/ cm3 , a maximum thickness of 40 mm, and a maximum width of 240 mm, with an oblate circular cross section, and when viewed from all angles, micro bubbles and coarse bubbles are mixed together, making it look like marble. It was a reflection of the pattern.
第1図は、この発明方法の一実施態様を断面図
で示したものである。第2図及び第3図は、この
発明方法で用いられる隔壁の構成用材料を示した
斜視図である。第4図は、この発明方法で用いら
れる他の隔壁構成用材料を示した平面及び断面図
である。
FIG. 1 shows a cross-sectional view of one embodiment of the method of this invention. FIGS. 2 and 3 are perspective views showing materials for forming partition walls used in the method of the present invention. FIG. 4 is a plan view and a sectional view showing another partition wall forming material used in the method of the present invention.
Claims (1)
に混練して、発泡剤を含有する高温の溶融樹脂を
作り、これを外側から冷却された樹脂通路に通
し、その後樹脂通路に対して斜めに延びる隔壁に
より溶融樹脂を分割し、分割された樹脂部分を互
いに異なる方向に進行させ、その後樹脂部分を集
合させ、溶融樹脂全体中に温度の異なる部分を局
部的に存在させ、この状態で樹脂を口金に導き、
口金から押出し発泡させることを特徴とする、合
成樹脂発泡体に模様を表わす方法。1 In an extruder, a thermoplastic resin is melted and kneaded to create a high-temperature molten resin containing a blowing agent, which is passed through a cooled resin passage from the outside, and then a partition wall that extends obliquely to the resin passage. The molten resin is divided by the molten resin, the divided resin parts are made to proceed in different directions, and then the resin parts are brought together, and parts with different temperatures are locally present in the whole molten resin, and in this state, the resin is transferred to the base. guidance,
A method of expressing a pattern on a synthetic resin foam, which is characterized by extrusion and foaming from a die.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57120117A JPS5911226A (en) | 1982-07-09 | 1982-07-09 | Pattern expressing method of synthetic resin foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57120117A JPS5911226A (en) | 1982-07-09 | 1982-07-09 | Pattern expressing method of synthetic resin foam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5911226A JPS5911226A (en) | 1984-01-20 |
| JPS6348693B2 true JPS6348693B2 (en) | 1988-09-30 |
Family
ID=14778371
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57120117A Granted JPS5911226A (en) | 1982-07-09 | 1982-07-09 | Pattern expressing method of synthetic resin foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5911226A (en) |
-
1982
- 1982-07-09 JP JP57120117A patent/JPS5911226A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5911226A (en) | 1984-01-20 |
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