JPH11300739A - Granulating method and device - Google Patents

Granulating method and device

Info

Publication number
JPH11300739A
JPH11300739A JP10072035A JP7203598A JPH11300739A JP H11300739 A JPH11300739 A JP H11300739A JP 10072035 A JP10072035 A JP 10072035A JP 7203598 A JP7203598 A JP 7203598A JP H11300739 A JPH11300739 A JP H11300739A
Authority
JP
Japan
Prior art keywords
pellets
cutter
cooling water
die surface
die
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
JP10072035A
Other languages
Japanese (ja)
Other versions
JP3996695B2 (en
Inventor
Yukio Katsuki
幸雄 香月
Kazuhiko Yamamoto
山本  和彦
Tetsuji Umemoto
鉄司 梅本
Nobuo Matsubara
伸夫 松原
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.)
Mitsui Chemicals Inc
Original Assignee
Mitsui Chemicals Inc
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 Mitsui Chemicals Inc filed Critical Mitsui Chemicals Inc
Priority to JP07203598A priority Critical patent/JP3996695B2/en
Publication of JPH11300739A publication Critical patent/JPH11300739A/en
Application granted granted Critical
Publication of JP3996695B2 publication Critical patent/JP3996695B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/02Making granules by dividing preformed material
    • B29B9/06Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
    • B29B9/065Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion under-water, e.g. underwater pelletizers

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce the incidence of stuck-together pellts or grape-like pellets by a method wherein a melted resin film formed on a die surface is solidified by being sprayed with cooling water. SOLUTION: An annular plate 13 is fixed to the shaft supporting part 12 of a holder shaft 11. At both the sides of the plate, atomizing nozzles 14 are attached. Cooling water pipings 18 including a pump 15 or the like are connected to both the atomizing nozzles 14. Cooling water is atomized in mist against a die surface and cutters 5 from both the atomizing nozzles 14 so as to cool and solidify and peel off a melted resin film formed on the die surface. The stomizing angle is adjusted by changing the rotational frequency of the pump 15 and the pressure of cooling water. Cut pellets fall in the cooling water 2, which spirally runs on the peripheral surface of a cutter hood 1, and are cooled down and, at the same time, carried to an outlet 7. After that, the pellets are fed to an centrifugal drier and an automatic sifter so as to select single pellets, which are products, from stuck-together pellets and grape-like pellets. Thus, the incidence of stuck-together pellets or grape-like pellets an be reduced.

Description

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

【0001】[0001]

【発明が属する技術分野】本発明は、熱可塑性樹脂、と
くに例えばポリメチルペンテンのような高融点ポリオレ
フィンに好適な造粒方法及び装置に関し、とりわけ押出
機の先端に取付けたダイより押出される溶融樹脂をホッ
トカット方式で切断することよりなる造粒方法及び装置
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus suitable for granulating thermoplastic resins, especially high-melting polyolefins such as polymethylpentene, and more particularly to a method for extruding a melt extruded from a die attached to the tip of an extruder. The present invention relates to a method and an apparatus for granulating a resin by cutting a resin by a hot cut method.

【0002】[0002]

【従来技術】樹脂原料をペレット化する方法には、ダイ
より押出された溶融樹脂を空気中でカッティングして冷
却水中に落として冷却する空中ホットカット方式と、溶
融樹脂を水中に押出して、そのまゝ水中でカッティング
と同時に冷却してペレット化する水中カット方式とがあ
る。
2. Description of the Related Art A method of pelletizing a resin material includes an aerial hot-cut method in which a molten resin extruded from a die is cut in air and dropped in cooling water to be cooled, and a molten resin is extruded into water. Well, there is an underwater cutting method that cools and pelletizes at the same time as cutting in water.

【0003】図1は、空中ホットカット方式の一例を示
すもので、カッターフード1の内周面に冷却水を斜め接
線方向に噴出させて図の矢印方向に螺旋状に流れる水流
で水膜2を形成した状態で、モータ3より減速機を介し
て回転駆動されるホルダー4に放射状に取付けたカッタ
ー5を押出機先端に取付けたダイ6に押付けて、ダイ6
より押出される溶融樹脂をペレット状にカッティング
し、これを水膜中に落として冷却させながら螺旋状の水
流により出口7まで運んで排出させるようになってい
る。
FIG. 1 shows an example of an aerial hot-cut method, in which cooling water is jetted obliquely tangentially to the inner peripheral surface of a cutter hood 1 so that a water film 2 flows spirally in the direction of the arrow in FIG. Is formed, a cutter 5 radially attached to a holder 4 rotationally driven by a motor 3 via a speed reducer is pressed against a die 6 attached to the tip of the extruder.
The molten resin to be extruded is cut into pellets, dropped into a water film, cooled, transported to the outlet 7 by a spiral water flow, and discharged.

【0004】[0004]

【発明が解決しようとする課題】水中カット方式の場
合、樹脂の冷却によりダイの目詰まりを生じ易い。こと
に樹脂が高融点樹脂であると、冷却水と樹脂の温度差が
大きくなって樹脂の冷却による目詰まりを生じ易い。こ
れに対し、空中ホットカット方式では、高融点樹脂であ
ってもダイの目詰まりを生じにくい利点があるが、従来
のこの方式のものではペレット同志が互いに融着する互
着ペレットが発生し易く、単独のペレットができるよう
に切断するのは容易でなかった。そのためこの方式で
は、カッティングされたペレットを自動篩器に掛けて単
独のペレットを選別し、製品化しているが、互着ペレッ
トが多いために収率の低下を来していた。とくにメルト
フローレイト(以下、MFRという)の値が50以上で
ある粘度の低い樹脂については、互着ペレットやペレッ
トが2個以上だんご状に付着したグレープ状ペレットの
発生率が高く、低収率であった。ここで、MFRとは2
60℃で5kgの力を受けたときに直径2.1mm、長さ
8mmのオリフィスから10分間に押し出される樹脂の量
(g)であって、ASTM D1238に示される試験
方法によって測定される値である(但し測定温度は試験
方法にある230℃を260℃に変更)。
In the case of the underwater cutting method, clogging of the die tends to occur due to cooling of the resin. In particular, when the resin is a high melting point resin, the temperature difference between the cooling water and the resin becomes large, and the resin tends to be clogged by cooling. On the other hand, the aerial hot cut method has an advantage that clogging of the die does not easily occur even with a high melting point resin, but in this conventional method, cohesive pellets in which pellets are fused to each other are easily generated. However, it was not easy to cut so that a single pellet could be formed. Therefore, in this method, the cut pellets are passed through an automatic sieve to select individual pellets for commercialization, but the yield is reduced due to the large number of cohesive pellets. In particular, for a resin having a low melt flow rate (hereinafter, referred to as MFR) having a value of 50 or more, the occurrence rate of grape-like pellets in which two or more cohesive pellets or pellets are adhered in a dumpling form is high, and the yield is low. Met. Here, MFR is 2
The amount (g) of resin extruded from an orifice 2.1 mm in diameter and 8 mm in length when subjected to a force of 5 kg at 60 ° C. in 10 minutes, and is a value measured by a test method shown in ASTM D1238. (However, the measurement temperature was changed from 230 ° C in the test method to 260 ° C).

【0005】本発明は、互着ペレットやグレープ状ペレ
ットの発生率を低減させて製品(単独ペレット)の収率
改善及び自動篩器での篩上ペレット除去作業の軽減によ
る省力化を図ることを目的としてなされたものである。
The present invention aims to improve the yield of products (single pellets) by reducing the incidence of cohesive pellets and grape-like pellets, and to reduce labor for removing pellets on sieves with an automatic sieve. It was made for the purpose.

【0006】[0006]

【課題の解決手段】本発明者らは、上記の目的を達成す
るためカッター刃による切れ味をよくすることを考え、
切れ味を損ねる原因を考えた結果、その一つにダイ面に
形成される溶融樹脂膜の存在があり、これによりカッタ
ー刃とダイ面の密着性が損なわれていると判断した。そ
して本発明者らは、ダイ面に形成される樹脂膜を除去す
るために冷却水を掛けるか噴霧させて樹脂膜を固化し、
ダイ面より剥離させることを考え、実際に樹脂膜に冷却
水を噴霧させたところ、互着ペレットやグレープ状ペレ
ットの発生率を低減させることができ、MFRの値が5
0以上の樹脂については特に効果が大きいことを見出し
た。すなわち、本発明によれば、260℃でのMFRの
値が1〜500g/10分、好ましくは5〜300g/
10分の範囲にある樹脂の造粒法において、互着ペレッ
ト及びグレープ状ペレットよりなる篩を通過しないで篩
上に残ったペレット、すなわちペレット同志が複数個く
っついて団子状になったペレット(以下、便宜上これを
「篩上ペレット」と呼称する)の発生率を低減させるこ
とがでる。例えばMFRが5〜300g/10分の範囲
にあるポリメチルペンテンの場合には、篩上ペレットの
発生率が、従来5〜10重量%あったものが、20〜4
0℃の噴霧冷却水を掛けることにより0.1〜0.2重
量%と大幅に低減させることができた。
The present inventors have thought of improving the sharpness of a cutter blade in order to achieve the above object.
As a result of considering the cause of impairing the sharpness, it was determined that one of them was the presence of the molten resin film formed on the die surface, which caused the adhesion between the cutter blade and the die surface to be impaired. And the inventors solidified the resin film by spraying or spraying cooling water to remove the resin film formed on the die surface,
Considering separation from the die surface, when cooling water was actually sprayed on the resin film, the occurrence rate of cohesive pellets and grape-like pellets could be reduced, and the MFR value was 5%.
It has been found that the effect is particularly large for a resin of 0 or more. That is, according to the present invention, the MFR value at 260 ° C. is 1 to 500 g / 10 min, preferably 5 to 300 g / min.
In the resin granulation method in the range of 10 minutes, pellets remaining on the sieve without passing through the sieve composed of the cohesive pellets and the grape-like pellets, that is, pellets in which a plurality of pellets are stuck together to form a dumpling (hereinafter referred to as a pellet) , For convenience, this is referred to as “sieve pellets”). For example, in the case of polymethylpentene having an MFR in the range of 5 to 300 g / 10 minutes, the rate of generation of on-sieve pellets has conventionally been 5 to 10% by weight, but 20 to 4% by weight.
By applying the spray cooling water at 0 ° C., it was possible to greatly reduce the amount to 0.1 to 0.2% by weight.

【0007】本発明は、この知見に基づいてなされたも
ので、押出機先端に取付けたダイより押出された溶融樹
脂をダイ面を摺接しながら回転するカッターで切断して
ペレット化し、水中に落下させて冷却する空中ホットカ
ット方式による造粒方法において、ダイ面に形成される
溶融樹脂膜を固化するため冷却水を散布ないし噴霧させ
ることを特徴とする。
The present invention has been made based on this finding. The molten resin extruded from a die attached to the tip of an extruder is cut by a rotating cutter while sliding on the die surface, pelletized, and dropped into water. In the granulation method based on an aerial hot cut method in which cooling is performed, cooling water is sprayed or sprayed to solidify a molten resin film formed on a die surface.

【0008】別の発明は、上記方法を実施するための装
置に関するもので、押出機先端に取付けたダイと、モー
タを駆動源として回転駆動されるホルダーに放射状に取
付けられ、ダイのダイ面に押付けられた状態で回転する
カッターとからなり、ダイより押出される溶融樹脂をカ
ッターにより切断してペレット化し、水中に落下させて
冷却する空中ホットカット方式による造粒装置におい
て、ダイ面に形成される溶融樹脂膜を固化するため冷却
水を散布ないし噴霧させるノズルを含む装置を設けたこ
とを特徴とする。
Another aspect of the present invention relates to an apparatus for performing the above method, which is radially mounted on a die attached to a tip of an extruder and a holder which is driven to rotate by a motor as a driving source, and is mounted on a die surface of the die. It consists of a cutter that rotates in a pressed state, and the molten resin extruded from the die is cut by the cutter into pellets, dropped into water and cooled by an aerial hot cut granulator, which is formed on the die surface. And a device including a nozzle for spraying or spraying cooling water to solidify the molten resin film.

【0009】上記各発明は、熱可塑性樹脂一般に適用さ
れるが、なかでもMFRが5〜500の互着ペレットを
生じ易いポリオレフィン、とくにMFR値が50以上の
樹脂に好適で、こうした樹脂のものに対して、互着ペレ
ットやグレープ状ペレットの発生率を低減させるのに有
効である。上記各発明で用いるカッターとしては、例え
ば図2に示すような従来の薄刃のナイフ状カッター1
0、図3及び図4に示すように肉厚で剛性を有し、柄8
に周方向に位置調整可能に取着される鉈刃状カッター9
等を用いることができる。この中では、図3及び図4に
示すような鉈刃状カッターを使用するのが望ましい。こ
の理由は次の通りである。
The above-mentioned inventions are generally applied to thermoplastic resins, and are particularly suitable for polyolefins having an MFR of 5 to 500, which are liable to form cohesive pellets, especially resins having an MFR value of 50 or more. On the other hand, it is effective for reducing the incidence of cohesive pellets and grape-like pellets. As the cutter used in each of the above-mentioned inventions, for example, a conventional thin blade knife-shaped cutter 1 as shown in FIG.
0, as shown in FIG. 3 and FIG.
Cutter 9 attached so that its position can be adjusted in the circumferential direction
Etc. can be used. In this, it is desirable to use a hatchet-shaped cutter as shown in FIGS. The reason is as follows.

【0010】図2に示すようなナイフ状カッターの場
合、ダイ面との面圧を上げるためカッターホルダー4で
カッター10をダイ面に強く押付けると、カッター先端
が反ってダイ面より浮き易いこと、ダイ面との面圧を上
げると、刃が摩耗し易く、寿命が短いこと、刃の撓みが
大きいために初期に数時間の馴らし運転が必要であるこ
と等の難点があるのに対し、図3及び図4に示すような
鉈刃状カッターの場合、ダイ面との面圧を上げてもカッ
ターの撓みが小さく、刃全体をダイ面に密着させること
で、カッティング状態を良好に保つことができること、
図1に示すカッターに比べ寿命が長く、再研磨すること
により繰返して使用できること、馴らし運転を不要にで
きること等のためである。
In the case of a knife-shaped cutter as shown in FIG. 2, if the cutter 10 is strongly pressed against the die surface by the cutter holder 4 in order to increase the surface pressure with the die surface, the tip of the cutter warps and is more likely to float than the die surface. However, when the surface pressure with the die surface is increased, the blades are liable to be worn, the service life is short, and the bending of the blades is large, so that a few hours of initial running-in operation is required. In the case of a hatchet-shaped cutter as shown in FIGS. 3 and 4, even if the surface pressure with the die surface is increased, the deflection of the cutter is small, and the cutting state is kept good by bringing the entire blade into close contact with the die surface. Can do,
This is because the cutter has a longer service life than the cutter shown in FIG. 1, can be used repeatedly by regrinding, and can eliminate a running-in operation.

【0011】以上の点からカッターは、図3及び図4に
示すような鉈刃状カッターが望ましいが、このカッター
の場合でも次のような条件のカッターを使用するのが良
好なカッティング状態を得るうえでより望ましい。すな
わち、図3及び図4に示すように、ホルダー軸中心Oを
通る線と刃9aがなす角(本明細書では、これをカッタ
ーの取付角度という)θが25〜45°であり、図5に
示すすくい角αが40〜50°、逃げ角γが15〜20
°、刃先角βが25〜30°である。これらの条件のう
ち、すくい角αが大きい程図6に示すようにカッティン
グされたペレットが飛ぶ方向とダイ面とのなす角ψが大
きくなり、ダイ面より離れる方向に飛び易い。
From the above points, it is desirable that the cutter is a hatchet-shaped cutter as shown in FIGS. 3 and 4. Even in the case of this cutter, it is preferable to use a cutter under the following conditions to obtain a good cutting state. More desirable above. That is, as shown in FIGS. 3 and 4, the angle θ formed by a line passing through the holder axis center O and the blade 9 a (in this specification, this is referred to as a cutter mounting angle) is 25 to 45 °, and FIG. The rake angle α is 40 to 50 ° and the clearance angle γ is 15 to 20
° and the cutting edge angle β are 25 to 30 °. Of these conditions, the larger the rake angle α, the larger the angle ψ between the direction in which the cut pellets fly and the die surface as shown in FIG. 6, and the easier it is to fly away from the die surface.

【0012】冷却水は、ダイ面に形成される溶融樹脂膜
を固化するだけで、ダイを過冷却して樹脂による目詰ま
りを生じさせないことが必要で、そのために冷却水を霧
状にして吹付けるのが望ましい。噴霧角度は圧力又は流
量を変えることにより調整することが可能で、15〜3
0°程度が効果的である。
The cooling water only needs to solidify the molten resin film formed on the die surface, and it is necessary that the die is supercooled so as not to cause clogging with the resin. It is desirable to attach. The spray angle can be adjusted by changing the pressure or the flow rate.
About 0 ° is effective.

【0013】[0013]

【発明の実施の形態】図7は、図1に示す空中ホットカ
ット方式の造粒装置において、ホルダー軸11の軸支持
部12に環状板13を固着し、環状板13の両側に噴霧
ノズル14を取着して両ノズル14にポンプ15、圧力
計16及びバルブ17等を含む冷却水の配管18を接続
してなるもので、両噴霧ノズル14から冷却水が霧状と
なってダイ面とカッター5に噴霧され、その噴霧角度
は、ポンプ15の回転数を変え、冷却水の圧力を変える
ことによって調整できるようにしてある。
FIG. 7 shows an aerial hot cut type granulating apparatus shown in FIG. 1 in which an annular plate 13 is fixed to a shaft support 12 of a holder shaft 11 and spray nozzles 14 are provided on both sides of the annular plate 13. The cooling water pipe 18 including the pump 15, the pressure gauge 16, the valve 17 and the like is connected to both nozzles 14, and the cooling water is sprayed from both the spray nozzles 14 to the die surface. The spray is sprayed on the cutter 5, and the spray angle can be adjusted by changing the rotation speed of the pump 15 and changing the pressure of the cooling water.

【0014】カッティングされたペレットはカッターフ
ード1の周面を螺旋状に流れる冷却水2中に落下して冷
却されながら出口7まで運ばれたのち、図示していない
が従来と同様、遠心乾燥機で乾燥され、ついで自動篩器
に掛けて製品となる単独のペレットと互着及びグレープ
状ペレットに選別される。実験例1カッターを図4に示
す鉈刃状カッター9とした図7に示す装置を用いてポリ
メチルペンテンの造粒を次のようにして行った。
The cut pellets fall into the cooling water 2 flowing spirally on the peripheral surface of the cutter hood 1 and are conveyed to the outlet 7 while being cooled. And then sieved through an automatic sieving machine to separate into single pellets, cohesive and grape-like pellets. Experimental Example 1 Granulation of polymethylpentene was performed as follows using an apparatus shown in FIG. 7 in which the cutter was a hatchet blade-shaped cutter 9 shown in FIG.

【0015】MFRが1〜10g/10分、20〜40
g/10分及び50〜500g/10分の範囲にある3
種類のポリ4−メチル−1−ペンテン樹脂の各々につい
て、以下に示すカッティング条件にて、H.IKEUCHI&CO.,
LTD製の噴霧ノズル14から冷却水を霧状にして所定の
噴霧角度でダイ面とカッター9とに吹付けながらカッテ
ィングし、造粒を行ってペレットを得た。 カッティッング条件 ダイ孔を通過する溶融樹脂の通過速度(線速):70〜
100cm/sec カッターについて 回転数:1700〜3000rpm、 カッターの取付角度:25〜45° カッターのすくい角:40〜50° カッターの逃げ角 :15〜20° カッターの刃先角 :25〜30° 冷却水の温度:20〜40℃ 冷却水の圧力:4Kg/cm2 噴霧角度:15〜30度
MFR of 1 to 10 g / 10 min, 20 to 40
g / 10 minutes and 3 in the range of 50 to 500 g / 10 minutes
For each type of poly-4-methyl-1-pentene resin, under the following cutting conditions, H.IKEUCHI & CO.,
Cooling water was atomized from a spray nozzle 14 manufactured by LTD and sprayed at a predetermined spray angle onto the die surface and the cutter 9 to perform cutting and granulation to obtain pellets. Cutting conditions Passing speed (linear speed) of the molten resin passing through the die hole: 70 to
100cm / sec About cutter Cutter rotation speed: 1700-3000rpm, Cutter mounting angle: 25-45 ° Cutter rake angle: 40-50 ° Cutter relief angle: 15-20 ° Cutter tip angle: 25-30 ° Cooling water Temperature: 20-40 ° C. Cooling water pressure: 4 kg / cm 2 Spray angle: 15-30 degrees

【0016】得られたペレットを乾燥後、自動篩器に掛
け、前記3種類のMFRの範囲にある各々の樹脂につい
て、篩上ペレットの発生量を調べた。この結果を以下の
表1に示す。該表にはダイ面に冷却水を注水しないでカ
ッティングする方法、すなわち、図1に示す従来の装置
を用い、図4に示す鉈刃状カッター9を用いて同様の条
件で同じ樹脂を造粒した場合の結果を併せて示した。表
1に見られるように注水しないでカッティングすると、
篩上ペレットの発生量が増えることがわかる。
After the obtained pellets were dried, they were passed through an automatic sieve, and the amount of pellets generated on the sieve was examined for each of the three types of resins in the MFR range. The results are shown in Table 1 below. The table shows a method of cutting without injecting cooling water into the die surface, that is, using the conventional apparatus shown in FIG. 1 and granulating the same resin under the same conditions using the hatchet cutter 9 shown in FIG. The results in the case where they were performed are also shown. When cutting without water injection as seen in Table 1,
It can be seen that the amount of pellets generated on the sieve increases.

【0017】[0017]

【表1】 [Table 1]

【0018】実験例2 カッターを図2に示すナイフ状カッター10とした以外
は、先の実験例1と同じ条件で、同じ樹脂について冷却
水を注水しながらカッティングした場合と、冷却水を注
水しないでカッティングした場合について調べた。この
結果を以下の表2に示す。
EXPERIMENTAL EXAMPLE 2 Except that the cutter was a knife-shaped cutter 10 shown in FIG. 2, under the same conditions as in Experimental Example 1 above, the same resin was cut while cooling water was injected, and no cooling water was injected. It examined about the case where it cut with. The results are shown in Table 2 below.

【0019】[0019]

【表2】 [Table 2]

【0020】実験例3 カッターを図3に示す鉈刃状カッター9とした以外は先
の実験例1と同じ条件で、同じ樹脂について冷却水を注
水しながらカッティングした場合と、冷却水を注水しな
いでカッティングした場合について調べた。この結果を
表3に示す。
EXPERIMENTAL EXAMPLE 3 Except that the cutter was a hatchet blade-shaped cutter 9 shown in FIG. 3, under the same conditions as in Experimental Example 1 above, the same resin was cut while cooling water was injected, and no cooling water was injected. It examined about the case where it cut with. Table 3 shows the results.

【0021】[0021]

【表3】 [Table 3]

【0022】以上の実験例1〜3の結果に見られるよう
に、冷却水を散布ないし噴霧した場合には、これを行わ
ない場合に比べ、MFRが1〜500g/10分の全て
の範囲において篩上ペレットの発生率が低下し、とくに
MFRが50以上の高MFR樹脂程、篩上ペレットの発
生量が急減し、該樹脂は冷却水の噴霧に顕著な効果があ
ることが判明した。またMFRが50以上の樹脂では、
図2に示すカッターを使用するよりも図3に示すカッタ
ーを、更には取付角度の小さな図4に示すカッターを使
用する方が篩上ペレットの発生量が低減し、効果がある
ことが判った。
As can be seen from the results of Experimental Examples 1 to 3, when the cooling water was sprayed or sprayed, the MFR was in the range of 1 to 500 g / 10 min in comparison with the case where the cooling water was not sprayed or sprayed. It has been found that the rate of generation of on-sieve pellets decreases, and in particular, the higher the MFR resin having an MFR of 50 or more, the more the amount of on-sieve pellets decreases, and the resin has a remarkable effect on spraying cooling water. In the case of a resin having an MFR of 50 or more,
The use of the cutter shown in FIG. 3 and the use of the cutter shown in FIG. 4 having a small mounting angle rather than the use of the cutter shown in FIG. .

【0023】[0023]

【発明の効果】請求項1及び5記載の方法及び装置によ
ると、ダイ面に形成される溶融樹脂膜が冷却水の散布な
いし噴霧により冷却固化されて剥離されるようになり、
その結果、カッター刃がダイ面に密着して切れ味が良好
に維持され、互着ペレットやグレープ状ペレットの発生
率が低下して製品の収率が改善されると共に、篩上ペレ
ット除去作業が軽減されて省力化が可能となる。
According to the method and the apparatus according to the first and fifth aspects, the molten resin film formed on the die surface is cooled and solidified by spraying or spraying cooling water, and peeled off.
As a result, the cutter blade adheres to the die surface, maintaining good sharpness, reducing the incidence of cohesive pellets and grape-like pellets, improving product yield, and reducing the work of removing pellets on the sieve. It is possible to save labor.

【0024】請求項2記載の方法によると、カッティン
グ状態を良好に保つことができる。請求項6記載の装置
のように、カッターとして鉈刃状カッターを用いると、
撓みが小さいため刃全体をダイ面に密着させてカッティ
ング状態を良好に保つことができ、馴らし運転を不要に
できること、寿命が長く、刃を研磨することにより繰返
して使用できること等の効果を奏する。
According to the method of the second aspect, the cutting state can be kept good. When a hatchet-shaped cutter is used as the cutter as in the device according to claim 6,
Since the bending is small, the entire blade can be brought into close contact with the die surface to maintain a good cutting state, the running-in operation can be eliminated, the life is long, and the blade can be used repeatedly by polishing it.

【0025】請求項7及び8記載の各発明によると、カ
ッティング状態を良好に保つことができる。
According to the seventh and eighth aspects of the present invention, it is possible to maintain a good cutting state.

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

【図1】従来の造粒装置の概略横断面図。FIG. 1 is a schematic cross-sectional view of a conventional granulation apparatus.

【図2】従来のカッターを取付けたホルダーの側面図。FIG. 2 is a side view of a holder to which a conventional cutter is attached.

【図3】本発明に係るカッター使用例を示す側面図。FIG. 3 is a side view showing an example of using a cutter according to the present invention.

【図4】本発明に係るカッターの別の例の実施形態の使
用例を示す側面図。
FIG. 4 is a side view showing an example of use of another embodiment of the cutter according to the present invention.

【図5】カッターの説明図。FIG. 5 is an explanatory view of a cutter.

【図6】切断時にペレットが飛ぶ方向を示す図。FIG. 6 is a view showing a direction in which pellets fly during cutting.

【図7】本発明に係る造粒装置の概略横断面図。FIG. 7 is a schematic cross-sectional view of a granulation apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

1・・カッターフード 2・・水膜 3・・モータ 4・・ホルダー 5・・カッター 6・・ダイ 7・・出口 8・・柄 9・・鉈刃状カッター 10・・ナイフ状カッター 11・・ホルダー軸 13・・環状板 14・・噴霧ノズル 15・・ポンプ 16・・圧力計 17・・パイプ 18・・配管 1. Cutter hood 2. Water film 3. Motor 4. Holder 5. Cutter 6. Die 7. Outlet 8. Pattern 9. Hatchet blade cutter 10. Knife cutter 11. Holder shaft 13, annular plate 14, spray nozzle 15, pump 16, pressure gauge 17, pipe 18, pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 松原 伸夫 山口県玖珂郡和木町和木六丁目1番2号 三井化学株式会社内 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Nobuo Matsubara 1-2-1, Waki, Waki-machi, Kuga-gun, Yamaguchi Prefecture Inside Mitsui Chemicals, Inc.

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】押出機先端に取付けたダイより押出された
溶融樹脂をダイ面を摺接しながら回転するカッターで切
断してペレット化し、水中に落下させて冷却する空中ホ
ットカット方式による造粒方法において、ダイ面に形成
される溶融樹脂膜を固化するため冷却水を散布ないし噴
霧させることを特徴とする造粒方法。
1. A granulating method by an in-air hot-cut method in which molten resin extruded from a die attached to the extruder tip is cut into pellets by a rotating cutter while slidingly contacting the die surface, dropped into water and cooled. The method according to claim 1, wherein cooling water is sprayed or sprayed to solidify the molten resin film formed on the die surface.
【請求項2】冷却水の噴霧角度は15〜30°である請
求項1記載の造粒方法。
2. The granulation method according to claim 1, wherein the spray angle of the cooling water is 15 to 30 °.
【請求項3】造粒に供される樹脂のMFR値が5〜50
0g/10分である請求項1又は2記載の造粒方法。
3. The resin subjected to granulation has an MFR value of 5 to 50.
The granulation method according to claim 1 or 2, wherein the amount is 0 g / 10 minutes.
【請求項4】造粒に供される樹脂がポリ4−メチル−1
ペンテンである請求項1ないし3のいづれかの請求項に
記載の造粒方法。
4. The resin used for granulation is poly-4-methyl-1.
The granulation method according to any one of claims 1 to 3, wherein the granulation method is pentene.
【請求項5】押出機先端に取付けたダイと、モータを駆
動源として回転駆動されるホルダーに放射状に取付けら
れ、ダイのダイ面に押付けられた状態で回転するカッタ
ーとからなり、ダイより押出される溶融樹脂をカッター
により切断してペレット化し、水中に落下させて冷却す
る空中ホットカット方式による造粒装置において、ダイ
面に形成される溶融樹脂膜を固化するため冷却水を散布
ないし噴霧させるノズルを含む装置を設けたことを特徴
とする造粒装置。
5. A die attached to the tip of an extruder, and a cutter radially mounted on a holder which is rotated and driven by a motor as a driving source, and rotated while being pressed against the die surface of the die. In a granulator using an aerial hot-cut method in which the molten resin to be cut is pelletized by cutting with a cutter, dropped into water and cooled, spraying or spraying cooling water to solidify the molten resin film formed on the die surface. A granulating device comprising a device including a nozzle.
【請求項6】カッターには剛性の大なる鉈状カッターが
使用される請求項5記載の造粒装置。
6. The granulating apparatus according to claim 5, wherein a cutter having high rigidity is used as the cutter.
【請求項7】カッターの取付角度は25〜45°である
請求項5又は6記載の造粒装置。
7. The granulating apparatus according to claim 5, wherein the cutter has an attachment angle of 25 to 45 °.
【請求項8】カッターのすくい角が40〜50°、逃げ
角が15〜20°、刃先角が25〜30°である請求項
5ないし7のいづれかの請求項に記載の造粒装置。
8. The granulating apparatus according to claim 5, wherein the rake angle of the cutter is 40 to 50 °, the clearance angle is 15 to 20 °, and the cutting edge angle is 25 to 30 °.
JP07203598A 1998-02-20 1998-03-20 Granulation method and apparatus Expired - Lifetime JP3996695B2 (en)

Priority Applications (1)

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Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP10-38910 1998-02-20
JP3891098 1998-02-20
JP07203598A JP3996695B2 (en) 1998-02-20 1998-03-20 Granulation method and apparatus

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Publication Number Publication Date
JPH11300739A true JPH11300739A (en) 1999-11-02
JP3996695B2 JP3996695B2 (en) 2007-10-24

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JP2002120222A (en) * 2000-10-18 2002-04-23 Polyplastics Co Resin cutting device for pelletizing and method for pelletizing
JP2005503944A (en) * 2001-09-25 2005-02-10 バイエル アクチェンゲゼルシャフト Cutting granulator for producing cut pieces and method for producing cut pieces
JP2009501622A (en) * 2005-07-20 2009-01-22 ネステク ソシエテ アノニム Equipment for producing granular products by extrusion and cutting
JP2010030105A (en) * 2008-07-28 2010-02-12 Japan Steel Works Ltd:The Hot cuter
WO2011155166A1 (en) * 2010-06-07 2011-12-15 株式会社神戸製鋼所 Knife holder for underwater cutting granulator
CN103011934A (en) * 2012-12-13 2013-04-03 江苏金利化工机械有限公司 Tower type centrifugal-spraying differential action pelleting device
JP2021070204A (en) * 2019-10-30 2021-05-06 住友化学株式会社 Resin pellet and resin pellet manufacturing method
CN113853285A (en) * 2019-06-27 2021-12-28 东洋纺株式会社 Method for producing pellets
CN115570701A (en) * 2022-10-24 2023-01-06 山东颐工材料科技股份有限公司 Underwater granulating unit of granulator for MBS resin production
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Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002120222A (en) * 2000-10-18 2002-04-23 Polyplastics Co Resin cutting device for pelletizing and method for pelletizing
JP4647076B2 (en) * 2000-10-18 2011-03-09 ポリプラスチックス株式会社 Pelletizing resin cutting apparatus and pelletizing method
JP2005503944A (en) * 2001-09-25 2005-02-10 バイエル アクチェンゲゼルシャフト Cutting granulator for producing cut pieces and method for producing cut pieces
JP2009501622A (en) * 2005-07-20 2009-01-22 ネステク ソシエテ アノニム Equipment for producing granular products by extrusion and cutting
JP2010030105A (en) * 2008-07-28 2010-02-12 Japan Steel Works Ltd:The Hot cuter
JP2011255535A (en) * 2010-06-07 2011-12-22 Kobe Steel Ltd Knife holder for underwater cutting granulating apparatus
WO2011155166A1 (en) * 2010-06-07 2011-12-15 株式会社神戸製鋼所 Knife holder for underwater cutting granulator
CN102917848A (en) * 2010-06-07 2013-02-06 株式会社神户制钢所 Knife holder for underwater cutting granulator
CN102917848B (en) * 2010-06-07 2015-12-16 株式会社神户制钢所 Prilling granulator knife rest is cut in water
CN103011934A (en) * 2012-12-13 2013-04-03 江苏金利化工机械有限公司 Tower type centrifugal-spraying differential action pelleting device
CN113853285A (en) * 2019-06-27 2021-12-28 东洋纺株式会社 Method for producing pellets
CN113853285B (en) * 2019-06-27 2023-12-26 东洋纺Mc株式会社 Process for producing pellets
JP2021070204A (en) * 2019-10-30 2021-05-06 住友化学株式会社 Resin pellet and resin pellet manufacturing method
WO2023214555A1 (en) * 2022-05-05 2023-11-09 株式会社湘南貿易 Molten resin cooling device
CN115570701A (en) * 2022-10-24 2023-01-06 山东颐工材料科技股份有限公司 Underwater granulating unit of granulator for MBS resin production

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