KR200324423Y1 - Mixing screw structure of extrusion molding machine for recycle is waste synthetic resin - Google Patents

Mixing screw structure of extrusion molding machine for recycle is waste synthetic resin Download PDF

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KR200324423Y1
KR200324423Y1 KR20-2003-0014821U KR20030014821U KR200324423Y1 KR 200324423 Y1 KR200324423 Y1 KR 200324423Y1 KR 20030014821 U KR20030014821 U KR 20030014821U KR 200324423 Y1 KR200324423 Y1 KR 200324423Y1
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South Korea
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kneading
raw material
teeth
synthetic resin
waste synthetic
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KR20-2003-0014821U
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Korean (ko)
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안대경
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안대경
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING 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
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/26Scrap or recycled material

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  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

본 고안은 폐합성수지 재생용 압출 성형기의 혼련스크류 구조에 관한 것으로 보다 구체적으로는, 전방에는 원료투입부(102)를 형성하고, 후방에는 배출노즐을 형성한 압출다이(20)가 설치되는 가열실린더(10) 내부에 동일한 직경의 중심축(302)을 따라서 외주면에 일정 간격으로 형성된 스파이럴 형태의 치차(304)를 가진 한 쌍이 설치되어, 원료투입부(102)를 통해 투입되어 가열실린더(10) 내부에서 용융되는 폐합성수지 원료를 압출다이(20) 쪽으로 이송하면서 혼련시켜, 압출다이(20)를 통해 용융된 폐합성수지 원료가 압출되게 하는 공지의 폐합성수지 재생용 압출 성형기의 혼련스크류(30,30')에 있어서,The present invention relates to a kneading screw structure of an extrusion molding machine for recycling waste resin, and more specifically, a heating cylinder in which an extrusion die 20 having a raw material input part 102 is formed at a front side and a discharge nozzle is formed at a rear side thereof. (10) A pair having a spiral tooth 304 formed at regular intervals on the outer circumferential surface along the central axis 302 of the same diameter therein is installed through the raw material input unit 102, the heating cylinder 10 A kneading screw (30, 30) of a known waste synthetic resin recycling extrusion molding machine for kneading while transporting the waste synthetic resin material melted therein to the extrusion die 20, the extrusion of the molten waste synthetic resin raw material through the extrusion die 20. For '),

원료투입부(102)의 하부에 위치하며 압출다이(20) 쪽으로 갈수록 치차(304)간의 간격이 점차 좁아지는 투입이송부(30a)와, 투입이송부(30a)의 후방에 위치하며 치차(304)간의 간격이 일정한 1차혼련부(30b)와, 치차(304)간의 간격이 1차혼련부(30b)보다 조밀하며, 치차(304)의 둘레에는 등간격으로 홈부(306)를 형성한 고압믹싱부(30c)와, 1차혼련부(30b)보다 치차(304)간의 간격이 넓고 일정한 저압혼련부(30d)로 구성하여 고압믹싱부(30c)와 저압혼련부(30d)는 반복적으로 배치하며, 모든 치차(304)는 동일한 외경으로 서로 이어지게 형성하되, 첫 고압믹싱부(30c)의 양측에는 치차(304)가 끊어진 머물기부(30e)를 형성함으로서, 압출기로 투입되어 용융되는 폐합성수지 원료의 혼련성능을 크게 향상시킬 수 있을 뿐 만 아니라, 치차간의 간격이 다른 고압 믹싱부와 배출부의 반복적인 배열을 통해서 용융, 혼련되는 원료의 고밀도, 고속 압출이 가능케 되어 재생된 제품의 품질과 생산성을 크게 향상시킬 수 있게 된다.Located in the lower portion of the raw material input portion 102 and positioned toward the extrusion die 20, the interval between the teeth (304) gradually becomes narrower, and the rear of the input transfer portion (30a) and the tooth 304 ), The interval between the primary kneading portion 30b and the tooth 304 is denser than that of the primary kneading portion 30b, and the groove 306 is formed at equal intervals around the tooth 304 at a high pressure. The high-pressure mixing section 30c and the low-pressure mixing section 30d are repeatedly arranged by the mixing section 30c and the low-pressure kneading section 30d having a larger spacing between the teeth 304 than the primary kneading section 30b and the constant mixing section 30d. And, all the teeth 304 are formed to be connected to each other with the same outer diameter, the waste synthetic resin raw material is injected into the extruder by forming the staying portion 30e is the tooth 304 is broken on both sides of the first high-pressure mixing section (30c) Not only can greatly improve the kneading performance of the high pressure mixing section, but also This arrangement enables high-density, high-speed extrusion of melted and kneaded raw materials, greatly improving the quality and productivity of recycled products.

Description

폐합성수지 재생용 압출 성형기의 혼련스크류 구조{MIXING SCREW STRUCTURE OF EXTRUSION MOLDING MACHINE FOR RECYCLE IS WASTE SYNTHETIC RESIN}MIXING SCREW STRUCTURE OF EXTRUSION MOLDING MACHINE FOR RECYCLE IS WASTE SYNTHETIC RESIN}

본 고안은 폐합성수지 재생용 압출 성형기의 혼련스크류 구조에 관한 것으로, 보다 구체적으로는 압출 성형기의 가열실린더 내부에 설치되는 한 쌍의 혼련스크류 외주면에 형성된 스파이럴 형상의 치차 구조를 효율적으로 개선하여 압출 성형기의 가열실린더 내부에서 용융된 폐합성수지의 혼련 성능을 크게 향상시킴과 동시에 용융된 원료의 압출밀도와 압출속도를 크게 향상시킬 수 있게 한 것이다.The present invention relates to a kneading screw structure of an extrusion molding machine for recycling waste resin, and more specifically, an extrusion molding machine by efficiently improving the spiral gear structure formed on the outer peripheral surface of a pair of kneading screws installed inside a heating cylinder of the extrusion molding machine. It is to improve the kneading performance of the molten waste synthetic resin in the heating cylinder of the molten raw material at the same time and to greatly improve the extrusion density and extrusion speed of the molten raw material.

일반적인 폐합성수지 재생용 압출 성형기는 플라스틱 성형기의 일종으로서, 재생을 위해 수거되어 펠릿 형태로 가공된 폐합성수지 소재를 가열실린더 내부에 공급하여 고열로 용융시키면서 압출다이를 통해 압출하여 가열실린더의 단부에 설치된 압출다이의 단면 형태에 따라서 봉재, 판재, 형재 등 다양한 형태의 합성수지 제품으로 재생하는데 사용되는 성형기로서 통상적으로 가열실린더의 내부에는 용융된 수지를 혼련, 압출하기 위한 혼련스크류가 설치되는데, 과거에서 하나의 혼련스크류가 설치된 압출성형기가 주를 이루었으나, 최근에는 용융된 수지의 압출밀도를향상시키기 위하여 한 쌍의 스크류를 서로 맞물리게 설치하는 형태가 일반화되어 있는 실정이다.General waste synthetic resin recycling extrusion machine is a kind of plastic molding machine, and the waste synthetic resin material collected for recycling and processed into pellets is supplied to the inside of the heating cylinder, extruded through an extrusion die while being melted at high temperature and installed at the end of the heating cylinder. Depending on the cross-sectional shape of the extrusion die, it is a molding machine used to regenerate various types of synthetic resin products such as rods, plates, and shapes, and a kneading screw for kneading and extruding molten resin is usually installed inside a heating cylinder. Extruder is equipped with a kneading screw of the predominantly, but in recent years, in order to improve the extrusion density of the molten resin is a situation in which a pair of screws are interlocked with each other to install the situation.

그러나, 이와 같은 종래의 압출 성형기에 설치된 한 쌍으로 구성된 혼련스크류는 중심축의 외주면에 형성된 치차간의 간격이 모두 일정하거나 또는 용융된 수지의 배출밀도를 향상시키기 위하여 압출 성형기에서 압출다이 쪽으로 갈수록 중심축이나 치차의 외경이 증가하게 함으로서, 용융된 원료의 압출 압력을 향상시켜 배출밀도를 증가시키는 효과는 발휘하였으나, 이에 반해 용융된 원료의 압출속도는 저하되어 생산성의 떨어지는 문제점이 있었다.However, the pair of kneading screws installed in such a conventional extrusion molding machine has a constant interval between the teeth formed on the outer peripheral surface of the central axis, or in order to improve the discharge density of the molten resin in the extrusion die in the direction toward the extrusion die By increasing the outer diameter of the gear, the extrusion pressure of the molten raw material was improved to exert an effect of increasing the discharge density, while the extrusion rate of the molten raw material was lowered, resulting in a drop in productivity.

본 고안은 위와 같은 종래의 문제점을 해소하기 위하여 안출한 것으로서, 압출 성형기 내부에서 용융된 수지를 배출하는 배출밀도와 배출속도를 동시에 향상시키는데 고안의 목적이 있다.The present invention has been made in order to solve the above conventional problems, the purpose of the present invention to improve the discharge density and discharge rate for discharging the molten resin in the extrusion molding machine at the same time.

이러한 고안의 목적 달성을 위하여 본 고안의 혼련스크류는 원료투입부에서는 치차의 간격이 압출다이 쪽으로 갈수록 점차 좁아지게 형성하고, 혼련부에서는 치차의 간격이 일정하게 형성하며, 고압믹싱부에서는 치차의 간격이 조밀하고 치차의 외주를 따라서 홈을 형성하여, 혼련부와 고압믹싱부는 일정 간격으로 반복되게 함으로서, 혼련스크류의 직경 변화 없이도 용융된 수지의 배출밀도와 배출속도를 동시에 향상시킬 수 있게 한 것으로 이를 첨부된 도면에 의하여 보다 상세히 설명하면 다음과 같다.In order to achieve the object of the present invention, the kneading screw of the present invention is formed such that the tooth gap gradually becomes narrower toward the extrusion die in the raw material input portion, the tooth gap is uniformly formed in the kneading portion, and the tooth gap in the high pressure mixing portion. By forming grooves along the outer periphery of the compact gear, the kneading portion and the high pressure mixing portion are repeated at regular intervals, thereby simultaneously improving the discharge density and discharge rate of the molten resin without changing the diameter of the kneading screw. When described in more detail by the accompanying drawings as follows.

도 1은 본 고안의 평면 예시도1 is a plan view of the present invention

도 2의 (가)는 본 고안의 투입이송부의 치차 확대 단면 예시도Figure 2 (a) is an enlarged cross-sectional view of the tooth feed portion of the present invention

(나)는 본 고안의 1차혼련부의 치차 확대 단면 예시도(B) is an enlarged cross-sectional view of the first kneading portion of the present invention

(다)는 본 고안의 고압믹싱부의 치차 확대 단면 예시도(C) is an enlarged cross-sectional view of the high-pressure mixing unit of the present invention

(라)는 본 고안의 저압혼련부의 치차 확대 단면 예시도(D) is an enlarged cross-sectional view of the low pressure kneading portion of the present invention

도 3은 본 고안의 사용상태를 나타낸 성형기의 평면 부분 단면 예시도Figure 3 is a partial cross-sectional view of a molding machine showing a state of use of the subject innovation

도 4는 본 고안의 사용상태를 나타낸 종단면 예시도Figure 4 is a longitudinal cross-sectional view showing a state of use of the subject innovation

도 5는 일반적인 폐합성수지 재생용 압출 성형기를 나타낸 측면 예시도이다.Figure 5 is an exemplary view showing a side extrusion molding machine for recycling general waste resin.

< 도면의 주요 부분에 대한 부호의 설명 ><Description of Symbols for Main Parts of Drawings>

10 : 가열실린더 102 : 원료투입부10: heating cylinder 102: raw material input portion

104 : 가스배출구 20 : 압출다이104 gas outlet 20 extrusion die

30, 30' : 혼련스크류 30a : 투입이송부30, 30 ': Kneading screw 30a: Feeding and conveying part

30b : 1차혼련부 30c : 고압믹싱부30b: primary kneading unit 30c: high pressure mixing unit

30d : 저압혼련부 30e : 머물기부30d: low pressure kneading part 30e: staying part

302 : 중심축 304 : 치차302: central axis 304: gear

306 : 홈부306: groove

전방에는 원료투입부(102)를 형성하고, 후방에는 배출노즐을 형성한 압출다이(20)가 설치되는 가열실린더(10) 내부에 동일한 직경의 중심축(302)을 따라서 외주면에 일정 간격으로 형성된 스파이럴 형태의 치차(304)를 가진 한 쌍이 설치되어, 원료투입부(102)를 통해 투입되어 가열실린더(10) 내부에서 용융되는 폐합성수지 원료를 압출다이(20) 쪽으로 이송하면서 혼련시켜, 압출다이(20)를 통해 용융된 폐합성수지 원료가 압출되게 하는 공지의 폐합성수지 재생용 압출 성형기의 혼련스크류(30,30')에 있어서,A raw material input part 102 is formed at the front side, and is formed at regular intervals on the outer circumferential surface along the central axis 302 of the same diameter inside the heating cylinder 10 in which the extrusion die 20 having the discharge nozzle is formed at the rear. A pair having a spiral tooth 304 is installed and kneaded while conveying the waste synthetic resin raw material which is introduced through the raw material input unit 102 and melted in the heating cylinder 10 toward the extrusion die 20, and the extrusion die In the kneading screw (30, 30 ') of the known waste synthetic resin recycling extrusion molding machine for extruding the molten waste synthetic resin raw material through the (20),

원료투입부(102)의 하부에 위치하며 압출다이(20) 쪽으로 갈수록 치차(304)간의 간격이 점차 좁아지는 투입이송부(30a)와,Located in the lower portion of the raw material input section 102 and the feed port (30a) and the gap between the teeth 304 gradually narrowed toward the extrusion die 20,

투입이송부(30a)의 후방에 위치하며 치차(304)간의 간격이 일정한 1차혼련부(30b)와,A first kneading portion 30b positioned at the rear of the feeding portion 30a and having a constant interval between the teeth 304;

치차(304)간의 간격이 1차혼련부(30b)보다 조밀하며, 치차(304)의 둘레에는 등간격으로 홈부(306)를 형성한 고압믹싱부(30c)와,The space between the teeth 304 is denser than the primary kneading portion 30b, and the high pressure mixing portion 30c having the groove portions 306 formed at equal intervals around the teeth 304,

1차혼련부(30b)보다 치차(304)간의 간격이 넓고 일정한 저압혼련부(30d)로 구성하되,Although the interval between the teeth 304 is wider than the primary kneading portion 30b and constitutes a constant low pressure kneading portion 30d,

고압믹싱부(30c)와 저압혼련부(30d)는 반복적으로 배치하며, 모든 치차(304)는 동일한 외경으로 서로 이어지게 형성하되, 첫 고압믹싱부(30c)의 양측에는 치차(304)가 끊어진 머물기부(30e)를 형성한 구성이다.The high pressure mixing unit 30c and the low pressure kneading unit 30d are repeatedly arranged, and all the teeth 304 are formed to be connected to each other with the same outer diameter, but the teeth 304 stay on both sides of the first high pressure mixing unit 30c. It is the structure which formed the base 30e.

미설명부호 '104'는 용융된 수지를 압출하는 과정에서 발생하는 가스가 배출되는 가스배출부를 나타낸 것이다.Reference numeral '104' indicates a gas discharge part through which gas generated in the process of extruding the molten resin is discharged.

이와 같이 된 본 고안은 가열실린더(10)의 원료투입부(102)를 통해 투입되어 용융되는 폐합성수지 원료를 보다 신속하게 압출다이(20) 쪽으로 이송시킬 수 있을 뿐 만 아니라, 보아 향상된 혼련 성능을 통해서 고밀도, 고속 압출이 가능케 된다.The present invention as described above can not only transfer the waste synthetic resin material which is injected and melted through the raw material input portion 102 of the heating cylinder 10 to the extrusion die 20 more quickly, but also improves the kneading performance in view. High density, high speed extrusion is possible.

즉, 첨부도면 도 1에서와 같이 중심축(302)을 따라서 외주면에 치차(304)를 형성하여 가열실린더(10) 내부에서 서로의 치차(304)가 맞물리게 설치되는 한 쌍의 혼련스크류(30,30')는 도면에서와 같이 도면의 우측에 위치한 원료투입부(102) 쪽에는 압출다이(20) 쪽으로 갈수록 치차(304)간의 간격이 점차 좁아지는 투입이송부(30a)가 형성되는데, 이러한 치차(304)의 구조를 가진 투입이송부(30a)는 펠릿 형태로 가공된 폐합성수지 소재가 원료투입부(102)를 통해서 최초로 투입되어 가열실린더(10) 내부에서 완전히 용융되지 않은 상태이므로 그 입자가 크기 때문에 입자가 큰 원료를 보다 신속하게 이송시켜 원활한 원료 공급이 이루어질 수 있도록 하게되며, 투입된 원료는 이송되는 과정에서 점차 용융되기 때문에 투입이송부(30a)의 치차(304)는 압출다이(20) 쪽으로 갈수록 그 간격이 점차 좁아지면서 원료를 점차 높은 압력으로 혼련하게 된다.That is, as shown in FIG. 1, a pair of kneading screws 30 are formed in which the teeth 304 are engaged with each other in the heating cylinder 10 by forming the teeth 304 on the outer circumferential surface along the central axis 302. 30 ') is formed on the side of the raw material input unit 102 located on the right side of the drawing, an injection feed unit 30a is formed in which the distance between the teeth 304 gradually decreases toward the extrusion die 20. The input transfer part 30a having the structure of 304 has a state in which the waste synthetic resin material processed in a pellet form is first introduced through the raw material input part 102 and is not completely melted inside the heating cylinder 10, so that the particles Due to its size, the raw material having large particles can be transferred more quickly so that a smooth raw material can be supplied. Since the injected raw material is gradually melted in the process of being transferred, the tooth 304 of the feeding portion 30a is extruded 20. Go towards As the gap becomes narrower, the raw material is kneaded at higher pressure.

그리하여 가열실린더(10) 내부에서 원료가 어느 정도 용융되면 투입이송부(30a)의 후방에 위치하며 치차(304)간의 간격이 일정한 1차혼련부(30b)에서 용융된 원료의 본격적인 혼련이 이루어지게 되는데, 1차혼련부(30b)는 치차(304)간의 간격이 일정하기 때문에 일정한 속도로 용융된 원료가 혼련되면서 이송되게 된다.Thus, when the raw material is melted to some extent inside the heating cylinder 10, the kneading of the raw material melted in the primary kneading unit 30b at the rear of the feeding and feeding unit 30a and the interval between the teeth 304 is constant is made. The first kneading unit 30b is transported while the molten raw material is kneaded at a constant speed because the interval between the teeth 304 is constant.

한편, 1차혼련부(30b)의 후방에는 치차(304)간의 간격이 1차혼련부(30b)보다 조밀하고, 치차(304)의 둘레에 홈부(306)를 형성한 고압믹싱부(30c)가 형성되어 있어서, 1차혼련부(30b)에서 혼련된 원료를 보다 높은 압력을 혼련할 뿐 만 아니라, 치차(304)의 둘레에 형성된 홈부(306)는 완전히 용융되지 않은 폐합성수지 펠릿을 으깨는 작용을 수행함으로서 큰 입자의 상태를 유지하고 있는 원료를 보다 작은 입자의 상태로 쪼개어주면서 용융된 수지에 고전단율 및 고전단응력을 발생시키기 때문에 보다 향상된 혼련 성능을 발휘할 수 있게된다.On the other hand, in the rear of the primary kneading portion 30b, the spacing between the teeth 304 is denser than the primary kneading portion 30b, and the high-pressure mixing portion 30c in which the groove portion 306 is formed around the tooth 304 is formed. Is formed, the raw material kneaded in the primary kneading portion 30b not only kneading higher pressure, but also the groove portion 306 formed around the tooth 304 crushes the waste synthetic resin pellets which are not completely melted. By performing the action, the raw material holding the state of the large particles is split into the state of the smaller particles, thereby generating a high shear rate and a high shear stress in the molten resin, thereby exhibiting improved kneading performance.

아울러, 위와 같이 강력한 혼련을 수행하는 고압믹싱부(30c)의 후방에는 고압믹싱부(30c)에 형성된 치차(304)간의 간격보다 더 넓고 일정한 간격으로 형성된 치차(304)를 가진 저압혼련부(30d)가 형성되어 있어서, 고압믹싱부(30c)에서 강력한 혼련 과정을 거친 용융된 원료를 일정 구간동안 부드럽고 신속하게 이송시키게 되는데, 이러한 저압혼련부(30d)의 후방에는 다시 고압믹싱부(30c)와 또 다른 저압혼련부(30d)를 반복적으로 형성함으로서, 강력한 혼련과 부드럽고 신속한 이송의 반복을 통해서 펠릿 형태로 투입된 폐합성수지 원료가 완벽하게 용융되어 고밀도 상태에서도 신속한 배출이 이루어질 수 있게 되는 것이다.In addition, the lower pressure kneading portion 30d having a tooth 304 formed at a constant interval and wider than the interval between the teeth 304 formed in the high pressure mixing portion 30c at the rear of the high pressure mixing portion 30c that performs the strong kneading as described above. ) Is formed, and the molten raw material that has undergone a strong kneading process in the high pressure mixing unit 30c is smoothly and quickly transferred for a predetermined period, and the high pressure mixing unit 30c and the back of the low pressure mixing unit 30d are again. By repeatedly forming another low pressure kneading unit 30d, the waste synthetic resin raw material introduced in pellet form through strong kneading and soft and rapid transfer repeating can be completely melted and can be quickly discharged even in a high density state.

한편, 1차혼련부(30b)의 후방에 위치한 첫 번째 고압믹싱부(30c)의 양측에는 머물기부(30e)가 형성되어 있는데, 이는 1차혼련부(30b)에서 빠른 속도로 이송된 원료가 1차혼련부(30b)보다 조밀한 치차(304) 구조를 가진 고압믹싱부(30c)로 진입하기 이전에 이송속도를 적절하게 조절하는 역할을 수행할 뿐 만 아니라, 고압믹싱부(30c)에서 1차 저압혼련부(30d)로 이송되는 원료의 이송속도도 절적히 조절하는 역할을 수행함으로서 연속적이고 원활한 원료의 이송이 이루어질 수 있게된다.On the other hand, on both sides of the first high-pressure mixing section (30c) located behind the primary kneading unit (30b) is formed a staying portion (30e), which is a raw material conveyed at a high speed from the primary kneading unit (30b) Not only serves to properly adjust the feed rate before entering the high pressure mixing unit 30c having the tooth 304 structure that is denser than the primary kneading unit 30b, but also in the high pressure mixing unit 30c. By appropriately adjusting the feed rate of the raw material to be transferred to the primary low pressure kneading unit 30d, it is possible to achieve continuous and smooth transfer of the raw material.

아울러, 본 고안에서 혼련스크류(30,30')의 투입이송부(30a)와 1차혼련부(30b) 및 고압믹싱부(30c)와 저압혼련부(30d)에 형성된 중심축(302)상의 모든 치차(304)의 직경은 동일한 직경으로 형성되며, 본 고안의 혼련스크류(30,30')가 설치되는 가열실린더(10)의 내경은 혼려스크류의 치차(304)의 직경과 마찬가지로 원료공급부에서부터 압출다이(20)에 이르기까지 동일한 외경으로 형성된다.In addition, in the present invention, on the central axis 302 formed in the feed and transfer portion 30a and the primary kneading portion 30b and the high pressure mixing portion 30c and the low pressure kneading portion 30d of the kneading screws 30 and 30 '. The diameters of all the teeth 304 are formed to the same diameter, and the inner diameter of the heating cylinder 10 in which the kneading screws 30 and 30 'of the present invention are installed is the same as the diameter of the teeth 304 of the blend screws from the raw material supply part. The extrusion die 20 is formed to the same outer diameter.

상술한 바와 같이 본 고안은 혼련스크류의 구조를 개선하여 압출기로 투입되어 용융되는 폐합성수지 원료의 혼련성능을 크게 향상시킬 수 있을 뿐 만 아니라, 치차간의 간격이 다른 고압믹싱부와 배출부의 반복적인 배열을 통해서 용융, 혼련되는 원료의 고밀도, 고속 압출이 가능케 되어 재생된 제품의 품질과 생산성을 크게 향상시킬 수 있는 이점이 있다.As described above, the present invention not only can greatly improve the kneading performance of the waste synthetic resin raw material that is injected into the extruder by improving the structure of the kneading screw, but also repeats the arrangement of the high pressure mixing part and the discharge part having different tooth spacing. Through the high-density, high-speed extrusion of the raw material to be melted and kneaded, it is possible to greatly improve the quality and productivity of the recycled product.

Claims (1)

전방에는 원료투입부(102)를 형성하고, 후방에는 배출노즐을 형성한 압출다이(20)가 설치되는 가열실린더(10) 내부에 동일한 직경의 중심축(302)을 따라서 외주면에 일정 간격으로 형성된 스파이럴 형태의 치차(304)를 가진 한 쌍이 설치되어, 원료투입부(102)를 통해 투입되어 가열실린더(10) 내부에서 용융되는 폐합성수지 원료를 압출다이(20) 쪽으로 이송하면서 혼련시켜, 압출다이(20)를 통해 용융된 폐합성수지 원료가 압출되게 하는 공지의 폐합성수지 재생용 압출 성형기의 혼련스크류(30,30')에 있어서,A raw material input part 102 is formed at the front side, and is formed at regular intervals on the outer circumferential surface along the central axis 302 of the same diameter inside the heating cylinder 10 in which the extrusion die 20 having the discharge nozzle is formed at the rear. A pair having a spiral tooth 304 is installed and kneaded while conveying the waste synthetic resin raw material which is introduced through the raw material input unit 102 and melted in the heating cylinder 10 toward the extrusion die 20, and the extrusion die In the kneading screw (30, 30 ') of the known waste synthetic resin recycling extrusion molding machine for extruding the molten waste synthetic resin raw material through the (20), 원료투입부(102)의 하부에 위치하며 압출다이(20) 쪽으로 갈수록 치차(304)간의 간격이 점차 좁아지는 투입이송부(30a)와,Located in the lower portion of the raw material input section 102 and the feed port (30a) and the gap between the teeth 304 gradually narrowed toward the extrusion die 20, 투입이송부(30a)의 후방에 위치하며 치차(304)간의 간격이 일정한 1차혼련부(30b)와,A first kneading portion 30b positioned at the rear of the feeding portion 30a and having a constant interval between the teeth 304; 치차(304)간의 간격이 1차혼련부(30b)보다 조밀하며, 치차(304)의 둘레에는 등간격으로 홈부(306)를 형성한 고압믹싱부(30c)와,The space between the teeth 304 is denser than the primary kneading portion 30b, and the high pressure mixing portion 30c having the groove portions 306 formed at equal intervals around the teeth 304, 1차혼련부(30b)보다 치차(304)간의 간격이 넓고 일정한 저압혼련부(30d)로 구성하여 고압믹싱부(30c)와 저압혼련부(30d)는 반복적으로 배치하며, 모든 치차(304)는 동일한 외경으로 서로 이어지게 형성하되, 첫 고압믹싱부(30c)의 양측에는 치차(304)가 끊어진 머물기부(30e)를 형성한 것을 특징으로 하는 폐합성수지 재생용 압출 성형기의 혼련스크류 구조The high-pressure mixing section 30c and the low-pressure mixing section 30d are repeatedly arranged and composed of a constant low-pressure kneading section 30d having a larger spacing between the teeth 304 than the first kneading section 30b, and all the teeth 304. Are formed to be connected to each other with the same outer diameter, the kneading screw structure of the waste plastic resin recycling extrusion molding machine, characterized in that the teeth 30 on both sides of the first high-pressure mixing section (30c) formed a staying portion (30e) is broken
KR20-2003-0014821U 2003-05-14 2003-05-14 Mixing screw structure of extrusion molding machine for recycle is waste synthetic resin KR200324423Y1 (en)

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