KR101388650B1 - An injection molding apparatus for urethane - Google Patents

An injection molding apparatus for urethane Download PDF

Info

Publication number
KR101388650B1
KR101388650B1 KR1020130108891A KR20130108891A KR101388650B1 KR 101388650 B1 KR101388650 B1 KR 101388650B1 KR 1020130108891 A KR1020130108891 A KR 1020130108891A KR 20130108891 A KR20130108891 A KR 20130108891A KR 101388650 B1 KR101388650 B1 KR 101388650B1
Authority
KR
South Korea
Prior art keywords
urethane
injection
mold
inlet
batch tank
Prior art date
Application number
KR1020130108891A
Other languages
Korean (ko)
Inventor
문기남
Original Assignee
주식회사 듀라테크
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 주식회사 듀라테크 filed Critical 주식회사 듀라테크
Priority to KR1020130108891A priority Critical patent/KR101388650B1/en
Application granted granted Critical
Publication of KR101388650B1 publication Critical patent/KR101388650B1/en

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/20Injection nozzles
    • B29C45/23Feed stopping equipment
    • 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
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/22Component parts, details or accessories; Auxiliary operations
    • B29B7/26Component parts, details or accessories; Auxiliary operations for discharging, e.g. doors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/0001Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor characterised by the choice of material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/76Measuring, controlling or regulating
    • B29C45/77Measuring, controlling or regulating of velocity or pressure of moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/76Measuring, controlling or regulating
    • B29C45/78Measuring, controlling or regulating of temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2945/00Indexing scheme relating to injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould
    • B29C2945/76Measuring, controlling or regulating
    • B29C2945/76494Controlled parameter
    • B29C2945/76498Pressure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2945/00Indexing scheme relating to injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould
    • B29C2945/76Measuring, controlling or regulating
    • B29C2945/76494Controlled parameter
    • B29C2945/76531Temperature
    • 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
    • B29K2075/00Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as moulding material

Abstract

Disclosed is an injection apparatus for mold urethane by which a fixed quantity of a urethane material defoamed after being completely mixed using a batch tank is supplied to an injection machine. The injection apparatus for mold urethane according to the present invention includes: an injection machine for injecting a molten solution into a mold; a fixed quantity injection part having a piston vertically moving in a cylinder, wherein an outlet of the cylinder is connected to an inlet of the injection machine via an outlet tube; a batch tank to which an inlet of the cylinder is coupled via an inlet tube and in which mold urethane is stored; an inlet opening/closing valve and an outlet opening/closing valve which are installed at the inlet tube and the outlet tube, respectively, and perform reciprocal opening or closing operations; and a controller for controlling the injection machine, the fixed quantity injection part, the batch tank, the inlet opening and closing valve, and the outlet opening and closing valve. The batch tank is filled with nitrogen in order to prevent properties of the mold urethane from being changed and provide a jet pressure of the mold urethane. [Reference numerals] (130) Controller

Description

주형 우레탄용 사출방법{An injection molding apparatus for urethane}Injection method for casting urethane {An injection molding apparatus for urethane}

본 발명은 주형 우레탄용 사출방법에 관한 것으로, 더욱 상세하게는 우레탄의 주재와 경화제가 섞일때에 빠르게 굳지 않도록 최근에 개발된 신재료를 이용하여 대량생산이 가능한 주형 우레탄용 사출방법에 관한 것이다.
The present invention relates to an injection method for molding urethane, and more particularly, to an injection method for molding urethane that can be mass-produced using a newly developed new material so as not to quickly solidify when the main body of urethane and the curing agent are mixed.

주형 우레탄은 일반적으로 원재와 경화제를 교반하여 주형하는 방식을 말한다.Molding urethane generally refers to a method of casting by stirring the raw material and the curing agent.

이와 같은 주형 우레탄의 원재료와 경화제는 적정온도(60 ~ 120도)로 예열된 금형에 교반후 pouring하는 방식으로, 작업가능시간(경화시간)은 1분에서 ~ 10분이 한계였다. 이는 정해진 온도가 아니더라도 원재료와 경화제가 교반할때에 반응이 일어나 경화됨으로써, 기존의 사출장비와 대량생산을 갖추려는 장비에서는 장비의 공급장치 라인의 경화문제 때문에 사용을 할 수가 없었던 문제가 있었다.The raw material and the curing agent of the mold urethane were stirred and poured into a mold preheated to an appropriate temperature (60 to 120 degrees), and the working time (curing time) was limited from 1 minute to 10 minutes. This reaction occurs when the raw material and the curing agent are stirred even though the temperature is not set, and there was a problem that the existing injection equipment and equipment to be equipped with mass production could not be used due to the hardening of the feeder line of the equipment.

따라서 주형용 우레탄 주형기를 이용하여 정해진 경화시간안에 금형에 붓는 방식이 현재까지의 작업방법이었으며, pulley및 oring 등은 열판프레스금형을 이용하여 정해진 경화시간안에 작업을 진행하는 것이었다. 그래서 주형용 우레탄제품은 대량생산이 불가하였고 또한 작업시마다 작업자의 작업능력이 물성에 중요변수 요인이었다.Therefore, the method of pouring the mold into the mold within the predetermined curing time using the urethane casting machine for casting was the work method up to now, and the pulley and the oring were performed in the predetermined curing time using the hot plate press mold. Therefore, the urethane product for casting was not mass-produced, and the worker's work ability was an important variable factor in the physical properties.

한편, 최근에 경화시간을 조절할 수 있는 우레탄이 출시되어 원재료와 경화제를 교반하여도 현재의 1 ~ 10분이 아닌 4 ~ 24시간동안 경화가 되지 않는 재료가 출시되었고, 이러한 재료를 이용하여 대량생산이 가능한 사출장비를 제작하는 것이 필요하게 되었다.On the other hand, the urethane that can control the curing time has recently been released, a material that does not cure for 4 to 24 hours instead of the current 1 to 10 minutes even after stirring the raw material and the curing agent has been released. There is a need to fabricate possible injection equipment.

사출장비란, 일반적으로는 PE, PP, PC 등의 플라스틱사출장치를 말하며, 이재료의 대부분은 열가소성수지이고 이것은 일액형 재료이다. 물론, 우레탄계열중에는 TPU도 있으나 이 재료도 일액형 재료로 정해진 온도로 녹여서 금형에 사출하는 방식일 뿐이다.Injection equipment generally refers to plastic injection devices such as PE, PP, and PC. Most of these materials are thermoplastic resins, which are one-component materials. Of course, there are also TPUs in the urethane series, but this material is only a one-component material that is melted at a predetermined temperature and injected into a mold.

플라스틱사출장치와 달리 LSR이라는 액상실리콘장비는 사출장비의 개념을 이용한 실리콘 사출성형장비로, 원재료와 경화제를 DOSING장비를 이용하여 장비에 공급 후 장비에 STATIC MIXER를 이용하여 교반 후 사출장비에 공급하는 방식이다. 이 실리콘사출장비는 외국에서는 이미 개발되어 판매되고 있으며 국내에서는 외국에서 수입하던것을 최근에는 국산화하여 납품하고 있는 시점이다.Unlike the plastic injection device, the liquid silicone equipment called LSR is a silicone injection molding equipment using the concept of injection equipment. It supplies raw materials and hardeners to the equipment by using the dosing equipment, and then supplies the equipment to the injection equipment after stirring by using the STATIC MIXER. That's the way. This silicone injection equipment has already been developed and sold in foreign countries, and it is now time to localize and supply what was imported from foreign countries in Korea.

이때, 플라스틱사출은 원재료 PALLET을 200 ~ 250도의 온도로 녹여서 스크류를 이용하여 용해시킨후 30 ~ 50도의 금형에 재료를 냉각시켜서 작업하는 방법이며, 이 재료는 열가소성수지로 제품을 다시 온도를 올릴시 재사용이 가능한 재료들이다.At this time, plastic injection is a method of melting raw material PALLET at a temperature of 200 to 250 degrees and dissolving it with a screw, and then cooling the material in a mold of 30 to 50 degrees. This material is a thermoplastic resin when the product is heated again. Reusable materials.

그리고 LSR은 플라스틱사출과 다른 개념으로, 상온의 원재료와 경화제를 장비 DOSING에 공급후 스텍틱믹서를 이용하여 교반후 스쿠류로 공급하여 150 ~ 200도의 금형에 경화시키는 방법이다. 플라스틱사출과는 온도차이라고 생각되나 반응하는 구조 및 화학식 전체가 전혀 다른 개념이다.And LSR is a different concept from plastic injection. It is a method of supplying raw materials and hardeners at room temperature to equipment dosing, and then stirring them using a static mixer to supply them to the scourers to cure them in molds of 150 to 200 degrees. Though it is considered to be a temperature difference from plastic injection, the reaction structure and chemical formula are completely different concepts.

그러나 위와 같은 플라스틱사출장비와 액상실리콘장비는 모두 주형용 우레탄의 사출에는 이용할 수 없었으며 현재의 장비를 구입하여 수정하는 것 역시 불가능한 것임을 알게 되었다. 즉, 우레탄 재료의 가장 중요한 온도관리 문제를 해결할 수 없었고, 믹싱 및 탈포가 완료된 우레탄은 40 ~ 70도의 금형에 들어가기 전까지 공기중의 수분과 노출이 되지 않아야 하며, 기포나 이물질이 절대로 발생하면 안되는 재료이기 때문이다. 또한, 기존의 플라스틱사출장비 및 액상실리콘장비보다 교반이 훨씬 정교해야하기 때문에 기존의 장비를 가지고는 주형 우레탄의 물성을 유지할 수 없는 문제가 발생되었다.However, both the plastic injection equipment and the liquid silicone equipment were not available for injection of the molding urethane, and it was found that it is impossible to purchase and modify the current equipment. That is, the most important temperature control problem of urethane material could not be solved, and the mixed and degassed urethane should not be exposed to moisture and air in the air until it enters the mold of 40 ~ 70 degrees, and bubbles or foreign substances should never occur. Because it is. In addition, since the stirring must be much more sophisticated than conventional plastic injection equipment and liquid silicone equipment, a problem arises that the physical properties of the cast urethane cannot be maintained with the existing equipment.

일부 유사하게나마 대한민국 공개특허 제10-2004-0019651호(2004.03.06. 공개)의 실리콘 성형제품 제조방법이 개시된바 있다. 이 공개특허는 도 1에서 보는 것과 같이, 액상의 실리콘 액(10) 및 경화제 액(20)을 펌핑하여 하나의 공급라인(P)으로 이송시키는 단계와, 이송되는 액상의 실리콘 액(10) 및 경화제 액(20)을 혼합기(24)를 통해 성형소재로 혼합하는 단계와, 혼합된 성형소재를 혼합기(24)를 통해 공급받아 저장실린더(30)내에 공급하는 단계와, 저장실린더(30)내에 공급된 성형소재를 금형에 공급하기 이전 냉각시키는 단계와, 저장실린더(30)의 일측에 설치된 유압실린더(32)의 전진 동작으로 성형소재를 금형(40) 내에 정량 충진시키는 단계와, 금형(40)에 공급된 성형소재를 성형하는 과정에서 소정의 온도로 가열하여 제품(A)의 형상으로 성형하는 단계 및 성형된 제품(A)을 취출한 후, 멸균처리 및 포장하는 단계 등으로 구성되어 있다.Some similarly disclosed is a method for producing a silicone molded product of Republic of Korea Patent Publication No. 10-2004-0019651 (published on June 6, 2004). This patent discloses a step of pumping a liquid silicone liquid 10 and a hardener liquid 20 to one supply line P, as shown in FIG. 1, and a liquid silicone liquid 10 to be transferred and Mixing the curing agent liquid 20 into the molding material through the mixer 24, receiving the mixed molding material through the mixer 24, and supplying the mixed molding material into the storage cylinder 30, and in the storage cylinder 30. Cooling the supplied molding material before supplying it to the mold, and quantitatively filling the molding material into the mold 40 by a forward operation of the hydraulic cylinder 32 installed at one side of the storage cylinder 30, and the mold 40 In the process of molding the molding material supplied to the) is heated to a predetermined temperature to form a shape of the product (A) and take out the molded product (A), and then sterilization and packaging and the like. .

따라서 발명자들은 위와 같은 실리콘 성형제품 제조방법의 사출장비를 이용하여 우레탄 재료를 피스톤에 공급하려고 하였으나, 상기 공개특허의 사출장비는 2액형으로 상온에서 작업이 가능하였으나, 새롭게 개발된 우레탄 재료는 상온에서 작업하는 것이 불가능 하기 때문이다.
Therefore, the inventors tried to supply the urethane material to the piston by using the injection equipment of the method for manufacturing a silicone molded product as described above, but the injection equipment of the disclosed patent was able to work at room temperature in a two-component type, but the newly developed urethane material was stored at room temperature. Because it is impossible to work.

본 발명은 상기와 같은 문제점을 해결하기 위해 안출된 것으로, 배치탱크를 이용하여 완벽하게 믹싱후 탈포된 우레탄 재료의 정량을 피스톤에 공급하도록 할 수 있는 주형 우레탄용 사출방법을 제공하려는 것이다.The present invention has been made to solve the above problems, it is to provide an injection method for casting urethane that can be supplied to the piston a quantity of the defoamed urethane material after mixing completely using a batch tank.

본 발명이 이루고자 하는 기술적 과제들은 이상에서 언급한 기술적 과제들로 제한되지 않는다.
The technical objects to be achieved by the present invention are not limited to the above-mentioned technical problems.

상기와 같은 과제를 해결하기 위해 본 발명은, 주재와 경화제를 배치탱크에 저장 한 후, 믹싱 및 탈포하여 주형 우레탄을 제조하는 단계(S10); 주형 우레탄을 정량주입부에 완충시키는 단계(S20); 정량주입부를 작동시켜 주형 우레탄을 사출기에 충진시키는 단계(S30); 및 사출기에 충진된 주형 우레탄을 금형 내로 인젝션하여 사출을 완료하는 단계(S40);를 포함하며, 단계(S10)에서부터 단계(S40)까지 에서는 열보온 유지장치에 의해 주형 우레탄이 섭씨 40~70도의 온도로 유지됨과 아울러 단계(S10)에서는 4~24시간 동안 상기 주형 우레탄이 보관된다.
구체적으로 단계(S10)에서의 주형 우레탄은 배치탱크 내로 충진된 질소의 압력에 의해 정량주입부로 주입되며, 질소의 압력은 2~7bar의 상대압력을 갖도록 충진된다.
구체적으로 단계(S20)에서의 정량주입부는, 실린더의 토출구가 사출기의 주입구로 토출관에 의해 연결되고, 실린더의 유입구가 유입관에 의해 배치탱크와 연결되며, 실린더에는 상하운동을 하는 피스톤 헤드 및 로드가 내장되며, 배치탱크에 저장된 주형 우레탄은 토출관에 장착된 토출개폐밸브를 폐쇄한 상태 하에서 유입관에 배치된 유입개폐밸브가 개방되면 피스톤 헤드 및 로드가 위로 올리면서 실린더 내로 충진된다.
구체적으로 단계(S30)에서의 주형 우레탄은, 유입개폐밸브를 폐쇄하고 토출개폐밸브를 개방한 상태 하에서 가압되는 로드 및 피스톤 헤드에 의해 사출기 내로 충진된다.
In order to solve the above problems, the present invention, after storing the main material and the curing agent in a batch tank, mixing and defoaming to prepare a mold urethane (S10); Buffering the urethane mold injection unit (S20); Filling the mold urethane into the injection molding machine by operating a fixed quantity injection unit (S30); And injecting the mold urethane filled into the injection molding machine into the mold (S40); and, from step S10 to step S40, the mold urethane is 40 to 70 degrees Celsius by a heat retaining device. In addition to maintaining the temperature in step (S10) the mold urethane is stored for 4 to 24 hours.
Specifically, the mold urethane in step (S10) is injected into the metering unit by the pressure of nitrogen filled into the batch tank, the pressure of nitrogen is filled to have a relative pressure of 2 ~ 7bar.
Specifically, the fixed-quantity injection unit in step S20, the discharge port of the cylinder is connected to the injection port of the injection machine by the discharge pipe, the inlet of the cylinder is connected to the batch tank by the inlet pipe, the piston head and the vertical movement in the cylinder and The rod is built-in, and the mold urethane stored in the batch tank is filled into the cylinder while the piston head and the rod are raised upward when the inlet / opening valve disposed in the inlet pipe is opened while the discharge opening / closing valve mounted on the discharge pipe is closed.
Specifically, the mold urethane in step S30 is filled into the injection molding machine by a rod and a piston head which are pressurized under the state in which the inlet opening and closing valve is closed and the discharge opening and closing valve is opened.

삭제delete

삭제delete

삭제delete

삭제delete

삭제delete

삭제delete

삭제delete

삭제delete

전술한 바와 같이 본 발명에 따른 주형 우레탄용 사출방법에 따르면 물성은 좋으나 환경적 변화에 민감한 신물질 우레탄을 제품의 대량생산이 가능하도록 제공할 수 있어 대량생산 및 품질균일문제가 끊임없이 발생하는 우레탄업계에서 대량생산체제인 장비의 도입이 가능하게 될 것이며, 주형용 우레탄이 대량생산이 불가하고 품질이 일정하지 못하다는 이유로 진입이 힘들었던 기존의 고무시장, 실리콘시장 또한, 물성이 좋지 않으나 대처가 불가하여 사용되던 일반사출시장의 진입이 가능하게 될 것이다.
As described above, according to the injection method for casting urethane according to the present invention, it is possible to provide a new material urethane which has good physical properties but sensitive to environmental changes, so that mass production of the product can be provided. It will be possible to introduce mass production equipment, and the existing rubber market and silicone market, which are difficult to enter due to the inability to mass-produce molds and inconsistent quality, also have poor physical properties but cannot be used. It will be possible to enter the general injection market.

도 1은 종래기술에 따른 액상실리콘사출장비를 나타낸 일예이고,
도 2는 본 발명에 따른 주형 우레탄 사출장비를 나타낸 도면이고,
도 3은 본 발명에 따른 주형 우레탄 사출장비의 정량주입부에 주형 우레탄이 주입된 상태를 보인 도면이며, 그리고
도 4는 본 발명에 따른 주형 우레탄 사출장비의 사출기에 주형 우레탄이 주입된 상태를 보인 도면이다.
1 is an example showing a liquid-silicon injection equipment according to the prior art,
Figure 2 is a view showing the molding urethane injection equipment according to the present invention,
3 is a view showing a state in which the cast urethane is injected into the metering injection portion of the injection molding machine urethane according to the present invention, and
Figure 4 is a view showing a state in which the molding urethane is injected into the injection molding machine of the injection molding machine urethane according to the present invention.

이하, 첨부된 도면을 참조하여 본 발명의 바람직한 실시 예를 상세하게 설명한다. 도면들 중 동일한 구성요소들은 가능한 어느 곳에서든지 동일한 부호로 표시한다. 또한 본 발명의 요지를 불필요하게 흐릴 수 있는 공지 기능 및 구성에 대한 상세한 설명은 생략한다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. In the drawings, the same components are denoted by the same reference symbols whenever possible. In the following description, well-known functions or constructions are not described in detail since they would obscure the invention in unnecessary detail.

도 2를 참고하면, 본 발명에 따른 주형 우레탄 사출장비(100)는 금형(20)에 주형 우레탄을 인젝션하기 위한 사출기(10)와, 이 사출기(10)에 정량의 주형 우레탄을 주입하기 위한 정량주입부(110)와, 이 정량주입부(110)에 주형 우레탄을 공급하기 위한 배치탱크(120)와, 이들을 콘트롤하는 제어부(130)를 포함하여 구성된다.Referring to FIG. 2, the mold urethane injection apparatus 100 according to the present invention includes an injection machine 10 for injecting a mold urethane into a mold 20, and a quantity for injection of a fixed amount of mold urethane into the injection machine 10. It comprises an injection unit 110, a batch tank 120 for supplying the mold urethane to the fixed-quantity injection unit 110, and a control unit 130 for controlling them.

금형(20) 및 사출기(10)는 사출분야의 당업자들이라면 누구나 다 알 수 있는 구성이므로 자세한 설명은 생략하기로 한다.Since the mold 20 and the injection machine 10 can be understood by anyone skilled in the art, detailed description thereof will be omitted.

정량주입부(110)는 피스톤의 상하작용으로 실린더(112)내에 주입된 주형 우레탄을 사출기(10)내로 주입해 주는 것으로, 실린더(112)에 내장된 피스톤 헤드(116)와, 이 피스톤 헤드(116)에 연결되어 실린더(112) 외부로 연장되는 로드(118)와, 실린더(112)의 하부로 주형 우레탄이 입출되는 유입구(113) 및 토출구(114)가 형성된 구성을 갖는다.The fixed quantity injection part 110 injects the molding urethane injected into the injection molding machine 10 into the injection molding machine 10 by the vertical action of the piston, and the piston head 116 embedded in the cylinder 112 and the piston head ( A rod 118 connected to the 116 and extending out of the cylinder 112, and an inlet 113 and an outlet 114 through which the mold urethane enters and exits the cylinder 112 are formed.

이러한 정량주입부(110)의 유입구(113)와 토출구(114)에는 각각 유입관(140) 및 토출관(150)이 결합되어, 유입관(140)은 주형 우레탄이 믹싱되어 저장되어 있는 배치탱크(120)와 연결되며, 토출관(150)은 사출기(10)의 주입구(11)와 연결된다.An inlet tube 140 and an outlet tube 150 are coupled to the inlet 113 and the outlet 114 of the fixed quantity injection unit 110, respectively, and the inlet tube 140 is a batch tank in which mold urethane is mixed and stored. It is connected to the 120, the discharge pipe 150 is connected to the injection port 11 of the injection machine 10.

이때, 유입관(140)과 토출관(150)에는 각각 유입개폐밸브(145) 및 토출개폐밸브(155)가 장착되어 주형 우레탄의 유입 및 토출을 제어하게 된다. 즉, 유입개폐밸브(145) 및 토출개폐밸브(155)는 서로 반대의 개폐작용을 하게 되면서 정량주입부(110)의 실린더(112)내에 정량의 주형 우레탄을 주입시키는가 하면, 주입된 정량의 주형 우레탄을 정량으로 사출기(10)내에 주입시킬 수 있게 되는 것이다. 보다 상세한 작용은 하기에 설명하기로 한다.In this case, the inlet and outlet valve 140 and the discharge tube 150 are respectively equipped with an inlet opening and closing valve 145 and a discharge opening and closing valve 155 to control the inlet and outlet of the casting urethane. That is, the inlet opening and closing valve 145 and the discharge opening and closing valve 155 are injecting and quantifying the mold urethane into the cylinder 112 of the metering injection unit 110 while opening and closing the opposite operation. Urethane is to be injected into the injection molding machine 10 in a quantitative manner. More detailed operation will be described below.

다음으로 배치탱크(120)는 주형 우레탄의 주재 및 경화제가 일정한 혼합비율을 갖도록 저장된 후에 교반믹서(122)에 의해 완벽한 믹싱 및 탈포가 된다. 이러한 배치탱크(120)는 열보온 유지장치(124)를 설치하여 국부적인 열에 노출시 우레탄의 물성변화가 발생하는 것을 방지할 수 있게 구성하였고, 수분과 공기중의 산소와 반응하여 경화되는 것을 방지하기 위하여 질소를 충진한다. 질소의 충진압력은 2BAR ~ 7BAR사이의 상대압력을 유지하는 것이 적당함을 여러 번의 실험을 통해 알게 되었다.Next, the batch tank 120 is completely mixed and defoamed by the stirring mixer 122 after the main body and the curing agent of the mold urethane are stored to have a constant mixing ratio. The batch tank 120 is configured to prevent the change in the physical properties of the urethane when exposed to the local heat by installing a heat retaining device 124, and prevents hardening by reacting with moisture and oxygen in the air Nitrogen is charged. Several experiments have shown that nitrogen filling pressure is appropriate to maintain a relative pressure between 2 and 7 bar.

이처럼 배치탱크(120)에 질소를 충진하는 이유는 질소가 재료의 물성의 변화 없이 유지하는 기능도 하지만, 질소압을 이용하여 주형 우레탄을 정량주입부(110)에 공급하도록 하기 위함이다. 따라서 이 배치탱크(120)는 지속적으로 고압을 유지하여 배치탱크(120)와 연결되는 유입관(140)의 유입개폐밸브(145)가 열릴때에 주형 우레탄을 정량주입부(110)에 완충할 수 있게 되는 것이다.The reason for filling nitrogen into the batch tank 120 is to maintain the nitrogen without changing the physical properties of the material, but to supply the mold urethane injection unit 110 using the nitrogen pressure. Therefore, the batch tank 120 maintains a high pressure to buffer the urethane in the injection molding unit 110 when the inlet opening and closing valve 145 of the inlet pipe 140 is connected to the batch tank 120 is opened. It will be possible.

한편, 주형 우레탄은 정해진 온도인 섭씨 40 ~ 70도(각재료별로 다름)에서 유지해야하는 이유로는, 주형 우레탄이 공급되면서 연결되는 본 발명의 주형 우레탄용 사출장비(100) 각부 모두에 열보온 유지장치를 설치하였으며, 히팅블럭 및 열보호 케이블 열매유를 이용하여 우레탄의 물성을 최대한 유지하도록 할 수 있다.On the other hand, the mold urethane must be maintained at a predetermined temperature of 40 to 70 degrees Celsius (different for each material), the thermal insulation holding device for all parts of the injection molding apparatus for injection molding urethane 100 of the present invention connected while the mold urethane is supplied It was installed, using the heating block and heat protection cable fruit oil can be maintained to maximize the physical properties of the urethane.

마지막으로, 제어부(130)는 배치탱크(120), 유입개폐밸브(145), 정량주입부(110), 토출개폐밸브(155) 및 사출기(10)를 각 조건에 따라 컨트롤한다. 즉, 배치탱크(120)내에 충진되어 있는 질소압이 기준치보다 낮거나 높을 경우 이를 제어하고, 사출의 흐름에 따라 유입개폐밸브(145) 및 토출개폐밸브(155), 정량유입부(110) 및 사출기(10)를 시간적 또는 센싱적으로 제어하게 되는 것이다.Finally, the controller 130 controls the batch tank 120, the inlet opening and closing valve 145, the metering injection unit 110, the discharge opening and closing valve 155 and the injection machine 10 in accordance with each condition. That is, when the nitrogen pressure filled in the batch tank 120 is lower or higher than the reference value, it is controlled, and the inlet opening and closing valve 145 and the discharge opening and closing valve 155, the fixed quantity inlet 110 and It is to control the injection machine 10 in a time or sensing manner.

하기에는 위와 같이 구성된 주형 우레탄 사출장비(100)의 작용을 도면을 참조하여 간략하게 설명한다.Hereinafter, the operation of the mold urethane injection device 100 configured as described above will be briefly described with reference to the drawings.

도 3 및 도 4는 배치탱크에 저장되어 있는 주형 우레탄이 사출기에 완충되기 가지의 흐름을 나타낸 도면이다.3 and 4 is a view showing the flow of the branch to be cast to the injection molding machine urethane stored in the batch tank.

우선, 전술한 바와 같이 주재 및 경화제가 일정한 혼합비율을 갖도록 저장한 후에 믹싱 및 탈포하여 주형 우레탄을 제조한다(단계 S10). 그리고 배치탱크(120) 내에 질소를 충진한다. 도 3을 참고하면, 전술한 바와 같이 배치탱크(120)에는 질소가 충전되어 있기 때문에, 배치탱크(120)에 저장되어 있는 주형 우레탄은 항상 배출될 준비를 하게 된다.
다음으로 배치탱크(120) 내에 주형 우레탄을 정량주입부(110)에 완충시킨다. 주형 우레탄의 배출은 유입개폐밸브(145)가 열리게 됨으로써, 자동으로 정량주입부(110)로 유입된다. 이때, 정량주입부(110)의 실린더(112)내에 주형 우레탄(U)이 정량으로 충진되기 위해서는 주형 우레탄(U)의 유입압에 의해 피스톤 헤드(116) 및 로드(118)가 위로 올라가야 하는데, 이를 위해서는 실린더(112)의 토출구(114)가 막혀져 있어야 가능하게 된다. 따라서 유입개폐밸브(145)가 열릴때에는 토출개폐밸브(155)가 닫히도록 제어되어 주형 우레탄(U)은 배치탱크(120)에서부터 정량주입부(110)의 피스톤이 최대로 승강한 상태의 실린더(112) 내부 및 토출개폐밸브(155) 전까지 완충되게 된다.
First, as described above, the main body and the curing agent are stored to have a constant mixing ratio, and then mixed and degassed to prepare a mold urethane (step S10). And nitrogen is filled in the batch tank 120. Referring to FIG. 3, since the batch tank 120 is filled with nitrogen as described above, the mold urethane stored in the batch tank 120 is always ready to be discharged.
Next, the mold urethane is buffered in the fixed quantity injection part 110 in the batch tank 120. The discharge of the casting urethane is automatically introduced into the metering injection unit 110 by opening the inlet opening and closing valve 145. At this time, in order to fill the mold urethane (U) in the cylinder 112 of the metered dose injection unit 110 in a quantitative manner, the piston head 116 and the rod 118 must be lifted up by the inflow pressure of the mold urethane (U). For this, the discharge port 114 of the cylinder 112 must be blocked. Therefore, when the inlet opening and closing valve 145 is opened, the discharge opening and closing valve 155 is controlled to be closed so that the mold urethane (U) is a cylinder in which the piston of the fixed quantity injection unit 110 is lifted up to the maximum from the batch tank 120 ( 112) the inner and the discharge opening and closing valve 155 is fully buffered.

이와 같이 정량주입부(110)에 주형 우레탄(U)이 완충되면, 다음으로 정량주입부(110)를 작동시켜 주형 우레탄(U)을 사출기(10)에 충진시킨다(단계 S30). 도 4에서 보는 것과 같이 상승한 로드(118)를 가압하여 실린더(112)내에 충진된 주형 우레탄(U)을 사출기(10)에 밀어 넣어준다. 이때, 주형 우레탄(U)이 사출기(10) 쪽으로 이송되기 위해서는 토출구(114)쪽이 열리고 유입구(113)쪽이 닫혀야 되므로, 유입개폐밸브(145)는 닫히면서 토출개폐밸브(155)는 열리도록 제어부(130)에서 컨트롤한다.When the molding urethane U is buffered in the metering injection unit 110 as described above, the metering injection unit 110 is operated to fill the molding urethane U in the injection machine 10 (step S30). As shown in FIG. 4, the urged rod 118 is pressed to push the mold urethane U filled in the cylinder 112 into the injection machine 10. At this time, in order for the mold urethane (U) to be transferred to the injection molding machine 10, the discharge port 114 must be opened and the inlet 113 must be closed, so that the inlet opening and closing valve 145 is closed while the discharge opening and closing valve 155 is opened. The control unit 130 to control.

사출기(10)로 충진된 주형 우레탄(U)은 금형(20)내로 인젝션되어 사출을 완료하게 된다(단계 S40).
여기서 주형 우레탄은 전술한 바와 같이 주형 우레탄(U)이 유통되는 각부에 장착된 열보온 유지장치에 의해 섭씨 40~70도의 온도가 유지되며, 이로 인해 배치탱크(120) 내의 주형 우레탄은 4~24시간 굳지 않고 보관된다.
The mold urethane U filled with the injection molding machine 10 is injected into the mold 20 to complete the injection (step S40).
As described above, the mold urethane is maintained at a temperature of 40 to 70 degrees Celsius by a heat retaining device mounted to each part through which the mold urethane (U) is distributed, and thus, the mold urethane in the batch tank 120 is 4 to 24 degrees. It is stored without time hardening.

위에서 설명된 실시 예들의 구성과 작동 방식에 한정되는 것이 아니다. 상기 실시 예들은 각 실시 예들의 전부 또는 일부가 선택적으로 조합되어 다양한 변형이 이루어질 수 있도록 구성될 수도 있다.
The present invention is not limited to the configuration and operation of the embodiments described above. The embodiments may be configured so that all or some of the embodiments may be selectively combined so that various modifications may be made.

100 : 주형 우레탄용 사출장비
10 : 사출기 20 : 금형
110 : 정량주입부 112 : 실린더
113 : 유입구 114 : 토출구
116 : 피스톤 헤드 118 : 로드
120 : 배치탱크 122 : 교반믹서
124 : 열보온 유지장치 130 : 제어부
140 : 유입관 145 : 유입개폐밸브
150 : 토출관 155 : 토출개폐밸브
100: Injection molding machine for casting urethane
10: injection molding machine 20: mold
110: fixed quantity injection unit 112: cylinder
113: inlet 114: outlet
116: piston head 118: rod
120: batch tank 122: stirring mixer
124: heat retaining device 130: control unit
140: inlet pipe 145: inlet opening and closing valve
150: discharge pipe 155: discharge opening and closing valve

Claims (6)

주재와 경화제를 배치탱크에 저장 한 후, 믹싱 및 탈포하여 주형 우레탄을 제조하는 단계(S10);
상기 주형 우레탄을 정량주입부에 완충시키는 단계(S20);
상기 정량주입부를 작동시켜 상기 주형 우레탄을 사출기에 충진시키는 단계(S30); 및
상기 사출기에 충진된 상기 주형 우레탄을 금형 내로 인젝션하여 사출을 완료하는 단계(S40);를 포함하며,
상기 단계(S10)에서부터 상기 단계(S40)까지 에서는 열보온 유지장치에 의해 상기 주형 우레탄이 섭씨 40~70도의 온도로 유지됨과 아울러 상기 단계(S10)에서는 4~24시간 동안 상기 주형 우레탄이 보관되는 것을 특징으로 하는 주형 우레탄용 사출방법.
After storing the casting material and the curing agent in a batch tank, mixing and defoaming to prepare a mold urethane (S10);
Buffering the mold urethane to the injection unit (S20);
Filling the mold urethane into an injection molding machine by operating the metering injection unit (S30); And
And injecting the mold urethane filled in the injection machine into a mold to complete injection (S40).
The mold urethane is maintained at a temperature of 40 to 70 degrees Celsius by the heat retaining device in the step S10 to the step S40, and the mold urethane is stored for 4 to 24 hours in the step S10. Injection molding method for casting urethane, characterized in that.
제 1 항에 있어서,
상기 단계(S10)에서의 상기 주형 우레탄은 상기 배치탱크 내로 충진된 질소의 압력에 의해 상기 정량주입부로 주입되며,
상기 질소의 압력은 2~7bar의 상대압력을 갖도록 충진되는 것을 특징으로 하는 주형 우레탄용 사출방법.
The method according to claim 1,
The mold urethane in the step (S10) is injected into the metering unit by the pressure of nitrogen filled into the batch tank,
The pressure of the nitrogen is injection method for molding urethane, characterized in that the filling to have a relative pressure of 2 ~ 7bar.
제 1 항에 있어서,
상기 단계(S20)에서의 상기 정량주입부는,
실린더의 토출구가 상기 사출기의 주입구로 토출관에 의해 연결되고, 상기 실린더의 유입구가 유입관에 의해 배치탱크와 연결되며, 상기 실린더에는 상하운동을 하는 피스톤 헤드 및 로드가 내장되며,
상기 배치탱크에 저장된 상기 주형 우레탄은 상기 토출관에 장착된 토출개폐밸브를 폐쇄한 상태 하에서 상기 유입관에 배치된 유입개폐밸브가 개방되면 상기 피스톤 헤드 및 로드가 위로 올리면서 상기 실린더 내로 충진되는 것을 특징으로 하는 주형 우레탄용 사출방법.
The method according to claim 1,
The metered dose injection unit in the step (S20),
The discharge port of the cylinder is connected to the injection port of the injection machine by the discharge pipe, the inlet of the cylinder is connected to the batch tank by the inlet pipe, the cylinder has a piston head and rod for vertical movement
The mold urethane stored in the batch tank is filled into the cylinder while the piston head and the rod are lifted up when the inlet / opening valve disposed in the inlet pipe is opened while the discharge opening / closing valve mounted to the discharge pipe is closed. Injection molding method for cast urethane characterized in that.
청구항 3에 있어서,
상기 단계(S30)에서의 상기 주형 우레탄은,
상기 유입개폐밸브를 폐쇄하고 상기 토출개폐밸브를 개방한 상태 하에서 가압되는 로드 및 피스톤 헤드에 의해 상기 사출기 내로 충진되는 것을 특징으로 하는 주형 우레탄용 사출방법.
The method of claim 3,
The mold urethane in the step (S30),
Injection method for the cast urethane, characterized in that the inlet opening and closing valve and the discharge opening and closing valve is opened in the injection molding machine by the rod and the piston head is pressurized.
삭제delete 삭제delete
KR1020130108891A 2013-09-11 2013-09-11 An injection molding apparatus for urethane KR101388650B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020130108891A KR101388650B1 (en) 2013-09-11 2013-09-11 An injection molding apparatus for urethane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020130108891A KR101388650B1 (en) 2013-09-11 2013-09-11 An injection molding apparatus for urethane

Publications (1)

Publication Number Publication Date
KR101388650B1 true KR101388650B1 (en) 2014-04-24

Family

ID=50658585

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020130108891A KR101388650B1 (en) 2013-09-11 2013-09-11 An injection molding apparatus for urethane

Country Status (1)

Country Link
KR (1) KR101388650B1 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180022959A (en) * 2015-07-03 2018-03-06 선더호프 엔지니어링 게엠베하 Devices in which liquid plastic components are supplied intermittently
KR102181368B1 (en) * 2019-12-31 2020-11-20 (주)오톡스 Injection Machine and Manufacturing Method for casting polyurethane
KR20220035724A (en) 2020-09-14 2022-03-22 (주)오톡스 Deviece for harden preventiing
WO2022092618A1 (en) * 2020-10-29 2022-05-05 (주)오톡스 Apparatus for injecting cast polyurethane
KR20230075906A (en) 2021-11-23 2023-05-31 주식회사 대신폴리텍 Apparatus for production of urethane moldings

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR0185006B1 (en) * 1995-03-29 1999-05-15 히로세 마꼬또 Manufacture of urethane reaction injection molding
JP2001150485A (en) * 1999-12-01 2001-06-05 Japan Steel Works Ltd:The Mechanism for adjusting flow rate of supercritical fluid
US20030057606A1 (en) * 2001-09-14 2003-03-27 Demag Ergotech Wiehe Gmbh Method and apparatus for injection molding multi-component mixtures
JP3649954B2 (en) * 1999-07-16 2005-05-18 株式会社日本製鋼所 Raw material preheating method and apparatus for injection molding machine

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR0185006B1 (en) * 1995-03-29 1999-05-15 히로세 마꼬또 Manufacture of urethane reaction injection molding
JP3649954B2 (en) * 1999-07-16 2005-05-18 株式会社日本製鋼所 Raw material preheating method and apparatus for injection molding machine
JP2001150485A (en) * 1999-12-01 2001-06-05 Japan Steel Works Ltd:The Mechanism for adjusting flow rate of supercritical fluid
US20030057606A1 (en) * 2001-09-14 2003-03-27 Demag Ergotech Wiehe Gmbh Method and apparatus for injection molding multi-component mixtures

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180022959A (en) * 2015-07-03 2018-03-06 선더호프 엔지니어링 게엠베하 Devices in which liquid plastic components are supplied intermittently
KR102050176B1 (en) * 2015-07-03 2019-11-28 선더호프 엔지니어링 게엠베하 Intermittent supply of liquid plastic components
US10960575B2 (en) 2015-07-03 2021-03-30 Henkel Ag & Co. Kgaa Device configured to intermittently supply a liquid plastic component
KR102181368B1 (en) * 2019-12-31 2020-11-20 (주)오톡스 Injection Machine and Manufacturing Method for casting polyurethane
KR102261932B1 (en) * 2019-12-31 2021-06-07 (주)오톡스 Injection Machine for casting polyurethane
KR20220035724A (en) 2020-09-14 2022-03-22 (주)오톡스 Deviece for harden preventiing
KR20220108751A (en) 2020-09-14 2022-08-03 (주)오톡스 Deviece for harden preventiing
WO2022092618A1 (en) * 2020-10-29 2022-05-05 (주)오톡스 Apparatus for injecting cast polyurethane
KR20220057384A (en) * 2020-10-29 2022-05-09 (주)오톡스 Injection Machine for casting polyurethane
KR102417278B1 (en) * 2020-10-29 2022-07-06 (주)오톡스 Injection Machine for casting polyurethane
KR20230075906A (en) 2021-11-23 2023-05-31 주식회사 대신폴리텍 Apparatus for production of urethane moldings

Similar Documents

Publication Publication Date Title
KR101388650B1 (en) An injection molding apparatus for urethane
CN102985245B (en) Mold-runner system having independently controllable shooting-pot assemblies
CN103831927B (en) Injection molding machine, injection molding system, and raw material metering unit
CN105216252B (en) Polymer mold manufacturing method and plastic member manufacturing method
KR101619887B1 (en) Injection Molding Machine Using Epoxy Resin
US7258543B2 (en) Vertical micro-injection machine
KR102362599B1 (en) Process and device for the production of reinforced plastics componetns
CN205522298U (en) High -precision injection mold
KR100979764B1 (en) A low pressure injection molding machine
CN105793003B (en) Equipment for polymerizeing lactams in a mold
JP2017538598A5 (en)
KR101601836B1 (en) Micro Injection Device
JP2012040839A (en) Injection molding machine for foaming
KR101579549B1 (en) How to neutralize the stench of amine gas for cold box process, and amine gas generator containing the same
KR101233233B1 (en) Silicone injection molding apparatus of barrel type
JP2004255588A (en) Method for controlling preplastication type injection molding machine
KR101582328B1 (en) Apparatus for feeding fixed amount of molten material using vacuum
JPH054254A (en) Different material composite injection molding equipment
KR102181368B1 (en) Injection Machine and Manufacturing Method for casting polyurethane
US20080299248A1 (en) Plastics injection molding machine
KR20230043574A (en) Thermosetting resin Injection device
CN100439077C (en) Upper metal die with injection tube mouth having heating line fixing slot
CN109906138A (en) The manufacturing method and manufacturing device of foam molding
CN108381849A (en) Injecting glue component and injection molding machine on injection device and injection molding forming method
IT202000009199A1 (en) IMPROVED INJECTION GROUP

Legal Events

Date Code Title Description
A201 Request for examination
A302 Request for accelerated examination
E902 Notification of reason for refusal
E90F Notification of reason for final refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20170320

Year of fee payment: 4

FPAY Annual fee payment

Payment date: 20180302

Year of fee payment: 5

FPAY Annual fee payment

Payment date: 20190221

Year of fee payment: 6

FPAY Annual fee payment

Payment date: 20200217

Year of fee payment: 7