KR20010084127A - High efficiency·high press injection head bundle - Google Patents
High efficiency·high press injection head bundle Download PDFInfo
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- KR20010084127A KR20010084127A KR1020000009960A KR20000009960A KR20010084127A KR 20010084127 A KR20010084127 A KR 20010084127A KR 1020000009960 A KR1020000009960 A KR 1020000009960A KR 20000009960 A KR20000009960 A KR 20000009960A KR 20010084127 A KR20010084127 A KR 20010084127A
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- mixing head
- mixing
- mixing chamber
- high pressure
- efficiency
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/76—Mixers with stream-impingement mixing head
- B29B7/7663—Mixers with stream-impingement mixing head the mixing head having an outlet tube with a reciprocating plunger, e.g. with the jets impinging in the tube
- B29B7/7668—Mixers with stream-impingement mixing head the mixing head having an outlet tube with a reciprocating plunger, e.g. with the jets impinging in the tube having a second tube intersecting the first one with the jets impinging in the second tube
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/76—Mixers with stream-impingement mixing head
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/76—Mixers with stream-impingement mixing head
- B29B7/7631—Parts; Accessories
- B29B7/7636—Construction of the feed orifices, bores, ports
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/76—Mixers with stream-impingement mixing head
- B29B7/7663—Mixers with stream-impingement mixing head the mixing head having an outlet tube with a reciprocating plunger, e.g. with the jets impinging in the tube
- B29B7/7684—Parts; Accessories
- B29B7/7689—Plunger constructions
- B29B7/7694—Plunger constructions comprising recirculation channels; ducts formed in the plunger
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/3442—Mixing, kneading or conveying the foamable material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/36—Feeding the material to be shaped
- B29C44/365—Feeding the material to be shaped using elongate feed conduits provided with throttle devices
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
본 발명은 폴리우레탄(Polyurethane) 발포기의 믹싱헤드 뭉치에 관한 것으로 폴리올과 이소시아네이트를 고압분사시켜 혼합실(Mixing Chamber)에서와류와 난류에 의해 균질하게 혼합된 후 협류(Throttle)를 통과하면서 토출관(Outlet Pipe)에서는 층류유동이 되어 금형에 혼합물을 주입하여 고품질의 폴리우레탄 포옴을 제작하기 위한 것이다.The present invention relates to a mixing head bundle of a polyurethane foaming machine, and to a high pressure spray of polyol and isocyanate, homogeneously mixed by vortex and turbulence in a mixing chamber, and then passing through a throttle. (Outlet Pipe) is a laminar flow to inject a mixture into a mold to produce high quality polyurethane foam.
폴리우레탄 폼 제품의 제조 방법에는 저압 발포방식과 고압 발포방식으로 대별되며 저압 발포방식은 원료를 저압으로 노즐을 통하여 혼합실에 공급한 후 임펠러(Impeller)를 고속으로 회전시켜 혼합한 후 몰드(Mold)에 주입하는 방식으로 세척, 원료손실, 작업환경 열악, 품질 생산성 저하 등 경제, 환경적인 요인으로 인하여 이 방식은 점차적으로 감소, 고압발포기로 대체되고 있다. 한편 고압 발포방식은 원료를 노즐을 통하여 고압으로 분사하여 충돌력(Impingement Force)에 의해 혼합한 후 몰드에 주입하는 방식이다. 고압 발포기의 구성은 원료 탱크(Tank) 및 펌프(Pump), 믹싱 헤드 뭉치와 구동 유압 장치, 전기 전자 제어장치로 구성되며 특히 믹싱 헤드 뭉치는 원료를 혼합하여 주입하는 기구로 발포 제품의 품질을 결정하는 가장 핵심이 되는 제품이다.Polyurethane foam products are classified into low pressure foaming method and high pressure foaming method. Low pressure foaming method supplies raw materials to the mixing chamber at low pressure through a nozzle, rotates the impeller at high speed, and then molds the mold. This method is gradually reduced and replaced by high pressure foaming machine due to economic and environmental factors such as cleaning, loss of raw materials, poor working environment, and poor productivity. On the other hand, the high pressure foaming method is a method of injecting the raw material at a high pressure through the nozzle to be mixed by the impact force (Impingement Force) and injected into the mold. The composition of high pressure foaming machine is composed of raw material tank and pump, mixing head bundle and driving hydraulic system, and electric and electronic control device. Especially, mixing head bundle mixes and injects raw materials to improve the quality of foam products. It's the key to deciding.
종래에는 수평 또는 수직의 단일방향 분사방식으로 믹싱효율이 떨어지거나, 혼합실(Mixing Chamber) 이외에도 별도의 와류실(Swirl Chamber) 또는 부가 장치를따로 두어 믹싱효율, 출구에서의 층류유동을 개선하고자 하였으나 구조의 복잡으로 인한 유지 및 보수의 어려움, 장비의 고가화, 수명의 저하 등의 단점이 있었다.Conventionally, the mixing efficiency is decreased by horizontal or vertical unidirectional spraying method, or a separate swirl chamber or an additional device is provided in addition to the mixing chamber to improve the mixing efficiency and laminar flow at the outlet. Difficulties in maintenance and repair due to the complexity of the structure, expensive equipment, and reduced lifespan.
따라서, 상기한 바와 같은 문제점을 해결하기 위한 본 발명의 목적은 항상 고품질의 폴리우레탄 폼을 제작할 수 있는 2중 각도 분사방식에 의한 고효율·고압 믹싱헤드뭉치를 제공함에 있다.Accordingly, an object of the present invention for solving the problems as described above is to provide a high-efficiency, high-pressure mixing head bundle by a double angle injection method that can always produce a high-quality polyurethane foam.
상기한 바와 같은 목적을 달성하기 위하여 믹싱헤드(1)에서의 폴리올과 이소시아네이트의 고압 분사 시 믹싱효율을 개선하기 위하여 폴리올과 이소시아네이트의 분사노즐(4)을 수직·수평방향의 2중 경사각도로 형성하였다.In order to achieve the above object, in order to improve the mixing efficiency of the polyol and isocyanate at high pressure of the mixing head 1, the injection nozzle 4 of the polyol and the isocyanate was formed at a double inclination angle in the vertical and horizontal directions. .
제 1 도는 본발명의 믹싱헤드뭉치의 종단면도.1 is a longitudinal cross-sectional view of a mixing head bundle of the present invention.
제 2 도는 제 1 도에서의 원료흐름도.2 is a raw material flow diagram in FIG.
제 3 도는 제 1 도의 A-A선 부위의 수평단면도 및 원료흐름도.3 is a horizontal sectional view and a raw material flow diagram of the line A-A of FIG.
제 4 도는 제 3 도의 B-B선 부위의 수직단면도 및 원로 흐름도.4 is a vertical cross-sectional view of the line B-B in FIG.
제 5 도는 종래 제품의 수직 및 수평단면도에서의 원료흐름도.5 is a raw material flow diagram in the vertical and horizontal cross-sectional view of the conventional product.
<도면의 주요부분에 대한 부호의 설명><Description of the symbols for the main parts of the drawings>
1: 몸체 2: 토출관1: body 2: discharge tube
3: 믹싱챔버피스톤 4: 분사노즐3: mixing chamber piston 4: spray nozzle
5: 혼합실 6: 크리닝 피스톤5: mixing chamber 6: cleaning piston
7: 스로틀(Throttle) 조절장치7: Throttle Control
8: 실린더 커버 9: 스페이서 튜브8: cylinder cover 9: spacer tube
10: 이형윤활유 공급유로 11: 이형윤활유 공급실10: Release lubricant supply flow path 11: Release lubricant supply room
12-1,12-2,12-3: 저마찰 탄성체 스크레이퍼12-1,12-2,12-3: low friction elastomer scraper
가: 노즐위치 나: 원료의 1차 충돌A: Nozzle position B: Primary collision of raw material
다: 원료의 2차 충돌 라: 협류C: secondary collision of raw materials
이하 본 발명의 바람직한 실시예의 상세한 설명이 첨부된 도면들을 참조하여 설명될 것이다. 또한 본 발명을 설명함에 있어, 공지 기능 혹은 구성에 대한 구체적인 설명이 본 발명의 요지를 불필요하게 흐릴 수 있다고 판단되는 경우에는 그 상세한 설명을 생략할 것이다. 그리고 후술되는 용어들은 본 발명에서의 기능을 고려하여 정의 내려진 용어들로서 이는 사용자 혹은 설계자의 의도 또는 관례 등에 따라 달라질 수 있으므로, 그 정의는 본 명세서 전반에 걸친 내용을 토대로 내려져야 할 것이다.DETAILED DESCRIPTION A detailed description of preferred embodiments of the present invention will now be described with reference to the accompanying drawings. In describing the present invention, when it is determined that a detailed description of a known function or configuration may unnecessarily obscure the subject matter of the present invention, the detailed description thereof will be omitted. In addition, the terms to be described below are terms defined in consideration of functions in the present invention, and may be changed according to the intention or custom of a user or a designer, and the definitions should be made based on the contents throughout the present specification.
본 발명은 믹싱헤드(1)에 유압탱크와 폴리올 및 이소시아네이트 연결관 등을 연결한 상태(도시하지 않았음)에서 유압탱크의 펌프를 작동하면 유압 작동유에 의해 크리닝 피스톤(6)이 후진 한 뒤 믹싱 챔버 피스톤(3)이 후진하게 되어 믹싱 헤드 몸체(1)와 믹싱 챔버 피스톤(3)에 의해 혼합실(5)가 형성됨과 동시에 2중 각도의 분사노즐(4)이 열리면서 폴리올과 이소시아네이트가 고압(120∼200bar)으로 분사된다.According to the present invention, when the hydraulic tank and the polyol and isocyanate connecting pipes are connected to the mixing head 1 (not shown), when the pump of the hydraulic tank is operated, the cleaning piston 6 is reversed by the hydraulic oil and then mixed. The chamber piston (3) is reversed to form the mixing chamber (5) by the mixing head body (1) and the mixing chamber piston (3), and at the same time the injection nozzle (4) of the double angle is opened, the polyol and isocyanate are high pressure ( 120 to 200 bar).
고압 분사된 폴리올과 이소시아네이트는 혼합실(5) 내에서 강한 1차 충돌(가)을 하며 이는 다시 혼합실 벽면에 2차충돌(나)하면서 충돌에너지에 의해 매우 혼란한 1차 와류를 형성하고, 누즐구멍위치를 통과하면서 2차 와류 형성 및 난류 유동을 하고 크리닝 피스톤(6)에 의하여 형성된 협류(峽流)저항에 의해 혼합실(5)에서 최상의 혼합을 이루고, 이렇게 혼합된 혼합물은 협류(라)를 지나 토출관(2)을 통과하면서 자연스러운 층류유동이 되어 몰드에 주입된다. 필요량이 몰드에 주입되면 믹싱챔버 피스톤(3)이 전진하고 원료는 탱크로 순환되어 크리닝 피스톤(6)이 전진하면서 믹싱헤드 내부의 혼합 잔류물을 몰드로 깨끗이 주입한다.High pressure sprayed polyols and isocyanates have a strong primary impact in the mixing chamber 5 which in turn causes secondary collisions on the wall of the mixing chamber, forming a primary vortex which is very confused by the collision energy. Secondary vortex formation and turbulent flow are performed while passing through the nozzle hole position, and the best mixing in the mixing chamber 5 is achieved by the narrowing resistance formed by the cleaning piston 6, and the mixed mixture thus becomes Passing through the discharge pipe 2 and passing through) becomes natural laminar flow and injected into the mold. When the required amount is injected into the mold, the mixing chamber piston 3 is advanced and the raw material is circulated to the tank so that the cleaning piston 6 is advanced to cleanly inject the mixing residue inside the mixing head into the mold.
본 발명에서는 믹싱헤드(1)에서의 폴리올과 이소시아네이트의 고압분사 시 믹싱효율을 개선하기 위하여 폴리올과 이소시아네이트의 분사노즐(4)을 수직·수평방향의 2중 경사각도로 형성한 것이 특징이다. 이로 인해 고압 분사되는 폴리올과 이소시아네이트는 강한 1, 2차의 2단충돌에 의해 와류 및 난류발생을 매우 원활하게 하여 혼합실(5) 공간 전체가 와류 및 난류혼합 공간이 되어 균질한 최상의 혼합으로 인해 폴리우레탄 폼의 품질을 향상시킬 수 있도록 설계되어 있다. 뿐만 아니라 실린터 커버(8)에 스로틀 조절장치(7)를 부착하여 크리닝 피스톤(6)에 의해 협류(라)를 형성하고, 협류(라)에 의한 저항으로 혼합실(5)에서는 와류 및 난류유동이 활발해지고 협류(라)를 통과한 혼합물은 토출관(2)에서 그 흐름이 보다 부드러운 층류유동이 이루어 지도록 설계되어졌다.In the present invention, in order to improve the mixing efficiency during high pressure injection of the polyol and isocyanate in the mixing head 1, the injection nozzle 4 of the polyol and isocyanate is formed at a double inclination angle in the vertical and horizontal directions. As a result, the polyol and isocyanate that are injected at a high pressure make vortices and turbulence very smooth by strong first and second stage collisions, and the entire mixing chamber 5 becomes the vortex and turbulent mixing space, resulting in the best homogeneous mixing. It is designed to improve the quality of polyurethane foam. In addition, the throttle adjusting device 7 is attached to the cylinder cover 8 to form a narrow flow (d) by the cleaning piston (6), and vortex and turbulent flow in the mixing chamber (5) due to the resistance caused by the narrowed flow (d). The mixture which became active and passed through the narrow flow (d) was designed to have a laminar flow which is smoother in the discharge pipe (2).
또한 크리닝 피스톤(6)과 믹싱챔버 피스톤(3)이 몸체(1, Housing)와 고착하는 현상을 방지하기 위하여 이 부위에 이형윤활유(DOP, TOTM등)를 공급하기 위한 유로(10)를 형성하고, 혼합물, 이형윤활유 등이 미소틈새로 유출하는 현상을 방지하기 위한 저마찰 탄성 스크래이퍼(12-1,12-2,12-3)를 설치하였다.Also, in order to prevent the cleaning piston 6 and the mixing chamber piston 3 from sticking to the body 1, a flow path 10 for supplying release lubricant (DOP, TOTM, etc.) is formed in this area. Low friction elastic scrapers 12-1, 12-2, and 12-3 for preventing the outflow of the mixture, the lubricating oil, and the like into the micro gaps were provided.
상술한 바와 같이 본 발명은 믹싱헤드 뭉치내의 폴리올과 이소시아네이트를 고압 분사 시 분사노즐의 수평·수직의 2중 경사각으로 인해 강한 충돌력에 의한 와류 및 난류현상으로 인해 혼합실(5) 내의 믹싱효율을 개선시키고, 크리닝 피스톤(6)의 스로틀 조절장치(7)로 혼합실에서는 믹싱효율을 개선하고 토출관(2)에서는 원활한 층류유동이 되어져 고품질의 폴리우레탄 폼을 제작할 수 있다.As described above, the present invention improves the mixing efficiency in the mixing chamber 5 due to the vortex and turbulence caused by the strong collision force due to the double inclination angle of the horizontal and vertical of the injection nozzle when the polyol and isocyanate in the mixing head bundle are injected under high pressure. In addition, the throttle control device 7 of the cleaning piston 6 improves the mixing efficiency in the mixing chamber, and smooth laminar flow in the discharge pipe 2 can be used to produce high-quality polyurethane foam.
스페이서 튜브(9)에 채워진 이형윤활유(DOP, TOTM 등)는 자중에 의해 유로(10)를 지나 크리닝 피스톤(6)과 믹싱챔버 피스톤(3)의 표면에 이형윤활막을 형성하여 이형윤활막의 혼합물의 고착을 최대한 방지하여 제품의 수명연장을 꾀하며, 저마찰 탄성체 스크래이퍼(12-1, 2, 3)는 밀봉(Sealing)작용과 베어링 작용을 동시에 수행하여 청결한 작업환경을 유지하고 원료의 손실을 방지할 수 있다.Release lubricant (DOP, TOTM, etc.) filled in the spacer tube (9) passes the flow path (10) by its own weight to form a release lubricant film on the surface of the cleaning piston (6) and the mixing chamber piston (3) of the mixture of the release lubricant film In order to prevent seizure as much as possible, the life of the product is extended, and the low friction elastomer scraper 12-1, 2, 3 performs sealing and bearing at the same time to maintain a clean working environment and prevent the loss of raw materials. Can be.
Claims (3)
Priority Applications (1)
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KR10-2000-0009960A KR100368178B1 (en) | 2000-02-23 | 2000-02-23 | High efficiency·high press injection head bundle |
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KR10-2000-0009960A KR100368178B1 (en) | 2000-02-23 | 2000-02-23 | High efficiency·high press injection head bundle |
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KR20010084127A true KR20010084127A (en) | 2001-09-06 |
KR100368178B1 KR100368178B1 (en) | 2003-01-24 |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2004004879A1 (en) * | 2002-07-03 | 2004-01-15 | Yong Chae Jeong | Mixing head assembly with double-angled injection nozzle |
KR101353564B1 (en) * | 2012-11-15 | 2014-01-22 | 한국생산기술연구원 | Mixing head having enhanced mixing performance and discharging apparatus of the same |
KR101413514B1 (en) * | 2013-06-21 | 2014-07-02 | 한국생산기술연구원 | Mixing head having enhanced mixing performance |
KR101458613B1 (en) * | 2013-09-30 | 2014-11-11 | (주) 디유티코리아 | High-pressure mixing head with injection nozzle fixed by horizontal-vertical double angle of inclination |
FR3110869A1 (en) * | 2020-06-02 | 2021-12-03 | Dut Korea Co., Ltd | MIXING HEAD UNIT WITH HIGH MIXING EFFICIENCY |
Families Citing this family (5)
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KR101348268B1 (en) | 2012-09-07 | 2014-01-10 | 주식회사 우레아텍 | Spacer tube of mixing head for discharger |
KR101676486B1 (en) * | 2016-05-13 | 2016-11-15 | (주)이스턴에프티씨 | Foam Mixing Head having a Calibration |
KR101882670B1 (en) * | 2017-09-14 | 2018-07-27 | (주)에이아이엠텍 | Polyurethane foaming mixing head for promulgation correction of deformities by using ultrasonic |
KR102028039B1 (en) * | 2019-02-19 | 2019-10-02 | (주)이스턴에프티씨 | Foam Mixing Head device having a cleaning function |
KR20220158313A (en) | 2021-05-24 | 2022-12-01 | (주) 디유티코리아 | Mixing head unit with dynamic mixer |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1214531B (en) * | 1986-09-25 | 1990-01-18 | Afros Spa | HIGH PRESSURE MIXING EQUIPMENT. |
US5498151A (en) * | 1993-05-05 | 1996-03-12 | Nennecker; Gunter H. | Mixing head for molding machine |
-
2000
- 2000-02-23 KR KR10-2000-0009960A patent/KR100368178B1/en not_active IP Right Cessation
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004004879A1 (en) * | 2002-07-03 | 2004-01-15 | Yong Chae Jeong | Mixing head assembly with double-angled injection nozzle |
KR101353564B1 (en) * | 2012-11-15 | 2014-01-22 | 한국생산기술연구원 | Mixing head having enhanced mixing performance and discharging apparatus of the same |
KR101413514B1 (en) * | 2013-06-21 | 2014-07-02 | 한국생산기술연구원 | Mixing head having enhanced mixing performance |
KR101458613B1 (en) * | 2013-09-30 | 2014-11-11 | (주) 디유티코리아 | High-pressure mixing head with injection nozzle fixed by horizontal-vertical double angle of inclination |
FR3110869A1 (en) * | 2020-06-02 | 2021-12-03 | Dut Korea Co., Ltd | MIXING HEAD UNIT WITH HIGH MIXING EFFICIENCY |
Also Published As
Publication number | Publication date |
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KR100368178B1 (en) | 2003-01-24 |
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