KR20010076084A - Method manufacturing buoy with double structure - Google Patents
Method manufacturing buoy with double structure Download PDFInfo
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- KR20010076084A KR20010076084A KR1020000003504A KR20000003504A KR20010076084A KR 20010076084 A KR20010076084 A KR 20010076084A KR 1020000003504 A KR1020000003504 A KR 1020000003504A KR 20000003504 A KR20000003504 A KR 20000003504A KR 20010076084 A KR20010076084 A KR 20010076084A
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- KR
- South Korea
- Prior art keywords
- rich
- resin
- weight
- foam
- buoy
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 14
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 12
- 229920005989 resin Polymers 0.000 claims abstract description 21
- 239000011347 resin Substances 0.000 claims abstract description 21
- 239000006260 foam Substances 0.000 claims abstract description 18
- 238000005187 foaming Methods 0.000 claims abstract description 15
- -1 polypropylene Polymers 0.000 claims abstract description 15
- 229920001903 high density polyethylene Polymers 0.000 claims abstract description 12
- 239000004700 high-density polyethylene Substances 0.000 claims abstract description 12
- 239000004743 Polypropylene Substances 0.000 claims abstract description 10
- 239000005020 polyethylene terephthalate Substances 0.000 claims abstract description 10
- 229920000139 polyethylene terephthalate Polymers 0.000 claims abstract description 10
- 229920001155 polypropylene Polymers 0.000 claims abstract description 10
- 230000009977 dual effect Effects 0.000 claims abstract description 9
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 claims abstract description 8
- 239000004417 polycarbonate Substances 0.000 claims abstract description 8
- 239000004677 Nylon Substances 0.000 claims abstract description 7
- 229920001778 nylon Polymers 0.000 claims abstract description 7
- 229920000515 polycarbonate Polymers 0.000 claims abstract description 7
- 239000004800 polyvinyl chloride Substances 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims description 22
- 238000001125 extrusion Methods 0.000 claims description 11
- 229920001451 polypropylene glycol Polymers 0.000 claims description 10
- 229920005830 Polyurethane Foam Polymers 0.000 claims description 7
- 239000003054 catalyst Substances 0.000 claims description 7
- 239000011496 polyurethane foam Substances 0.000 claims description 7
- KIQKWYUGPPFMBV-UHFFFAOYSA-N diisocyanatomethane Chemical compound O=C=NCN=C=O KIQKWYUGPPFMBV-UHFFFAOYSA-N 0.000 claims description 4
- 239000003381 stabilizer Substances 0.000 claims description 4
- 239000004698 Polyethylene Substances 0.000 claims description 3
- 229920000573 polyethylene Polymers 0.000 claims description 3
- 229920002323 Silicone foam Polymers 0.000 claims description 2
- 239000013514 silicone foam Substances 0.000 claims description 2
- 229920002635 polyurethane Polymers 0.000 abstract description 13
- 239000004814 polyurethane Substances 0.000 abstract description 13
- 239000002699 waste material Substances 0.000 abstract description 10
- 241000251468 Actinopterygii Species 0.000 abstract description 8
- 229920000915 polyvinyl chloride Polymers 0.000 abstract description 4
- 229920005992 thermoplastic resin Polymers 0.000 abstract description 2
- XECAHXYUAAWDEL-UHFFFAOYSA-N acrylonitrile butadiene styrene Chemical compound C=CC=C.C=CC#N.C=CC1=CC=CC=C1 XECAHXYUAAWDEL-UHFFFAOYSA-N 0.000 abstract 2
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 abstract 2
- 229920006026 co-polymeric resin Polymers 0.000 abstract 1
- 230000035939 shock Effects 0.000 abstract 1
- 235000015170 shellfish Nutrition 0.000 description 9
- 239000000203 mixture Substances 0.000 description 6
- 238000003912 environmental pollution Methods 0.000 description 5
- 239000004794 expanded polystyrene Substances 0.000 description 5
- 241001474374 Blennius Species 0.000 description 4
- 239000004088 foaming agent Substances 0.000 description 4
- 229920006327 polystyrene foam Polymers 0.000 description 4
- 239000004604 Blowing Agent Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000003795 desorption Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- JOYRKODLDBILNP-UHFFFAOYSA-N urethane group Chemical group NC(=O)OCC JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 3
- SVYKKECYCPFKGB-UHFFFAOYSA-N N,N-dimethylcyclohexylamine Chemical compound CN(C)C1CCCCC1 SVYKKECYCPFKGB-UHFFFAOYSA-N 0.000 description 2
- 238000009360 aquaculture Methods 0.000 description 2
- 244000144974 aquaculture Species 0.000 description 2
- 238000009395 breeding Methods 0.000 description 2
- 230000001488 breeding effect Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229920005862 polyol Polymers 0.000 description 2
- 150000003077 polyols Chemical class 0.000 description 2
- 229920001296 polysiloxane Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- XWJBRBSPAODJER-UHFFFAOYSA-N 1,7-octadiene Chemical group C=CCCCCC=C XWJBRBSPAODJER-UHFFFAOYSA-N 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 229920005822 acrylic binder Polymers 0.000 description 1
- 238000012644 addition polymerization Methods 0.000 description 1
- 230000001588 bifunctional effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000012792 core layer Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 229920006248 expandable polystyrene Polymers 0.000 description 1
- 238000005429 filling process Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000009863 impact test Methods 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 150000003512 tertiary amines Chemical class 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- CYRMSUTZVYGINF-UHFFFAOYSA-N trichlorofluoromethane Chemical compound FC(Cl)(Cl)Cl CYRMSUTZVYGINF-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
- B29C44/02—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
- B29C44/12—Incorporating or moulding on preformed parts, e.g. inserts or reinforcements
- B29C44/18—Filling preformed cavities
- B29C44/188—Sealing off parts of the cavities
-
- 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
- B29C44/60—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/001—Combinations of extrusion moulding with other shaping operations
- B29C48/0012—Combinations of extrusion moulding with other shaping operations combined with shaping by internal pressure generated in the material, e.g. foaming
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/04—Polymers of ethylene
- B29K2023/06—PE, i.e. polyethylene
- B29K2023/0608—PE, i.e. polyethylene characterised by its density
- B29K2023/065—HDPE, i.e. high density polyethylene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2075/00—Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as moulding material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/706—Buoys
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
본 발명은 발포수지로 이루어진 부자의 제조방법에 관한 것으로서, 더욱 상세하게는 내구성이 우수한 고밀도 폴리에틸렌, 폴리프로필렌, 폴리카보네이트, 폴리에틸렌테레프탈레이트, 폴리비닐클로라이드, 나일론 및 ABS 수지 중에서 선택된 수지를 압출성형하여 부자의 외부재를 제작한 다음, 부자의 내부를 폴리우레탄으로 발포 충전하거나 발포수지 폐기물로 충전함으로써 이중구조의 부자를 제작하여, 종래 단일 발포체를 사용한 경우에 비해 표면의 고밀도로 인한 어패류의 탈리가 용이하고 부력 및 내구성이 우수하여 장기간 사용할 수 있도록 개선된 이중구조 부자의 제조방법에 관한 것이다.The present invention relates to a method for producing a rich man made of foamed resin, and more particularly, by extrusion molding a resin selected from high-density polyethylene, polypropylene, polycarbonate, polyethylene terephthalate, polyvinyl chloride, nylon and ABS resin with excellent durability After making the outer material of the rich, foamed filling of the rich with polyurethane or filling with foamed resin waste to produce the double structure of the rich structure, compared to the case of using a single foam, the desorption of fish and shellfish due to the high density of the surface The present invention relates to a method for producing a double-structured rich, which is easy and has excellent buoyancy and durability and can be used for a long time.
종래 사용되는 부자(buoy)는 주로 폴리스타이렌 발포체(expandable polystyrene, 이하 EPS)를 발포 가공하여 사용하고 있다. 그러나, 상기 EPS는 성형품의 융착력이 부족하여 사용도중 가벼운 충격이나 마찰로도 쉽게 파손될 우려가 있으며, 내용제성 및 내마찰성이 부족하여 쉽게 파손되고 잦은 교체로 인하여그 폐기물에 의한 2차 환경오염을 가져온다. 그리고, 마찰시 형상의 변형과 손상을 일으켜 어패류의 부착시 탈리가 불가능하고, 일부가 탈리된다고 하더라도 어패류에 부착된 부분으로 인한 환경오염이 더욱 심각해진다. 또한, 시간이 지남에 따라 부력이 저하되어 연 1 ∼ 2회의 완전교체가 필요하며, 어패류 부착으로 인하여 재사용이 불가능하다. 결과적으로 폐기시 폐기물에 의한 환경오염을 가져오고, 각종 해조류의 포자번식으로 쉽게 침식되어 파손되는 등 여러가지 폐단이 있었다.The conventionally used rich (buoy) is mainly used to foam the expanded polystyrene (expandable polystyrene, hereinafter EPS). However, the EPS may be easily damaged by light impact or friction during use due to insufficient adhesion of the molded product, and easily damaged due to lack of solvent resistance and friction resistance, and the secondary environmental pollution caused by the waste due to frequent replacement. Bring. In addition, deformation and damage of the shape during the friction is impossible to detach when attaching the shellfish, and even if some detachment, the environmental pollution due to the part attached to the shellfish becomes more serious. In addition, over time, buoyancy decreases, requiring one or two complete replacements per year, and reusability is impossible due to the attachment of fish and shellfish. As a result, there were various waste stages such as environmental pollution caused by waste at the time of disposal, and easily eroded and damaged by spore propagation of various seaweeds.
이에, 상기 문제점을 해결하고자 내구성이 EPS 보다 우수한 폴리에틸렌 및 폴리우레탄 등으로 단독 발포하여 부자를 제조하였다. 그러나, 이 또한 발포물 단면의 기공 때문에 내구성이 떨어지고 어패류의 탈리가 순조롭지 못하게 되는 단점이 있다. 이에 따라, 재사용이 불가능하며 고분자 단일 발포체만으로는 요구되는 성질을 충족시킬 수 없기에 이를 개선하기 위하여 부자의 표면 경도 및 고밀도가 요구되고 있는 실정이다.Thus, in order to solve the above problems, the foam was prepared by foaming alone with polyethylene and polyurethane having superior durability than EPS. However, this also has the disadvantage of poor durability due to the pores of the cross-section foam and the desorption of fish and shellfish is not smooth. Accordingly, the surface hardness and the high density of the rich are required to improve the reusability and the polymer single foam alone cannot satisfy the required properties.
종래 부자의 제조시 사용되는 폴리스타이렌 발포제는 내구성 및 어패류의 탈리가 용이하지 않고, 장기간 사용시 부력이 저하되는 문제점이 있다.Polystyrene foaming agents used in the manufacture of conventional rich has a problem that the durability and desorption of fish and shellfish is not easy, and the buoyancy is reduced during long-term use.
따라서, 본 발명에서는 내구성이 우수한 고밀도 폴리에틸렌, 폴리프로필렌, 폴리카보네이트, 폴리에틸렌테레프탈레이트, 폴리비닐클로라이드, 나일론 및 ABS 수지 중에서 선택된 수지를 압출성형을 거쳐 부자의 외부재를 제작한 다음, 부자의내부를 폴리우레탄으로 발포 충전하거나 폐기되는 발포수지를 충전함으로써, 내구성, 내충격성 및 내유성이 뛰어나고 어패류의 탈리가 용이하여 장시간 사용시에도 부력을 오랜동안 유지할 수 있으며, 이에 따른 폐기물의 오염을 극소화 할 수 있도록 개선된 이중구조 부자의 제조방법을 제공하는데 그 목적이 있다.Therefore, in the present invention, after the extrusion of a resin selected from high-density polyethylene, polypropylene, polycarbonate, polyethylene terephthalate, polyvinyl chloride, nylon and ABS resin with excellent durability to produce a rich external material, the inside of the rich By foaming or filling foamed polyurethane with polyurethane, it is excellent in durability, impact resistance and oil resistance, and can be easily detached from fish and shellfish to maintain buoyancy for a long time when using it for a long time, thereby minimizing waste contamination. It is an object of the present invention to provide a method for manufacturing a rich double-structured structure.
본 발명은 발포수지로 이루어진 부자의 제조방법에 있어서, 압출압력 2 ∼ 5 kg/㎠, 온도 190 ∼ 210℃로 고밀도 폴리에틸렌(HDPE), 폴리프로필렌(PP), 폴리카보네이트(PC), 폴리에틸렌테레프탈레이트(PET), 폴리비닐클로라이드(PVC), 나일론 및 ABS 수지 중에서 선택된 수지를 압출성형하여 두께 2 ∼ 4㎜인 부자의 외부재를 제작하는 공정과,The present invention is a method for producing a rich man made of foamed resin, high pressure polyethylene (HDPE), polypropylene (PP), polycarbonate (PC), polyethylene terephthalate at an extrusion pressure of 2 ~ 5 kg / ㎠, temperature 190 ~ 210 ℃ (PET), polyvinyl chloride (PVC), a process for producing a rich external material having a thickness of 2 to 4 mm by extrusion molding a resin selected from nylon and ABS resin,
폴리우레탄 발포체 또는 폐발포 수지를 발포밀도가 40 ∼ 60 kg/㎡이 되도록 상기 외부재에 충전시키고 밀봉시키는 공정으로 이중구조의 부자를 제조하는 것을 그 특징으로 하고 있다.It is characterized by producing a rich double structure by the step of filling the polyurethane foam or the waste foaming resin into the outer material so as to have a foam density of 40 to 60 kg / m 2.
이와 같은 본 발명을 더욱 상세하게 설명하면 다음과 같다.The present invention will be described in more detail as follows.
본 발명은 내구성이 우수한 열가소성 수지로 외부재를 제작하고, 내부를 폴리우레탄 및 폐발포 수지로 발포 충전하여 이중구조 부자를 제조함으로써 내구성, 내충격성 및 내유성이 우수하여 장시간 사용이 가능하고 어패류의 탈리가 용이하도록 개선된 이중구조 부자에 관한 것이다.The present invention is made of a thermoplastic resin having excellent durability, foamed filling the inside with polyurethane and waste foaming resin to produce a double structure rich, excellent durability, impact resistance and oil resistance can be used for a long time and detachment of fish and shellfish It is related to the dual structure rich improved to be easy.
먼저, 본 발명의 외부재로 사용되기 위해서는 장기간 사용이 가능해야 하므로 내구성 및 내유성이 우수하고, 각종 해조류의 포자 번식을 억제할 수 있는 고밀도의 수지로 사용하는 것이 바람직하다. 종래 부자로 사용되고 있는 폴리스타이렌 발포체(EPS)의 경우 충격강도가 0.6 ∼ 10 kgf·㎝/㎠ 로 파도 및 태풍에 의한 자체충돌시 부자가 쉽게 파괴되는 단점이 있었다. 이에, 본 발명에서는 고밀도 폴리에틸렌(HDPE), 폴리프로필렌(PP), 폴리카보네이트(PC), 폴리에틸렌테레프탈레이트(PET), 폴리비닐클로라이드(PVC), 나일론 및 ABS 수지 중에서 선택된 수지가 사용될 수 있으며, 그중 HDPE를 사용하는 것이 경제적인 면에서 바람직하다. 상기 HDPE 수지는 밀도 0.940 ∼ 0.965 g/㎤인 것으로, 부자의 외부재로 사용한 경우 표면이 고밀도로 인하여 매끄럽기 때문에 각종 해조류의 포자번식이 어렵다. 또한, 충격강도가 25 ∼ 40 kgf·㎝/㎠로 내구성, 내충격성 및 내유성이 우수한 특징이 있다.First, in order to be used as the external material of the present invention, it should be able to be used for a long time, so it is preferable to use it with a high density resin which is excellent in durability and oil resistance and can suppress spore propagation of various seaweeds. In the case of polystyrene foam (EPS), which is conventionally used as a rich man, the impact strength of 0.6 to 10 kgf · cm / cm 2 has a disadvantage in that the rich easily breaks during self-collision caused by waves and typhoons. Therefore, in the present invention, a resin selected from high density polyethylene (HDPE), polypropylene (PP), polycarbonate (PC), polyethylene terephthalate (PET), polyvinyl chloride (PVC), nylon and ABS resin may be used, among which The use of HDPE is economically desirable. The HDPE resin has a density of 0.940 to 0.965 g / cm 3, and when used as a rich external material, spore breeding of various seaweeds is difficult because the surface is smooth due to high density. In addition, the impact strength of 25 to 40 kgf · cm / ㎠ has the characteristics of excellent durability, impact resistance and oil resistance.
본 발명의 이중구조 부자의 외부재는 폴리우레탄 원료 주입구가 있는 형태로 제조하며, 그 제조방법은 압출공정이 가장 적당하고 이 분야에서 통상의 지식을 가진 자에 의해 적용될 수 있다. 본 발명의 외부재는 HDPE, PP, PC, PET, PVC, Nylon 및 ABS 수지 중에서 선택된 수지 100 중량부에 대하여 안료 2 ∼ 4 중량부를 첨가하여 일축압출기, 이축압출기 및 다륜스크류 압출기등의 일반적인 압출기에 적용시켜 사용할 수 있다. 이때, 압출압력은 2 ∼ 5 kg/㎠, 온도 190 ∼ 210℃의 범위내에서 수행하는 것이 바람직하다. 또한, 상기 압출공정을 통하여 제조된 부자의 외부재 두께는 2 ∼ 4㎜로, 이때 상기 두께가 2㎜보다 적으면 외부재로서 요구되는 내구성 및 내충격성의 물성이 저하되고, 4㎜ 보다 많으면 무게로 인한부력저하 및 원가상승으로 비경제적이어서 바람직하지 못하게 된다.The outer material of the dual structure rich of the present invention is manufactured in the form of a polyurethane raw material injection hole, the manufacturing method is the most suitable extrusion process and can be applied by those skilled in the art. The external material of the present invention is applied to a general extruder such as a single screw extruder, a twin screw extruder, and a multi-wheel screw extruder by adding 2 to 4 parts by weight of pigment to 100 parts by weight of a resin selected from HDPE, PP, PC, PET, PVC, Nylon and ABS resin. Can be used. At this time, the extrusion pressure is preferably carried out in the range of 2 ~ 5 kg / ㎠, temperature 190 ~ 210 ℃. In addition, the thickness of the outer material of the rich manufactured through the extrusion process is 2 ~ 4mm, wherein if the thickness is less than 2mm, the durability and impact resistance properties required as the external material is lowered, if more than 4mm by weight The buoyancy and cost increase caused by this are uneconomical and undesirable.
또한, 본 발명의 이중구조 부자의 내부를 충전하기 위하여 상기 제조된 외부재에 폴리우레탄 발포체 또는 폐발포 수지를 발포밀도가 20 ∼ 60 kg/㎡이 되도록 상기 외부재에 충전시키고 밀봉시키는 공정으로 이중구조의 부자를 제조한다.In addition, in order to fill the inside of the double-structure rich of the present invention, the polyurethane foam or waste foaming resin is filled in the outer material so as to have a foam density of 20 to 60 kg / ㎡ and sealed to the outer material prepared in the double To prepare the rich in the structure.
이러한 이중구조 부자의 내부 충전공정에 관하여 상기 2가지 방법을 더욱 구체적으로 설명하면 다음과 같다.The two methods for the internal filling process of the dual structure rich are described in more detail as follows.
일예로, 압출공정을 통하여 제조된 부자의 외부재에 폴리프로필렌 글리콜 100 중량부, 메틸렌디이소시아네이트 120 ∼ 180 중량부, 발포체 25 ∼ 35 중량부, 촉매 및 실리콘 정포제 5 ∼ 10 중량부를 주입하여 발포공정을 통해 폴리우레탄으로 충전하여 이중구조 부자를 제조한다.For example, 100 parts by weight of polypropylene glycol, 120 to 180 parts by weight of methylene diisocyanate, 25 to 35 parts by weight of foam, 5 to 10 parts by weight of catalyst and silicone foam stabilizer are injected into the external material of the rich manufactured through the extrusion process. Filling with polyurethane through the process to prepare the double-structure rich.
본 발명의 부자 내부를 충전하는 또 다른 방법으로, 폐기된 폴리스타이렌 발포체 또는 폴리우레탄 발포체를 각각 5 ∼ 10 ㎤ 크기로 분쇄하여 아크릴계 바인더로 처리하여 외부재로 주입한 다음, 외부재 및 주입구와의 공간에 폴리프로필렌 글리콜, 메틸렌디이소시아네이트, 발포체, 촉매 및 실리콘 증포제를 첨가하여 부자 내부를 충전하여 이중구조 부자를 제조한다.As another method of filling the rich inside of the present invention, the discarded polystyrene foam or polyurethane foam is crushed into 5 to 10 cm 3, respectively, treated with an acrylic binder and injected into an external material, followed by a space with an external material and an injection hole. Polypropylene glycol, methylene diisocyanate, foam, catalyst, and silicone thickener are added to the mixture to fill the rich interior to prepare a double structured rich.
본 발명의 폴리우레탄의 발포가공을 더욱 구체적으로 설명하면 다음과 같다.Referring to the foaming process of the polyurethane of the present invention in more detail as follows.
폴리우레탄의 발포가공은 활성 수산기(-OH)와 이소시아네이트(-N=C=O)의 부가 중합반응으로 우레탄기가 생성, 발포되어 폴리우레탄 폼이 형성된다. 본 발명의 폴리우레탄은 폴리올, 메틸렌디이소시아네이트, 촉매, 발포제 및 정포제를 함유시켜 발포가공을 한다.Polyurethane foam is produced by foaming urethane group by addition polymerization reaction of active hydroxyl group (-OH) and isocyanate (-N = C = O). The polyurethane of the present invention is foamed by containing polyol, methylene diisocyanate, catalyst, blowing agent and foam stabilizer.
먼저, 본 발명에서 사용되는 폴리올로는 주로 폴리프로필렌 글리콜(PPG)이 사용되는데, 상기 PPG는 양말단에 -OH기가 존재하는 2관능성으로, 중량평균분자량이 400 ∼ 2,000 인 것을 요구되는 물성에 따라 혼합하여 사용한다.First, the polyol used in the present invention is mainly used polypropylene glycol (PPG), the PPG is a bifunctional in which the -OH group is present at the sock end, the weight average molecular weight of 400 to 2,000 to the required physical properties Mix accordingly.
본 발명에 사용되는 디페닐메틴디아민(MDI)는 폴리머릭 MDI가 사용되고, 평균 관능기수가 2.3 ∼ 3.0으로 분자량은 360 ∼ 400 의 것이 사용된다. 본 발명에서 사용되는 함량은 PPG 100 중량부에 대하여 120 ∼ 180 중량부, 바람직하기로는 130 ∼ 160 중량부가 사용된다. 이때, 그 함량이 적은 경우 발포가 적어져 밀도가 높아 부력의 차이가 생기게 되고, 그 함량이 너무 많은 경우 발포체 표면이 부스러지는 현상을 나타내고 셀의 내구성이 떨어지게 되며, 외부재와의 접착력이 매우 떨어지게 되어 바람직하지 못하게 된다.As for diphenylmethinediamine (MDI) used for this invention, polymeric MDI is used, the average functional group number is 2.3-3.0, and the molecular weight 360-400 is used. The content used in the present invention is 120 to 180 parts by weight, preferably 130 to 160 parts by weight based on 100 parts by weight of PPG. At this time, if the content is small, the foaming is small and the density is high, so the difference of buoyancy is generated. If the content is too large, the surface of the foam is broken, the durability of the cell is decreased, and the adhesion to the external material is very poor. Becomes undesirable.
본 발명에서 사용되는 촉매로는 3급 아민(tertiary amine)이 사용되고, 각각 제품의 특성에 따라 두 종류 이상의 촉매를 조합하여 사용한다. 본 발명에서 사용되는 촉매로는 디메틸싸이클로헥실아민(dimethylcyclohexylamine, DMCHA) 및 테트라메틸렌디에틸렌(tetramethylenediethylene, TMHDA)이 사용된다. 본 발명에서 사용되는 함량은 PPG 100 중량부에 대하여 각각 5 ∼ 10 중량부 첨가하는데, 상기 함량보다 많거나 적은 경우 반응속도에 영향을 주어 반응 혼합물의 유동성과 폼 등 생성물의 표면/코어 층 형성 및 제품의 물성에 영향을 미치게 된다.Tertiary amine is used as the catalyst used in the present invention, and two or more kinds of catalysts are used in combination according to the characteristics of each product. As the catalyst used in the present invention, dimethylcyclohexylamine (DMCHA) and tetramethylenediethylene (TMHDA) are used. The content used in the present invention is added 5 to 10 parts by weight with respect to 100 parts by weight of PPG, respectively, if more or less than the content affects the reaction rate to form the surface / core layer of the product, such as fluidity and foam of the reaction mixture and This will affect the physical properties of the product.
본 발명에서 사용되는 발포제(blowing agent)는 고분자 반응 중 기포를 형성하고, 부자로 사용되기 위한 발포밀도 20 ∼ 60 ㎏/㎥을 제어하기 위해서 첨가된다. 상기 발포제는 통상적인 것으로 주로 불소계 화합물인 HCFC-14b 및 CFC 11등이 사용된다. 통상적으로는 발포는 물을 이용하여 수발포도 가능하나, 이러한 수발포의 경우 부자의 부력이 저하될 우려가 있다. 본 발명에서 사용되는 함량은 PPG 100 중량부에 대하여 25 ∼ 35 중량부가 첨가되며, 이때 그 함량이 상기의 범위에서 벗어나는 경우 요구되는 부자의 발포밀도에 영향을 주어 최적의 품질 조성에는 바람직하지 못하게 된다.The blowing agent used in the present invention is added to form bubbles during the polymer reaction and to control the foaming density of 20 to 60 kg / m 3 for use as rich. The blowing agent is conventional and mainly fluorine-based compounds such as HCFC-14b and CFC 11 are used. In general, the foaming may be water-foaming using water, but in the case of such water-foaming, there is a fear that the buoyancy of the rich is lowered. The content used in the present invention is added to 25 to 35 parts by weight based on 100 parts by weight of PPG, when the content is out of the above range affects the required foam density of the rich, which is undesirable for the optimal quality composition .
또한, 본 발명에서 사용되는 정포제(surfactant)로는 주로 실리콘 정포제를 사용한다. 상기 정포제는 원료의 혼합을 용이하게 하고, 우레탄 시스템의 표면장력을 낮추어 기포성장을 돕고, 발포시 충전성을 좋게 하여 제품밀도를 균일하게 하는 특징이 있다. 본 발명에서 사용되는 함량은 PPG 100 중량부에 대하여 0.5 ∼ 3 중량부이며, 이때 그 함량이 상기의 범위에서 벗어나는 경우 기포의 불안정성으로 인한 우레탄 셀이 균일하게 성장하지 못하게 된다.In addition, as the foaming agent (surfactant) used in the present invention, a silicone foaming agent is mainly used. The foam stabilizer is characterized by facilitating the mixing of the raw materials, lowering the surface tension of the urethane system to help bubble growth, and improve the fillability during foaming to uniform product density. The content used in the present invention is 0.5 to 3 parts by weight based on 100 parts by weight of PPG, in which case the urethane cells do not grow uniformly due to bubble instability when the content is out of the above range.
따라서, 상기의 조성 및 함량으로 제조된 이중구조 부자는 내구성이 우수하고, 부자로 사용되기 위한 발포밀도가 20 ∼ 60 ㎏/㎥인 부자를 제조할 수 있다. 본 발명에 의해 제조된 이중구조 부자의 수명은 종래 폴리스타이렌 발포체로 제조된 부자의 수명이 반년 ∼ 일년인 것에 비해 10 ∼ 20년 이상의 반영구적인 것으로 장기간 동안 사용이 가능하다. 또한, 이중구조 부자는 외부재의 수지의 고밀도성으로 인하여 표면이 매끄럽기 때문에 각종 해조류의 포자번식이 어렵고, 내구성, 내충격성 및 내유성이 우수하여 각종 양식업, 닻자망 어업 등의 어로작업에 아주 유용하게 사용될 수 있다.Therefore, the double-structured rich prepared with the above composition and content is excellent in durability, it is possible to produce a rich with a foam density of 20 to 60 kg / ㎥ for use as a rich. The lifespan of the dual structure rich according to the present invention is semipermanent for 10 to 20 years or more as compared to the life span of the rich made of the conventional polystyrene foam is half a year to one year, and can be used for a long time. In addition, due to the high-density of the resin of the external material, the double structure is difficult to spore breeding of various seaweeds, and has excellent durability, impact resistance and oil resistance, and is very useful for fishing operations such as aquaculture, anchor net fishing, etc. Can be used.
특히, 부자의 내부를 충전하기 위하여 폐기된 폴리스타이렌 발포체 및 폴리우레탄 발포체를 사용함으로써 폐기물을 재활용을 도모할 수 있으며, 이에 따른 2차적인 환경오염을 억제할 수 있다.In particular, by using the discarded polystyrene foam and the polyurethane foam to fill the inside of the rich, waste can be recycled, thereby suppressing secondary environmental pollution.
한편, 상기의 조성 성분들을 이용하여 본 발명의 폴리우레탄 발포제를 제조하는 방법이 특별히 한정되는 것은 아니며, 이 분야에서 통상적인 지식을 가진 자에 의해 쉽게 제조될 수 있다.On the other hand, the method for producing the polyurethane foaming agent of the present invention using the above composition components is not particularly limited, it can be easily prepared by those skilled in the art.
또한, 본 발명의 이중구조 부자는 용도에 따라 그 크기나 형태를 여러 가지로 변화시켜 제조할 수 있다.In addition, the dual structure of the present invention can be produced by varying the size and shape of the various in accordance with the use.
이하 본 발명을 실시예에 의거하여 더욱 상세히 설명하겠는바, 본 발명이 실시예에 의해 한정되는 것은 아니다.Hereinafter, the present invention will be described in more detail with reference to Examples, but the present invention is not limited by Examples.
실시예 1 ∼ 6 및 비교예 1 ∼ 3Examples 1-6 and Comparative Examples 1-3
부자의 길이방향 47 mm, 지름 37 mm 및 두께 2.5 mm의 외부재를 고밀도 폴리에틸렌 수지를 사용하여 압출강도 3 kg/㎠, 온도 210 ℃에서 압출가공하여 제조하였다.An outer material having a length of 47 mm, a diameter of 37 mm, and a thickness of 2.5 mm of the rich was prepared by extrusion processing using a high density polyethylene resin at an extrusion strength of 3 kg / cm 2 and a temperature of 210 ° C.
다음 표 1의 조성에 따라 상기 제조된 외부재에 폴리우레탄 원료를 주입하여 발포 충전하여 이중구조 부자를 제조하였다. 상기 제조된 이중구조 부자의 물성을 다음과 같은 방법으로 측정였으며, 그 결과를 나타내었다.Next, according to the composition of Table 1, the polyurethane material was injected into the prepared outer material and foam-filled to prepare a double structure rich. The physical properties of the prepared double structure was measured by the following method, and the results are shown.
(1) 내한 시험: 충진 완료후 냉동실에서 -25℃로 감온하여 24시간 후 5m 높이에서 낙하하여 내부 및 외부의 균열 및 파열 유무를 관찰하였다.(1) Cold resistance test: After the filling was completed, the temperature was reduced to -25 ° C in the freezer compartment, and after 24 hours, it was dropped at a height of 5m and observed for cracks and ruptures inside and outside.
(2) 충격 시험: 충진 완료후 10kgh 빔을 5m 높이에서 수평으로 낙하하여 내부 및외부의 균열 및 파열 유무를 관찰하였다.(2) Impact test: After the filling was completed, the 10 kgh beam was dropped horizontally at a height of 5 m to observe the presence of cracks and breaks inside and outside.
(3) 내열 시험 : 충진 완료후 열탕(70 ∼ 80℃)에 침적하여 10시간 후 내부 및 외부의 변형을 관찰하였다.(3) Heat test: After completion of filling, it was immersed in boiling water (70-80 ° C.) to observe internal and external deformation after 10 hours.
이상에서 설명한 바와 같이, 본 발명에 따른 이중구조의 부자는 내구성, 내충격성 및 내유성이 우수하여 장시간 사용이 가능하다. 또한, 태풍, 파도 및 부자끼리의 자체 충격에 의한 손상이 적고, 어패류의 탈리가 용이하여 재사용이 가능함에 따라 2차적인 환경오염 예방이 가능할 뿐만 아니라, 시간에 따른 부력 저하가 적으므로 양식업 등에 유용하게 사용할 수 있다.As described above, the rich of the dual structure according to the present invention is excellent in durability, impact resistance and oil resistance can be used for a long time. In addition, it is less damaged by typhoons, waves, and self-impact between each other, and it is easy to remove the fish and shellfish, so it is possible to prevent secondary environmental pollution as well as to reduce buoyancy over time, which is useful for aquaculture. Can be used.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101155877B1 (en) * | 2012-03-05 | 2012-06-20 | 김고명 | Environmentally friendly method for manufacturing buoys |
KR20180034801A (en) * | 2016-09-28 | 2018-04-05 | 주식회사 세기종합환경 | Floatable object and method of manufacturing the same |
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2000
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101155877B1 (en) * | 2012-03-05 | 2012-06-20 | 김고명 | Environmentally friendly method for manufacturing buoys |
KR20180034801A (en) * | 2016-09-28 | 2018-04-05 | 주식회사 세기종합환경 | Floatable object and method of manufacturing the same |
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