KR100809667B1 - Water blowned polyurethane composition having very low density and method for preparing the same - Google Patents
Water blowned polyurethane composition having very low density and method for preparing the same Download PDFInfo
- Publication number
- KR100809667B1 KR100809667B1 KR1020060101291A KR20060101291A KR100809667B1 KR 100809667 B1 KR100809667 B1 KR 100809667B1 KR 1020060101291 A KR1020060101291 A KR 1020060101291A KR 20060101291 A KR20060101291 A KR 20060101291A KR 100809667 B1 KR100809667 B1 KR 100809667B1
- Authority
- KR
- South Korea
- Prior art keywords
- weight
- water
- average
- low density
- parts
- Prior art date
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
- C08L75/04—Polyurethanes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
- C08G18/4205—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups
- C08G18/4208—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups
- C08G18/4211—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups derived from aromatic dicarboxylic acids and dialcohols
- C08G18/4213—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups derived from aromatic dicarboxylic acids and dialcohols from terephthalic acid and dialcohols
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4829—Polyethers containing at least three hydroxy groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0061—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof characterized by the use of several polymeric components
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
- C08J9/125—Water, e.g. hydrated salts
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/49—Phosphorus-containing compounds
- C08K5/51—Phosphorus bound to oxygen
- C08K5/52—Phosphorus bound to oxygen only
- C08K5/521—Esters of phosphoric acids, e.g. of H3PO4
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L71/00—Compositions of polyethers obtained by reactions forming an ether link in the main chain; Compositions of derivatives of such polymers
- C08L71/02—Polyalkylene oxides
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Polyurethanes Or Polyureas (AREA)
Abstract
Description
제1도는 실시예 1에서 제조된 수발포 폴리우레탄 폼 시편의 전자현미경 사진이다. 1 is an electron micrograph of the water-foamed polyurethane foam specimen prepared in Example 1. FIG.
제2도는 연질 폴리우레탄 폼 시편의 전자현미경 사진이다. 2 is an electron micrograph of a flexible polyurethane foam specimen.
제3도는 경질 폴리우레탄 폼 시편의 전자현미경 사진이다. 3 is an electron micrograph of a rigid polyurethane foam specimen.
발명의 분야Field of invention
본 발명은 초저밀도 수발포 폴리우레탄 조성물 및 그 제조 방법에 관한 것이다. 보다 구체적으로, 본 발명은 특정 폴리올 혼합물에 촉매제 및 정포제를 혼합하고, 발포제로 물을 사용한 레진프리믹스를 메틸렌 디페닐 디이소시아네이트(이하, MDI)계 이소시아네이트와 반응시켜 형성되는 초저밀도 수발포 폴리우레탄 조성물에 관한 것이다. The present invention relates to an ultra low density water-foaming polyurethane composition and a method for producing the same. More specifically, the present invention provides an ultra low density foamed polyurethane formed by mixing a catalyst and foam stabilizer with a specific polyol mixture and reacting a resin premix using water as a blowing agent with a methylene diphenyl diisocyanate (hereinafter referred to as MDI) -based isocyanate. It relates to a composition.
발명의 배경Background of the Invention
폴리우레탄은 냉동창고, 단열주택, 선박 내부 등을 비롯하여 각종 건축물의 단열 시공을 위한 재료로서 사용되어 오고 있다. Polyurethane has been used as a material for insulation construction of various buildings, including refrigerated warehouses, insulated houses, ships.
일반적으로 폴리우레탄 폼은 이소시아네이트 용액과 폴리올 용액을 일정한 비율로 혼합하여 발포하여 제조되며, 통상 발포제로 프레온류인 클로로 플루오로카본(Chlorofluoro Carbon, CFC)류가 사용되어 왔다. 그러나, CFC를 발포제로 사용할 경우, 오존층 파괴 및 지구 온난화 등의 문제를 유발하여 근래 이들의 사용량을 규제하고 있으며, 화재발생시 유독가스를 방출하는 문제점이 있다. In general, the polyurethane foam is prepared by mixing the isocyanate solution and the polyol solution in a fixed ratio and foaming. Freon chloro fluorocarbons (CFCs), which are commonly used as blowing agents, have been used. However, when CFC is used as a blowing agent, it causes problems such as ozone layer destruction and global warming, and has recently regulated their usage, and there is a problem of toxic gas emission in case of fire.
이에 따라 발포제를 펜탄 등과 같은 하이드로 카본을 적용하는 방법도 제안되었으나, 폭발 등의 위험이 있으며, 폭발 방지를 위한 막대한 시설투자비가 발생하는 또 다른 문제점이 있다. Accordingly, a method of applying a hydrocarbon such as pentane as a blowing agent has also been proposed, but there is a risk of explosion, and another problem of enormous facility investment cost for preventing explosion.
이러한 문제점을 해소하기 위해 최근에는 물을 사용한 수발포 우레탄 폼 제조가 꾸준히 연구되고 있다. 그러나 물을 발포제로 사용할 경우, 프레온을 사용할 때보다 열전도율, 강도, 접착력 등의 물성이 전반적으로 저하되어 적용이 어렵다는 단점이 있다. In order to solve this problem, the manufacture of water-foaming urethane foam using water has been steadily studied in recent years. However, when water is used as a blowing agent, the physical properties such as thermal conductivity, strength, adhesive strength, etc. are generally lowered than when using freon, so that it is difficult to apply.
국내특허 제391550호에서는 300~500mgKOH/g인 폴리에스테르 폴리올과 폴리에테르폴리올을 혼합하여 조성되고 혼합후 관능기가 2~5이고 수산기 값이 200~500mgKOH/g인 혼합폴리올을 적용한 경질 폴리우레탄 폼을 개시하고 있다.In Korean Patent No. 391550, a rigid polyurethane foam is prepared by mixing a polyester polyol having a concentration of 300 to 500 mgKOH / g and a polyether polyol, and applying a mixed polyol having a functional group of 2 to 5 and a hydroxyl value of 200 to 500 mgKOH / g after mixing. It is starting.
국내등록특허 제316326호에서는 관능기가 2~4이고 분자량이 300~800인 폴리에스테르폴리올과 관능기가 3~6이고 분자량이 300~800인 폴리에테르폴리올인 혼합 폴리올, 가교제, 실리콘 오일 등을 적용하여 스프레이용 저밀도 폴리우레탄 발포체 조성물을 개시하고 있다. In Korea Patent No. 316326, a polyester polyol having a functional group of 2 to 4 and a molecular weight of 300 to 800 and a mixed polyol, a crosslinking agent, a silicone oil, etc., which is a polyether polyol having a functional group of 3 to 6 and a molecular weight of 300 to 800 A low density polyurethane foam composition for spraying is disclosed.
국내등록특허 제561806호에서는 2~6의 평균 관능기와 30~200㎎KOH/g의 평균 수산기를 갖는 폴리에테르폴리올과 폴리옥시프로필렌글리콜에 폴리옥시에틸렌글리콜이 10~50중량% 캡핑된 폴리에테르폴리올, 카르복실류, 저분자량 에스테르 중 선택된 1종과 글리콜의 축합반응으로 얻어진 방향족 폴리에스테르폴리올을 적용한 스프레이용 저밀도 폴리우레탄 발포체 조성물을 개시하고 있다. In Korean Patent No. 561806, a polyether polyol having 10 to 50 wt% of polyoxyethylene glycol capped in a polyether polyol and a polyoxypropylene glycol having an average functional group of 2 to 6 and an average hydroxyl group of 30 to 200 mgKOH / g A low-density polyurethane foam composition for spraying is applied to an aromatic polyester polyol obtained by condensation reaction of one selected from carboxyl groups and low molecular weight esters with glycols.
일반적으로 폴리우레탄은 연질, 경질 등으로 분류되며, 연질 폴리우레탄폼은 도 2에 나타난 바와 같이 개방형 셀(Open Cell) 구조를 가짐으로써 빠르게 공기가 이동하고 수증기의 침투가 가능한 구조로 되어 있다. 따라서, 통기성이 좋고, 배합처방에 따른 광범위한 비중과 다양한 물성을 조절할 수 있으며, 양호한 쿠션성, 기계적 강도(신율, 인장강도, 내마모성)을 갖는 장점이 있다. 반면, 경질 폴리우레탄 폼은 도 3에 나타난 바와 같이 하나 하나의 셀이 모두 닫혀있어, 셀 간의 공기의 이동이나 수증기의 이동이 완전히 차단된 구조로 열전도율이 매우 낮아 단열재로써의 응용될 수 있다. In general, polyurethane is classified into soft, hard, and the like, and the flexible polyurethane foam has an open cell structure, as shown in FIG. 2, to allow air to move quickly and to penetrate water vapor. Therefore, it has good air permeability, can control a wide range of specific gravity and various physical properties according to the formulation, and has an advantage of having good cushioning property and mechanical strength (elongation, tensile strength, and wear resistance). On the other hand, the rigid polyurethane foam, as shown in Figure 3 all one cell is closed, the movement of air between the cells or the movement of water vapor is completely blocked structure can be applied as a heat insulating material is very low.
본 발명에서는 이러한 셀 구조에 따라 발현되는 특징에 착안하여 특수한 셀 구조를 갖는 우레탄 폼을 개발하였다. 즉, 닫혀진 셀로 연결된 연속기포이면서 각 셀 간의 수증기의 이동이 가능하도록 약간의 열린 셀이 존재하도록 할 경우, 수증 기는 연속기포 속으로 서서히 침투하게 되고 침투된 수증기는 낮은 수증기압을 가지는 기포속으로 서서히 확산을 하게 된다. 연속기포는 확산과 분산이 되는 그 특이한 구조 때문에 역학적으로 안정한 수증기압의 균형을 유지할 수 있고, 매우 조밀한 구조를 가지는 수천 수만 개의 셀이 단열재 내에서 공기가 대류하는 것을 어렵게 만들기 때문에 결로 방지 및 단열이 가능할 것이다. In the present invention, the urethane foam having a special cell structure was developed based on the features expressed according to the cell structure. In other words, if there are continuous cells connected to closed cells and some open cells exist to allow the movement of water vapor between each cell, the water vapor slowly penetrates into the continuous bubble and the water vapor gradually diffuses into the bubble having low water vapor pressure. Will be Because of their unique structure of diffusion and dispersion, continuous bubbles can balance mechanically stable water vapor pressures, and tens of thousands of cells with very dense structures make it difficult for convection of air in the insulation. It will be possible.
따라서, 본 발명자는 이를 위하여 특정 폴리올 혼합물에 촉매제 및 정포제를 혼합하고, 이를 물로 발포시킴으로써, 기존 우레탄폼의 장점인 우수한 단열성능과 접착성 등의 물성을 유지하면서 발포력이 대폭 향상시킨 환경친화적인 초저밀도 수발포 폴리우레탄 조성물 및 그 제조방법을 개발하기에 이른 것이다.Therefore, the present inventors, for this purpose, by mixing the catalyst and foam stabilizer in a specific polyol mixture, and foaming it with water, environmentally friendly foaming ability significantly improved while maintaining the properties such as excellent heat insulation performance and adhesiveness of the advantages of the existing urethane foam Phosphorus ultra-low density water-foamed polyurethane composition and a method for producing the same have been developed.
본 발명의 목적은 닫혀진 셀로 연결된 연속기포이면서 각 셀간의 수증기의 이동이 가능하도록 약간의 열린 셀이 존재하는 초저밀도 수발포 폴리우레탄 조성물을 제공하기 위한 것이다.An object of the present invention is to provide an ultra-low density water-foaming polyurethane composition which is a continuous bubble connected to a closed cell and there are some open cells to allow the movement of water vapor between each cell.
본 발명의 다른 목적은 화학 발포제가 아닌 물로 발포시킴으로써, 냄새가 거의 없고 화재발생시 유독가스를 방출하지 않는 환경친화적인 초저밀도 수발포 폴리우레탄 조성물을 제공하기 위한 것이다.Another object of the present invention is to provide an environmentally friendly ultra low density foamable polyurethane composition which is foamed with water rather than a chemical blowing agent, thereby having little odor and releasing toxic gases in the event of a fire.
본 발명의 또 다른 목적은 우수한 단열성능과 접착성이 뛰어난 초저밀도 수발포 폴리우레탄 조성물을 제공하기 위한 것이다.Still another object of the present invention is to provide an ultra low density water-foaming polyurethane composition having excellent heat insulating performance and adhesion.
본 발명의 또 다른 목적은 발포력이 대폭 향상된 초저밀도 수발포 폴리우레 탄 조성물을 제공하기 위한 것이다.Still another object of the present invention is to provide an ultra low density foamed polyurethane composition having greatly improved foaming force.
본 발명의 또 다른 목적은 우수한 단열 및 결로방지 효과로 인해 에너지 절감 효과를 얻을 수 있어 경제성이 우수한 초저밀도 수발포 폴리우레탄 조성물을 제공하기 위한 것이다.Still another object of the present invention is to provide an ultra-low density foamed polyurethane composition having excellent economic efficiency due to energy saving effect due to excellent heat insulation and anti-condensation effect.
본 발명의 또 다른 목적은 시공성이 뛰어난 초저밀도 수발포 폴리우레탄 조성물을 제공하기 위한 것이다.Still another object of the present invention is to provide an ultra low density foamable polyurethane composition having excellent workability.
본 발명의 또 다른 목적은 물로 발포시킴으로써, 원재료의 단가도 낮출 수 있는 초저밀도 수발포 폴리우레탄 조성물을 제공하기 위한 것이다.Another object of the present invention is to provide an ultra low density water-foaming polyurethane composition which can lower the unit cost of raw materials by foaming with water.
본 발명의 또 다른 목적은 차음흡음성이 우수한 초저밀도 수발포 폴리우레탄 조성물을 제공하기 위한 것이다.Another object of the present invention is to provide an ultra low density water-foaming polyurethane composition excellent in sound insulation.
본 발명의 상기 및 기타의 목적들은 하기에 설명되는 본 발명에 의하여 모두 달성될 수 있다. 이하 본 발명의 내용을 하기에 상세히 설명한다.The above and other objects of the present invention can be achieved by the present invention described below. Hereinafter, the content of the present invention will be described in detail.
발명의 요약Summary of the Invention
본 발명의 초저밀도 수발포 폴리우레탄 조성물은 (A)(a)평균 관능기가 2∼6이며, 300∼600 mgKOH/g의 평균 수산기를 가진 수크로스계 폴리에테르 폴리올 10 내지 40 중량%, (b) 평균 분자량이 200~800인 글리콜에테르 중합체 5~30 중량%, (c) 평균 관능기 수가 2∼5이며, 평균 수산기가 50∼200 mgKOH/g인 폴리에테르 폴리올 5 내지 30 중량%, 및 (d) 무수프탈산에 에틸렌 산화물과 프로필렌 산화물을 첨가중합하여 제조된 폴리에스테르 폴리올 10 내지 40 중량%로 이루어진 폴리올 혼합물 80 내지 90 중량부; (B) 물로 이루어진 발포제 3 내지 15 중량부; (C) 아민계 촉매제 0.0001 내지 10 중량부; 및 (D) 정포제 0.0001 내지 5 중량부로 이루어진 레진 프리믹스에 반응제로 MDI계 이소시아네이트를 NCO/OH비율이 1.0 내지 1.4로 혼합된 것이다. Ultra low density water-foaming polyurethane composition of the present invention (A) (a) 10 to 40% by weight of sucrose-based polyether polyol having an average functional group of 2 to 6, having an average hydroxyl group of 300 to 600 mgKOH / g, (b 5-30 wt% of a glycol ether polymer having an average molecular weight of 200-800, (c) 5-30 wt% of a polyether polyol having an average number of functional groups of 2-5, and an average hydroxyl group of 50-200 mgKOH / g, and (d 80 to 90 parts by weight of a polyol mixture consisting of 10 to 40% by weight of a polyester polyol prepared by adding and polymerizing ethylene oxide and propylene oxide to phthalic anhydride; (B) 3 to 15 parts by weight of the blowing agent consisting of water; (C) 0.0001 to 10 parts by weight of the amine catalyst; And (D) MDI isocyanate is mixed in a resin premix consisting of 0.0001 to 5 parts by weight of the foam stabilizer in an NCO / OH ratio of 1.0 to 1.4.
본 발명의 하나의 구체예에서는 상기 아민계 촉매제는 디메틸에탄올 아민(DMEA), 디메틸시클로헥실아민(DMCHA), 트리에틸렌디아민(TEDA), 펜타메틸디에틸렌트리아민(PMDETA), 트리에탄올아민(TEA), 트리스(3-디메틸아미노)프로필헥사하이드로트리아민 테트라 메틸렌 헥실디아민 (TMHDA), 트리프로필아민, 모노에탄올아민, 트리부틸아민. 트리옥틸아민, 헥사데실디메틸아민, N-메틸몰포린, N-에틸몰포린, N-옥타데실몰포린, 트리이소프로판올 아민, 비스디메틸아미노에틸에테르 및 이들의 혼합물로 선택된다. In one embodiment of the present invention, the amine catalyst is dimethylethanol amine (DMEA), dimethylcyclohexylamine (DMCHA), triethylenediamine (TEDA), pentamethyldiethylenetriamine (PMDETA), triethanolamine (TEA) , Tris (3-dimethylamino) propylhexahydrotriamine tetra methylene hexyldiamine (TMHDA), tripropylamine, monoethanolamine, tributylamine. Trioctylamine, hexadecyldimethylamine, N-methylmorpholine, N-ethylmorpholine, N-octadecylmorpholine, triisopropanol amine, bisdimethylaminoethylether and mixtures thereof.
본 발명의 다른 구체예에서는 상기 정포제는 폴리실록산 에테르이다. In another embodiment of the invention the foam stabilizer is a polysiloxane ether.
상기 레진 프리믹스는 트리스(2-클로로프로필)포스페이트(TCPP), 트리스(2-클로로에틸)포스페이트(TCEP) 및 트리크레실 포스페이트로 이루어진 군으로부터 선택된 난연제를 3 내지 30 중량부 더 포함할 수 있다. The resin premix may further include 3 to 30 parts by weight of a flame retardant selected from the group consisting of tris (2-chloropropyl) phosphate (TCPP), tris (2-chloroethyl) phosphate (TCEP) and tricresyl phosphate.
상기 MDI계 이소시아네이트는 평균 작용기 2.5 이상이며, 고분자형인 4,4'-디페닐메탄 디이소시아네이트인 것을 특징으로 한다.The MDI isocyanate has an average functional group of 2.5 or more, and is characterized in that the polymer type 4,4'-diphenylmethane diisocyanate.
본 발명에서는 초저밀도 수발포 폴리우레탄 폼의 제조방법을 제공한다. 상기 방법은 (a)평균 관능기가 2∼6이며, 300∼600 mgKOH/g의 평균 수산기를 가진 수크 로스계 폴리에테르 폴리올 10 내지 40 중량%, (b) 평균 분자량이 200~800인 글리콜에테르 중합체 5~30 중량% (c) 평균 관능기 수가 2∼5이며, 평균 수산기가 50∼200 mgKOH/g인 폴리에테르 폴리올 5 내지 30 중량%, 및 (d) 무수프탈산에 에틸렌 산화물과 프로필렌 산화물을 첨가중합하여 제조된 폴리에스테르 폴리올 10 내지 40 중량%로 이루어진 폴리올 혼합물, 아민계 촉매제 및 정포제에 발포제로서 물을 혼합한 레진 프리믹스에 MDI계 이소시아네이트와 반응시키는 것을 특징으로 한다. The present invention provides a method for producing an ultra low density foamed polyurethane foam. The method comprises (a) 10 to 40% by weight of sucrose-based polyether polyols having an average hydroxyl group of 2 to 6, an average hydroxyl group of 300 to 600 mgKOH / g, and (b) a glycol ether polymer having an average molecular weight of 200 to 800. 5 to 30% by weight (c) 5 to 30% by weight of polyether polyol having an average number of functional groups of 2 to 5 and an average hydroxyl group of 50 to 200 mgKOH / g, and (d) adding ethylene oxide and propylene oxide to phthalic anhydride It is characterized in that it is reacted with MDI isocyanate in a resin premix in which water is mixed as a blowing agent to a polyol mixture, an amine catalyst and a foam stabilizer made of 10 to 40% by weight of polyester polyol.
본 발명의 하나의 구체예에서는 상기 폴리올 혼합물과 이소시아네이트는 NCO/OH비율이 1.0 내지 1.4가 되도록 반응시키는 것을 특징으로 한다.In one embodiment of the present invention, the polyol mixture and the isocyanate are reacted such that the NCO / OH ratio is 1.0 to 1.4.
이하 본 발명의 구체적인 내용을 하기에 상세히 설명한다.Hereinafter, specific contents of the present invention will be described in detail below.
발명의 구체예에 대한 상세한 설명Detailed Description of the Invention
본 발명의 초저밀도 수발포 폴리우레탄 조성물은 (A)폴리올 혼합물 80 내지 90 중량부, (B) 물로 이루어진 발포제 3 내지 15 중량부, (C) 아민계 촉매제 0.0001 내지 10 중량부, 및 (D) 정포제 0.0001 내지 5 중량부로 이루어진 레진 프리믹스에 반응제로 MDI계 이소시아네이트를 NCO/OH비율이 1.0 내지 1.4로 혼합시킨 것이다. The ultra low density water-foaming polyurethane composition of the present invention comprises (A) 80 to 90 parts by weight of a polyol mixture, (B) 3 to 15 parts by weight of a blowing agent consisting of water, (C) 0.0001 to 10 parts by weight of an amine catalyst, and (D) MDI isocyanate is mixed at a NCO / OH ratio of 1.0 to 1.4 as a reactant in a resin premix consisting of 0.0001 to 5 parts by weight of a foam stabilizer.
상기 폴리올 혼합물은 (a)평균 관능기가 2∼6이며, 300∼600 mgKOH/g의 평균 수산기를 가진 수크로스계 폴리에테르 폴리올 10 내지 40 중량%, (b) 평균 분자량이 200~800인 글리콜에테르 중합체 5~30 중량% (c) 평균 관능기 수가 2∼5이며, 평균 수산기가 50∼200 mgKOH/g인 폴리에테르 폴리올 5 내지 30 중량%, 및 (d) 무수 프탈산에 에틸렌 산화물과 프로필렌 산화물을 첨가중합하여 제조된 폴리에스테르 폴리올 10 내지 40 중량%로 이루어진다. The polyol mixture has (a) 10 to 40% by weight sucrose-based polyether polyol having an average functional group of 2 to 6, an average hydroxyl group of 300 to 600 mgKOH / g, and (b) a glycol ether having an average molecular weight of 200 to 800. 5-30% by weight of polymer (c) 5-30% by weight of polyether polyol having an average number of functional groups of 2-5, an average hydroxyl group of 50-200 mgKOH / g, and (d) ethylene oxide and propylene oxide added to phthalic anhydride It consists of 10 to 40% by weight of polyester polyol prepared by polymerization.
상기 수크로스계 폴리에테르 폴리올(a)은 평균 관능기가 2∼6이며, 300∼600 mgKOH/g의 평균 수산기를 가진 것을 사용한다. 만일 평균수산기가 300 이하일 경우 제품의 저온 치수안정성이 급격히 저하되고 기계적 강도가 저하되며 600 이상일 경우 강도가 딱딱해져 깨어지는 현상이 일어나고 열전도도가 증가하여 단열재로써 단열성능이 떨어진다. The said sucrose type polyether polyol (a) has an average functional group of 2-6, and the thing which has an average hydroxyl group of 300-600 mgKOH / g is used. If the average hydroxyl value is less than 300, the low-temperature dimensional stability of the product is sharply lowered, the mechanical strength is lowered. If the average hydroxyl value is 600 or more, the strength is hardened and cracking occurs, the thermal conductivity increases, the heat insulating performance is lowered as a heat insulating material.
본 발명에서 상기 수크로스계 폴리에테르 폴리올(a)은 전체 폴리올 혼합물중 10 내지 40 중량% 사용한다. In the present invention, the sucrose-based polyether polyol (a) is used in an amount of 10 to 40% by weight in the total polyol mixture.
상기 폴리에테르 폴리올(b)은 평균 분자량이 200~800인 글리콜에테르 중합체 5~30 중량 %로 사용한다. 만일 5 중량% 미만으로 사용할 경우, 5 중량 % 미만으로 사용할 경우 Polyol 자체 반응성이 저하되며 기계적 물성이 저하되고, 30 중량 %를 초과하여 사용할 경우 열전도율이 높아져 단열성능이 떨어진다. The polyether polyol (b) is used in 5 to 30% by weight of a glycol ether polymer having an average molecular weight of 200 to 800. If less than 5% by weight, less than 5% by weight of the polyol self reactivity is lowered, mechanical properties are lowered, when used in excess of 30% by weight is higher thermal conductivity is lowered thermal insulation performance.
상기 평균 관능기 수가 2∼5이며, 평균 수산기가 50∼200 mgKOH/g인 폴리에테르 폴리올(c)을 5 중량% 미만으로 사용할 경우, 강도가 증가하여 폼이 부스러지거나 깨어질 가능성이 높다. 30 중량 %를 초과할 경우 강도가 약해져 생산성 저하를 일으킨다. When the polyether polyol (c) having an average number of functional groups of 2 to 5 and an average hydroxyl group of 50 to 200 mgKOH / g is used at less than 5% by weight, the strength is likely to increase and the foam may be broken or broken. If it exceeds 30% by weight, the strength is weakened, resulting in a decrease in productivity.
상기 폴리에스테르 폴리올(d)을 10 중량% 미만으로 사용할 경우, 10 중량% 미만으로 사용할 경우, 강도가 약해져 생산성 저하를 일으키고, 40 중량% 초과하여 사용하면, 강도는 높지만 지나친 가교 등으로 너무 강직해서 깨어지거나 부서질 염 려가 있다. When the polyester polyol (d) is used in less than 10% by weight, when used in less than 10% by weight, the strength is weakened, causing a decrease in productivity, when used in excess of 40% by weight, the strength is high, but too rigid due to excessive crosslinking, etc. There is a risk of breaking or breaking.
본 발명에서 상기 폴리올 혼합물(A)은 80 내지 90 중량부 사용한다. 사용되는 폴리올들은 각각의 OH- value 과 Functionality, 중합시에 개시제와 점도 등에 따라 고유의 특성을 가지고 있는데, OH- value 와 Functionality가 큰 폴리올들을 사용하면 가교도가 높아져 강도가 우수한 제품을 얻을 수 있지만, 밀도가 높아져 수율이 나빠지고 너무 강직해서 깨어지거나 부스러지기 쉬운 성질이 있고, OH- value 와 Functionality가 낮은 폴리올들을 사용하면 연성이 뛰어나 깨어지거나 부서지는 성질은 없지만 강도가 너무 낮게나와 건축자재로써 부적합한 경향이 있다. 따라서 건축자재로써 우수한 단열성능과 적당한 강도를 가지면서 연성과 탄성을 가지고 탁월한 수율을 낼 수 있으려면 위의 폴리올 들을 적절하게 혼합하여 사용하여야 한다. In the present invention, the polyol mixture (A) is used in an amount of 80 to 90 parts by weight. The polyols used have unique properties depending on the OH- value and functionality, and the initiator and viscosity during the polymerization. When the polyols having high OH-value and functionality are used, the crosslinking degree is increased, thereby obtaining a product having high strength. Higher density, poor yield, too stiff, brittle and brittle, and OH-value and low functional polyols are excellent in ductility, so they do not break or break, but their strength is too low, making them unsuitable for building materials. There is this. Therefore, the above polyols must be mixed and used properly to be able to produce excellent insulation with ductility and elasticity while having excellent insulation performance and moderate strength as a building material.
본 발명에서는 발포제로서 물을 단독 사용하며, 3 내지 15 중량부 사용한다. 만일 3 중량부 미만으로 사용할 경우, 발포가 안되어 밀도가 높아지며, 본 발명에서 목적으로 하는 초저밀도 폴리우레탄 폼을 제조할 수 없다. 또한 만일 15 중량부를 초과하여 사용할 경우, 이소시아네이트와의 반응열 때문에 제품에 스코칭(scorching)현상이 발생될 수 있다. 또한, 폼 내부에 과량의 CO2 가스가 남아 있어 열전도도를 상승시키는 요인이 된다.In the present invention, water is used alone as a blowing agent, and 3 to 15 parts by weight is used. If it is used less than 3 parts by weight, the foam is not foamed high density, it is impossible to produce the ultra-low density polyurethane foam of the present invention. In addition, if used in excess of 15 parts by weight, scorching may occur in the product due to the heat of reaction with isocyanate. In addition, excess CO 2 gas remains inside the foam, which is a factor of increasing the thermal conductivity.
본 발명에서는 촉매제로 아민계 촉매제를 사용한다. 상기 아민계 촉매제는 디메틸에탄올 아민(DMEA), 디메틸시클로헥실아민(DMCHA), 트리에틸렌디아민(TEDA), 펜타메틸디에틸렌트리아민(PMDETA), 트리에탄올아민(TEA), 트리스(3-디메틸아미노) 프로필헥사하이드로트리아민 테트라 메틸렌 헥실디아민(TMHDA), 트리프로필아민, 모노에탄올아민, 트리부틸아민. 트리옥틸아민, 헥사데실디메틸아민, N-메틸몰포린, N-에틸몰포린, N-옥타데실몰포린, 트리이소프로판올 아민, 비스디메틸아미노에틸에테르 및 이들의 혼합물로 선택된다. In the present invention, an amine catalyst is used as a catalyst. The amine catalyst is dimethylethanol amine (DMEA), dimethylcyclohexylamine (DMCHA), triethylenediamine (TEDA), pentamethyldiethylenetriamine (PMDETA), triethanolamine (TEA), tris (3-dimethylamino) Propylhexahydrotriamine tetra methylene hexyldiamine (TMHDA), tripropylamine, monoethanolamine, tributylamine. Trioctylamine, hexadecyldimethylamine, N-methylmorpholine, N-ethylmorpholine, N-octadecylmorpholine, triisopropanol amine, bisdimethylaminoethylether and mixtures thereof.
본 발명에서는 정포제로서 폴리실록산 에테르를 사용하는 것이 바람직하며, 0.0001 내지 5 중량부, 바람직하게는 0.0001 내지 3 중량부로 사용한다. 일반적으로 폴리우레탄 폼 발포에 이용되는 실리콘 정포제는 사용이 가능하며, 단독 또는 2가지 이상 혼합하여 사용한다. In the present invention, it is preferable to use polysiloxane ether as the foam stabilizer, and it is used in 0.0001 to 5 parts by weight, preferably 0.0001 to 3 parts by weight. In general, the silicone foam stabilizer used for polyurethane foam foaming may be used, and may be used alone or in combination of two or more thereof.
본 발명에서 물은 화학적 발포제로 사용하여 이소시아네이트와 물의 반응에서 생성되는 CO2 가스로 부풀어 오를때 생성되는 무수한 Cell 들은 표면장력 및 Cell내부의 압력에 의해서 서로 합쳐져서 보다 큰 Cell 을 형성하려는 경향을 보인다. 그러나 저밀도 폼의 물성을 우수하게 하기위해서는 균일하고 작은 셀이 형성되는 것이 가장 바람직하며, 이를 위해서 정포제로서 실리콘계 계면활성제를 이용한다. 실리콘계 계면활성제는 셀의 표면에 전하를 공급하여, 셀 사이에 정전기적 반발력를 일으켜 작고 균일한 셀이 크게 뭉쳐지는 것을 방지함으로써, 우수한 물성을 가진 저밀도 폼을 얻을 수 있게 하는 것이다. 상기 정포제를 0.0001 중량부 미만으로 사용할 경우 셀의 표면이 뭉쳐져 크고 불균일한 셀이 형성되므로, 저밀도 폼의 물성이 나빠지고, 5중량부 이상으로 사용하면, 저밀도 폼의 기계적강도가 저하된다. In the present invention, when water is used as a chemical blowing agent, the innumerable cells generated when inflated with the CO 2 gas generated in the reaction of isocyanate and water show a tendency to combine with each other by the surface tension and the pressure inside the cell to form a larger cell. However, in order to improve the properties of the low density foam, it is most preferable to form a uniform and small cell, and for this purpose, a silicon-based surfactant is used as the foam stabilizer. Silicon-based surfactants supply electric charges to the surface of the cell, thereby causing an electrostatic repulsion force between the cells to prevent large agglomeration of small and uniform cells, thereby obtaining a low density foam having excellent physical properties. When the foam stabilizer is used at less than 0.0001 parts by weight, the surface of the cells are agglomerated to form a large and uneven cell. Therefore, the properties of the low density foam deteriorate, and when used at 5 parts by weight or more, the mechanical strength of the low density foam is lowered.
상기 폴리올 혼합물 80 내지 90 중량부, 발포제 3 내지 15 중량부, 아민계 촉매제 0.0001 내지 10 중량부, 및 정포제 0.0001 내지 5 중량부로 이루어진 레진 프리믹스에 반응제로 MDI계 이소시아네이트를 사용한다. MDI isocyanate is used as a reactant in a resin premix consisting of 80 to 90 parts by weight of the polyol mixture, 3 to 15 parts by weight of blowing agent, 0.0001 to 10 parts by weight of amine catalyst, and 0.0001 to 5 parts by weight of foam stabilizer.
상기 MDI계 이소시아네이트는 NCO/OH비율이 1.0 내지 1.4로 혼합된다. 1.0 이하로 되면 폴리우레탄 반응형성이 어려워 폼 생성이 저하되고, 1.4 이상이면 저온에서의 치수안정성이 저하되고, 폼의 부스러짐 현상이 증가된다. The MDI isocyanate is mixed with an NCO / OH ratio of 1.0 to 1.4. When it becomes 1.0 or less, polyurethane reaction formation is difficult and foam formation falls, When it is 1.4 or more, the dimensional stability at low temperature falls and the crumb of a foam increases.
상기 MDI계 이소시아네이트는 평균 작용기 2.5 이상이며, 고분자형인 4,4'-디페닐메탄 디이소시아네이트인 것이 바람직하다. The said MDI type isocyanate is 2.5 or more of average functional groups, and it is preferable that it is polymeric 4,4'- diphenylmethane diisocyanate.
본 발명에서는 난연성을 부여하기 위해 필요에 따라 난연제를 3 내지 30 중량부 더 포함할 수 있다. 상기 난연제는 트리스(2-클로로프로필)포스페이트(TCPP), 트리스(2-클로로에틸)포스페이트(TCEP), 트리크레실 포스페이트 및 이들의 혼합물 등이 사용될 수 있으며, 반드시 이에 제한되는 것은 아니다. 만일 난연제를 3 중량부미만 사용시 기본적인 난연성인 화기를 제거 하였을 때, 스스로 꺼지는 성질인 자소성이 확보되지 않고, 30 중량부를 초과하여 사용시, 더 이상 난연제를 투입하여도 난연성의 향상은 거의 없으면서 밀도가 증가하여 저밀도 폼의 수율을 떨어뜨려 생산 효율을 감소시킨다. In the present invention, in order to impart flame retardancy, it may further comprise 3 to 30 parts by weight of a flame retardant as necessary. The flame retardant may include tris (2-chloropropyl) phosphate (TCPP), tris (2-chloroethyl) phosphate (TCEP), tricresyl phosphate and mixtures thereof, and the like, but is not limited thereto. If the flame retardant is less than 3 parts by weight, the basic flame retardant fire is removed, and the self-extinguishing property is not secured. If the flame retardant is used in excess of 30 parts by weight, the flame retardant is no longer improved. This increases the yield of low density foams, reducing the production efficiency.
본 발명의 초저밀도 수발포 폴리우레탄 폼의 제조방법은 (a)평균 관능기가 2∼6이며, 300∼600 mgKOH/g의 평균 수산기를 가진 수크로스계 폴리에테르 폴리올 10 내지 40 중량%, (b) 평균 분자량이 200~800인 글리콜에테르 중합체 5~30중량 % (c) 평균 관능기 수가 2∼5이며, 평균 수산기가 50∼200 mgKOH/g인 폴리에테르 폴 리올 5 내지 30 중량%, 및 (d) 무수프탈산에 에틸렌 산화물과 프로필렌 산화물을 첨가중합하여 제조된 폴리에스테르 폴리올 10 내지 40 중량%로 이루어진 폴리올 혼합물, 아민계 촉매제 및 정포제에 발포제로서 물을 혼합한 레진 프리믹스에 MDI계 이소시아네이트와 반응시키는 것을 특징으로 한다. 상기 폴리올 혼합물과 이소시아네이트는 NCO/OH비율이 1.0 내지 1.4가 되도록 반응시킨다. The method for producing an ultra low density water-foaming polyurethane foam of the present invention comprises (a) 10 to 40% by weight of sucrose-based polyether polyol having an average functional group of 2 to 6 and an average hydroxyl group of 300 to 600 mgKOH / g, (b 5 to 30% by weight glycol ether polymer having an average molecular weight of 200 to 800 (c) 5 to 30% by weight of polyether polyol having an average number of functional groups of 2 to 5 and an average hydroxyl group of 50 to 200 mgKOH / g, and (d Reaction with MDI isocyanate in a resin premix of a polyol mixture consisting of 10 to 40% by weight of a polyester polyol prepared by addition polymerization of ethylene oxide and propylene oxide to phthalic anhydride, an amine catalyst and a foam stabilizer mixed with water as a blowing agent It is characterized by. The polyol mixture and isocyanate are reacted such that the NCO / OH ratio is 1.0 to 1.4.
그 외에 폴리우레탄 폼에 일반적으로 사용되는 충전제 및 산화방지제, 자외선 흡수제, 안정제, 냄세제거제, 점도 저하제, 착색제 등은 필요에 따라 사용가능하다. In addition, fillers and antioxidants commonly used in polyurethane foams, ultraviolet absorbers, stabilizers, deodorants, viscosity reducing agents, colorants and the like can be used as necessary.
본 발명은 하기의 실시예에 의하여 보다 더 잘 이해될 수 있으며, 하기의 실시예는 본 발명의 예시 목적을 위한 것이며 첨부된 특허 청구 범위에 의하여 한정되는 보호범위를 제한하고자 하는 것은 아니다.The invention can be better understood by the following examples, which are intended for the purpose of illustration of the invention and are not intended to limit the scope of protection defined by the appended claims.
실시예 1Example 1
혼합폴리올에 촉매, 난연제, 계면활성제, 물을 하기 표 1에 기재된 함량으로 혼합한 다음, 반응제와의 인덱스 1.1로 조절하여 원액온도 13℃로 각각 맞춰서 3초간 격렬히 교반시킨 다음, 반응이 진행되는 정도에 따른 시간을 측정하면서 자유발포하였다. 제조된 우레탄 폼 시편에 대한 전자현미경 사진은 도 1에 나타내었으며, 물성 평가는 한국표준인증원의 KS M 3809의 규정에 따라 한국화학시험연구원에 의뢰하여 측정하고, 그 결과를 표 1에 나타내었다.The catalyst, flame retardant, surfactant, and water were mixed in the mixed polyol in the amounts shown in Table 1 below, and then adjusted to the index 1.1 with the reactants, vigorously stirred for 3 seconds at a stock solution temperature of 13 ° C., and then the reaction proceeded. Free foaming was performed by measuring the time according to the degree. The electron micrographs of the prepared urethane foam specimens are shown in FIG. 1, and the physical properties were evaluated by the Korea Testing Institute according to the provisions of KS M 3809 of the Korea Institute of Standards and Certification, and the results are shown in Table 1.
물성 평가 방법Property evaluation method
KS M 3809 : 2006 의 시험방법에 의해 물성을 측정하였다.Physical properties were measured by the test method of KS M 3809: 2006.
폴리올 a : 평균 관능기가 2∼6이며, 300∼600 mgKOH/g의 평균 수산기를 가진 수크로스계 폴리에테르 폴리올을 사용하였다.Polyol a: The sucrose type polyether polyol which has an average functional group of 2-6, and has an average hydroxyl group of 300-600 mgKOH / g was used.
폴리올 b : 평균 분자량이 200~ 800인 글리콜에테르 중합체를 사용하였다.Polyol b: glycol ether polymer having an average molecular weight of 200 to 800 was used.
폴리올 c : 평균 관능기 수가 2∼5이며, 평균 수산기가 50∼200 mgKOH/g인 폴리에테르 폴리올을 사용하였다.Polyol c: The polyether polyol whose average number of functional groups is 2-5, and whose average hydroxyl group is 50-200 mgKOH / g was used.
폴리올 d : 무수프탈산에 에틸렌 산화물과 프로필렌 산화물을 첨가 중합하여 제조된 폴리에스테르 폴리올을 사용하였다.Polyol d: Polyester polyol prepared by addition polymerization of ethylene oxide and propylene oxide to phthalic anhydride was used.
촉매 A : 디메틸시클로헥실아민(DMCHA)을 사용하였다.Catalyst A: Dimethylcyclohexylamine (DMCHA) was used.
촉매 B : 비스디메틸아미노에틸에테르를 사용하였다.Catalyst B: Bisdimethylaminoethyl ether was used.
촉매 C : 테트라 메틸렌 헥실디아민 (TMHDA)을 사용하였다. Catalyst C: Tetramethylene hexyldiamine (TMHDA) was used.
난연제 : 트리스클로로이소프로필포스페이트를 사용하였다.Flame retardant: Trischloroisopropyl phosphate was used.
반응제 : 폴리메틸렌디페닐이소시아네이트 점도 187cps/25℃이고 NCO 31.2 증량 % 함유한 것을 사용하였다. Reagent: A polymethylenediphenyl isocyanate having a viscosity of 187 cps / 25 DEG C and containing 31.2% by weight of NCO was used.
cream time : 원액이 섞이고 반응이 시작되어 색깔이 뿌옇게 변하면서 부풀어 오르기 시작하는 시점을 의미한다.cream time: The time when the stock solution starts to mix and the color starts to swell as the color starts to swell.
gel time : 고분자가 형성되기 시작하여 스트로우로 찍었을 때 스트로우에 폴리우레탄 폼이 실처럼 딸려 올라오는 시점을 의미한다.gel time: It means the time when the polymer starts to form and the polyurethane foam comes to the straw when taken with a straw.
Rise time : 폴리우레탄 폼 반응이 끝나 더 이상 높이 올라오지 않는 시점을 의미한다.Rise time: It means the time when the polyurethane foam reaction is over and no longer rises.
표 1에 나타난 바와 같이, 평균 분자량이 200∼800인 글리콜에테르 중합체의 사용량이 증가하면 혼합폴리올의 자제 반응성이 개선되고 기계적 물성도 좋아졌으나, 너무 많이 투입하면 열전도율이 급격히 높아져 단열성능이 떨어졌다. 또한 평균 분자량이 200∼800인 글리콜에테르 중합체(b)의 첨가량을 변화하면서 저밀도 폼의 반응성을 측정한 결과, 첨가량이 너무 적으면 혼합 폴리올 자제 반응이 느려 스프레이 작업에 적합하지 않고, 과다하게 첨가할 경우, 혼합 폴리올의 자체 반응이 너무 빨라져서 스프레이 작업이 적당하지 않음을 확인할 수 있었다. As shown in Table 1, when the amount of the glycol ether polymer having an average molecular weight of 200 to 800 was increased, the self-responsiveness of the mixed polyol was improved and the mechanical properties were also improved. However, when too much was added, the thermal conductivity rapidly increased, resulting in poor thermal insulation performance. In addition, the reactivity of the low-density foam was measured while varying the addition amount of the glycol ether polymer (b) having an average molecular weight of 200 to 800. If the addition amount is too small, the mixed polyol self-reaction is slow, which is not suitable for spraying, and it is excessively added. In this case, it was found that the self-reaction of the mixed polyol was so fast that spraying was not suitable.
본 발명은 화학 발포제가 아닌 물로 발포시킴으로써, 냄새가 거의 없고 화재발생시 유독가스를 방출하지 않는 환경친화적이고, 원재료의 단가도 낮출 수 있고, 독특한 셀 구조를 가짐으로써, 우수한 단열성능과 접착성이 뛰어나고, 발포력이 대폭 향상되며, 우수한 단열 및 결로방지 효과로 인해 에너지 절감 효과를 얻을 수 있어 경제성이 우수하고, 시공성이 뛰어나며, 차음흡음성이 우수한 초저밀도 수발포 폴리우레탄 조성물 및 그 제조방법을 제공하는 발명의 효과를 가진다. The present invention is environmentally friendly by foaming with water, not a chemical blowing agent, odorless and does not emit toxic gases in the event of a fire, lowers the cost of raw materials, and has a unique cell structure, excellent heat insulating performance and adhesion The foaming ability is greatly improved, and the energy saving effect can be obtained due to the excellent heat insulation and condensation prevention effect, thereby providing an excellent economic efficiency, excellent workability, and excellent sound absorption and sound absorption, and providing a super low density foamable polyurethane composition and a method of manufacturing the same. Has the effect of the invention.
본 발명의 단순한 변형 내지 변경은 이 분야의 통상의 지식을 가진 자에 의하여 용이하게 실시될 수 있으며, 이러한 변형이나 변경은 모두 본 발명의 영역에 포함되는 것으로 볼 수 있다.Simple modifications or changes of the present invention can be easily carried out by those skilled in the art, and all such modifications or changes can be seen to be included in the scope of the present invention.
Claims (7)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020060101291A KR100809667B1 (en) | 2006-10-18 | 2006-10-18 | Water blowned polyurethane composition having very low density and method for preparing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020060101291A KR100809667B1 (en) | 2006-10-18 | 2006-10-18 | Water blowned polyurethane composition having very low density and method for preparing the same |
Publications (1)
Publication Number | Publication Date |
---|---|
KR100809667B1 true KR100809667B1 (en) | 2008-03-05 |
Family
ID=39397532
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020060101291A KR100809667B1 (en) | 2006-10-18 | 2006-10-18 | Water blowned polyurethane composition having very low density and method for preparing the same |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR100809667B1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100978577B1 (en) | 2009-11-28 | 2010-08-27 | 주식회사 대양 | Water based non freon poly urethane foam |
WO2011118872A1 (en) * | 2010-03-26 | 2011-09-29 | 주식회사 대양 | Production method for water-soluble foamed expanded rigid polyurethane |
CN106397710A (en) * | 2016-09-30 | 2017-02-15 | 上海东大聚氨酯有限公司 | Combined polyether, polyurethane raw material composition, foam and preparation method |
US20180086873A1 (en) * | 2015-05-15 | 2018-03-29 | Stepan Company | Ethoxylated Vegetable Oils in Low Density Spray Foam Formulations |
CN112752780A (en) * | 2018-10-08 | 2021-05-04 | 陶氏环球技术有限责任公司 | Formulated polyol compositions |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001316443A (en) | 2000-05-10 | 2001-11-13 | Nippon Polyurethane Ind Co Ltd | Method for manufacturing hard polyurethane foam |
-
2006
- 2006-10-18 KR KR1020060101291A patent/KR100809667B1/en not_active IP Right Cessation
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001316443A (en) | 2000-05-10 | 2001-11-13 | Nippon Polyurethane Ind Co Ltd | Method for manufacturing hard polyurethane foam |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100978577B1 (en) | 2009-11-28 | 2010-08-27 | 주식회사 대양 | Water based non freon poly urethane foam |
WO2011118872A1 (en) * | 2010-03-26 | 2011-09-29 | 주식회사 대양 | Production method for water-soluble foamed expanded rigid polyurethane |
US20180086873A1 (en) * | 2015-05-15 | 2018-03-29 | Stepan Company | Ethoxylated Vegetable Oils in Low Density Spray Foam Formulations |
CN106397710A (en) * | 2016-09-30 | 2017-02-15 | 上海东大聚氨酯有限公司 | Combined polyether, polyurethane raw material composition, foam and preparation method |
CN106397710B (en) * | 2016-09-30 | 2019-01-01 | 上海东大聚氨酯有限公司 | Combined polyether, polyurethane raw material composition, foam and preparation method |
CN112752780A (en) * | 2018-10-08 | 2021-05-04 | 陶氏环球技术有限责任公司 | Formulated polyol compositions |
CN112752780B (en) * | 2018-10-08 | 2023-03-31 | 陶氏环球技术有限责任公司 | Formulated polyol compositions |
US11932722B2 (en) | 2018-10-08 | 2024-03-19 | Dow Global Technologies Llc | Formulated polyol compositions |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2599090C (en) | Rigid polyurethane foams with low thermal conductivity and a process for their production | |
US20150144829A1 (en) | Composition in the form of a dispersion comprising a lignin, a method for the manufacturing thereof and use thereof | |
BRPI0620510A2 (en) | rigidly molded polyurethane foam | |
JP2016531196A (en) | Vacuum assisted method for making closed cell rigid polyurethane foam using mixed foaming agents | |
JP2016532726A (en) | Flexible polyurethane foam and related methods and articles | |
ES2793850T3 (en) | Production of polyurethane foam | |
CN103619954B (en) | There is the isocyanate-based polymer foam of the thermal insulating properties of improvement | |
JP2008179831A (en) | Isocyanate composition and its use in manufacturing expanded polyurethane with improved physico-mechanical characteristics | |
KR20160060107A (en) | Polyurethane foam and associated method and article | |
KR100809667B1 (en) | Water blowned polyurethane composition having very low density and method for preparing the same | |
Efstathiou | Synthesis and characterization of a Polyurethane Prepolymer for the development of a novel Acrylate-based polymer foam | |
JP2004285319A (en) | Rigid polyurethane foam composition and low-temperature insulator using the same | |
US20040092616A1 (en) | Process for producing rigid polyurethane foams and finished articles obtained therefrom | |
CN109535688A (en) | A kind of polyurethane foam heat insulation material and preparation method thereof | |
CA2429868A1 (en) | Process for making polyurethane integral skin foams | |
KR101634309B1 (en) | Rigid polyurethane spray foam composition of low density | |
CN111518251A (en) | Polyurethane rigid foam and preparation method thereof | |
KR100753252B1 (en) | Flame retardant polyurethane foam for ultra-low-temperature and manufacturing method thereof | |
RU2765788C2 (en) | Polyol compositions | |
US20240279379A1 (en) | Open cell flexible isocyanate-based foams having a low exotherm during foaming | |
JPH04239516A (en) | Production of rigid polyurethane foam | |
KR100561806B1 (en) | Low density polyurethane foam compositions for spray | |
KR101446339B1 (en) | Rigid polyurethane foams for spray | |
JP2000290343A (en) | Stock solution for hard polyurethane foam and rigid polyurethane foam | |
JP2005330392A (en) | Method for producing polyamic acid foam |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
E902 | Notification of reason for refusal | ||
E701 | Decision to grant or registration of patent right | ||
GRNT | Written decision to grant | ||
FPAY | Annual fee payment |
Payment date: 20130227 Year of fee payment: 6 |
|
FPAY | Annual fee payment |
Payment date: 20140226 Year of fee payment: 7 |
|
FPAY | Annual fee payment |
Payment date: 20150216 Year of fee payment: 8 |
|
FPAY | Annual fee payment |
Payment date: 20160115 Year of fee payment: 9 |
|
LAPS | Lapse due to unpaid annual fee |