KR20220132828A - Manufacturing method of anionic water-dispersible polyurethane dispersion and biodegradable polyurethane film prepared therefrom - Google Patents
Manufacturing method of anionic water-dispersible polyurethane dispersion and biodegradable polyurethane film prepared therefrom Download PDFInfo
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- 229920006264 polyurethane film Polymers 0.000 title claims abstract description 51
- 229920003009 polyurethane dispersion Polymers 0.000 title claims abstract description 41
- 125000000129 anionic group Chemical group 0.000 title claims abstract description 38
- 238000004519 manufacturing process Methods 0.000 title claims description 14
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims abstract description 76
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 238000003756 stirring Methods 0.000 claims abstract description 53
- 238000000034 method Methods 0.000 claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000012153 distilled water Substances 0.000 claims abstract description 36
- 238000002156 mixing Methods 0.000 claims abstract description 32
- 239000006185 dispersion Substances 0.000 claims abstract description 28
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 19
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 19
- 239000004359 castor oil Substances 0.000 claims abstract description 18
- 235000019438 castor oil Nutrition 0.000 claims abstract description 18
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 claims abstract description 18
- JVYDLYGCSIHCMR-UHFFFAOYSA-N 2,2-bis(hydroxymethyl)butanoic acid Chemical compound CCC(CO)(CO)C(O)=O JVYDLYGCSIHCMR-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000002994 raw material Substances 0.000 claims abstract description 17
- 238000006386 neutralization reaction Methods 0.000 claims abstract description 16
- 239000004970 Chain extender Substances 0.000 claims abstract description 15
- NIMLQBUJDJZYEJ-UHFFFAOYSA-N isophorone diisocyanate Chemical compound CC1(C)CC(N=C=O)CC(C)(CN=C=O)C1 NIMLQBUJDJZYEJ-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000005058 Isophorone diisocyanate Substances 0.000 claims abstract description 14
- 238000001816 cooling Methods 0.000 claims abstract description 9
- 239000000203 mixture Substances 0.000 claims abstract description 9
- 230000002194 synthesizing effect Effects 0.000 claims abstract description 4
- 229920001046 Nanocellulose Polymers 0.000 claims description 13
- 229920002101 Chitin Polymers 0.000 claims description 12
- 239000002121 nanofiber Substances 0.000 claims description 12
- 229920001661 Chitosan Polymers 0.000 claims description 9
- 125000002057 carboxymethyl group Chemical group [H]OC(=O)C([H])([H])[*] 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 8
- 239000011521 glass Substances 0.000 claims description 7
- 230000003472 neutralizing effect Effects 0.000 claims description 4
- 238000005266 casting Methods 0.000 claims description 3
- 150000001450 anions Chemical class 0.000 claims 1
- 230000001747 exhibiting effect Effects 0.000 abstract description 4
- 239000004615 ingredient Substances 0.000 abstract description 3
- 239000003795 chemical substances by application Substances 0.000 abstract 2
- 230000003197 catalytic effect Effects 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 229920003023 plastic Polymers 0.000 description 9
- 239000004033 plastic Substances 0.000 description 9
- 238000002360 preparation method Methods 0.000 description 7
- 230000000704 physical effect Effects 0.000 description 6
- 239000003054 catalyst Substances 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 229920002635 polyurethane Polymers 0.000 description 5
- 239000004814 polyurethane Substances 0.000 description 5
- 229920000704 biodegradable plastic Polymers 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 238000002834 transmittance Methods 0.000 description 4
- 239000004034 viscosity adjusting agent Substances 0.000 description 4
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 108010059892 Cellulase Proteins 0.000 description 2
- 238000006065 biodegradation reaction Methods 0.000 description 2
- 229940106157 cellulase Drugs 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 239000007979 citrate buffer Substances 0.000 description 2
- 229920006238 degradable plastic Polymers 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 229920000426 Microplastic Polymers 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000000872 buffer Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000002041 carbon nanotube Substances 0.000 description 1
- 229910021393 carbon nanotube Inorganic materials 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 125000005442 diisocyanate group Chemical group 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920003225 polyurethane elastomer Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000001509 sodium citrate Substances 0.000 description 1
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
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- 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
- C08G18/82—Post-polymerisation treatment
-
- 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
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/75—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic
- C08G18/751—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring
- C08G18/752—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group
- C08G18/753—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group containing one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group having a primary carbon atom next to the isocyanate or isothiocyanate group
- C08G18/755—Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic containing only one cycloaliphatic ring containing at least one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group containing one isocyanate or isothiocyanate group linked to the cycloaliphatic ring by means of an aliphatic group having a primary carbon atom next to the isocyanate or isothiocyanate group and at least one isocyanate or isothiocyanate group linked to a secondary carbon atom of the cycloaliphatic ring, e.g. isophorone diisocyanate
-
- 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
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- 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
- C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
- C08J2375/04—Polyurethanes
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- 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)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Biological Depolymerization Polymers (AREA)
- Polyurethanes Or Polyureas (AREA)
Abstract
Description
본 발명은 음이온성 수분산 폴리우레탄 분산액의 제조방법 및 그 분산액으로 제조된 생분해성 폴리우레탄 필름에 관한 것으로, 더욱 상세하게는 인체에 해로운 촉매제를 사용하지 않으면서도, 우수한 생분해성, 기계적 물성 및 투명도를 나타내는 폴리우레탄 필름을 제공하는 음이온성 수분산 폴리우레탄 분산액의 제조방법 및 그 분산액으로 제조된 생분해성 폴리우레탄 필름에 관한 것이다.The present invention relates to a method for preparing an anionic water-dispersed polyurethane dispersion and a biodegradable polyurethane film prepared from the dispersion, and more particularly, excellent biodegradability, mechanical properties and transparency without using a catalyst harmful to the human body. It relates to a method for preparing an anionic water-dispersed polyurethane dispersion providing a polyurethane film showing
플라스틱은 편의성 때문에 현대생활의 필수품으로 자리잡았으나, 일회용품으로 적용되는 경우가 빈번하여 다량의 생활쓰레기를 배출하기 때문에 심각한 사회적 문제로 대두되고 있다.Plastic has become a necessity of modern life because of its convenience, but it is frequently applied as a disposable product and is emerging as a serious social problem because it produces a large amount of household waste.
플라스틱은 자연 상태에서는 매우 느리게 분해되는데, 플라스틱의 분해속도는 종류에 따라 수십 년에서 수백 년이 소요되는 것으로 알려져 있다. 또한, 최근에는 강이나 바다로 유출되는 플라스틱에 의해 해양이 미세플라스틱으로 오염되고 있다.Plastics decompose very slowly in their natural state, and it is known that the rate of decomposition of plastics takes several tens to hundreds of years depending on the type. In addition, recently, the ocean is polluted with microplastics by plastics flowing into rivers or seas.
상기의 문제점을 해소하기 위해 다양한 종류의 분해성 플라스틱이 개발되고 있는데, 현재 개발되고 있는 분해성 플라스틱은 빛(주로 자외선)에 의해 분해되는 광분해성 플라스틱과 미생물에 의해서 분해되는 생분해성 플라스틱이 주류를 이루고 있다.In order to solve the above problems, various types of degradable plastics are being developed. Currently, degradable plastics being developed are mainly photodegradable plastics that are decomposed by light (mainly ultraviolet) and biodegradable plastics that are decomposed by microorganisms. .
생분해성 플라스틱은 미생물이 생산하는 플라스틱(바이오 플라스틱), 전분이나 셀룰로오스 등의 천연 소재를 주성분으로 하여 제조하는 플라스틱과 분해성을 부여한 화학 합성 플라스틱으로 분류할 수 있다. 이들은 모두 땅속에 묻거나 바다 속에 버려두면 세균이나 조류, 곰팡이와 같은 자연에 존재하는 미생물에 의해 분해되어 저분자 화합물이 되었다가 최종적으로 물과 이산화탄소 또는 물과 메탄가스로 변하게 된다.Biodegradable plastics can be classified into plastics (bioplastics) produced by microorganisms, plastics manufactured with natural materials such as starch or cellulose as main components, and chemically synthesized plastics with degradability. If all these are buried in the ground or left in the sea, they are decomposed by microorganisms in nature, such as bacteria, algae, and mold, to form low molecular weight compounds, and finally turn into water and carbon dioxide or water and methane gas.
그러나, 기존의 생분해성 플라스틱은 성형이 어렵거나 성형에 의해 완성된 제품의 물성이 좋지않아 실용성이 떨어지는 한계가 있었다.However, conventional biodegradable plastics have limitations in that they are difficult to mold or have poor physical properties of products finished by molding, so that their practicality is poor.
한편, 일반적으로 폴리우레탄은 주 사슬의 반복 단위 속에 우레탄 결합(-NHCOO-)을 가지는 고분자 화합물의 총칭으로서, 내마모성, 내약품성, 내용제성이 좋을 뿐만 아니라 내노화성과 산소에 대한 안정성이 뛰어나 폴리우레탄 폼, 폴리우레탄 고무, 접착제, 합성섬유, 도료 등으로 많이 쓰이고, 플라스틱 제조 시에도 사용될 수 있다. 폴리우레탄은 일반적으로 자체적으로 가수분해성과 생분해성 등의 분해 특성을 가지고 있다. 그러나 그 분해특성이 매우 미약하여 폴리우레탄 제품을 사용한 후 폐기시 완전 분해되지 않고 부분 분해되어 반영구적으로 존재하거나 분해에 오랜 시간이 소요되어 환경오염의 원인이 된다는 문제점이 있었다.On the other hand, in general, polyurethane is a generic term for high molecular compounds having a urethane bond (-NHCOO-) in the repeating unit of the main chain. It is widely used in foam, polyurethane rubber, adhesives, synthetic fibers, paints, etc., and can also be used in the manufacture of plastics. Polyurethane generally has decomposition properties such as hydrolysis and biodegradability by itself. However, since the decomposition property is very weak, there was a problem that the polyurethane product is not completely decomposed when discarded after use, but is partially decomposed to exist semi-permanently, or it takes a long time to decompose, causing environmental pollution.
상기의 문제점을 해소하기 위해 수분산 폴리우레탄이 개발되고 있으나, 종래에 수분산 폴리우레탄의 경우 원료물질로 석유계의 디올, 디이소시아네이트 및 사슬확장제가 사용되어 친환경적이지 못하며, 합성과정에서 인체에 유해한 촉매제나 점도조절제가 사용되고, 물성이 좋지 않기 때문에 응용범위가 제한적이며, 물성보완을 위해 흑연이나 탄소나노튜브 등의 나노입자가 혼합되어 생분해성이 낮아지는 문제점이 있었다.Water-dispersed polyurethane is being developed to solve the above problems, but in the case of water-dispersed polyurethane, petroleum-based diol, diisocyanate and chain extender are used as raw materials, so it is not eco-friendly and harmful to the human body during the synthesis process. A catalyst or a viscosity modifier is used, and the application range is limited because the physical properties are not good, and there is a problem in that the biodegradability is lowered because nanoparticles such as graphite or carbon nanotubes are mixed to supplement the physical properties.
본 발명의 목적은 인체에 해로운 촉매제를 사용하지 않으면서도, 점도조절제로 아세톤을 사용하고 사슬확장제로 천연성분을 사용하여 우수한 생분해성, 기계적 물성 및 투명도를 나타내는 폴리우레탄 필름을 제공하는 음이온성 수분산 폴리우레탄 분산액의 제조방법 및 그 분산액으로 제조된 생분해성 폴리우레탄 필름을 제공하는 것이다.It is an object of the present invention to provide a polyurethane film exhibiting excellent biodegradability, mechanical properties and transparency by using acetone as a viscosity modifier and natural ingredients as a chain extender without using a catalyst harmful to the human body. To provide a method for preparing a polyurethane dispersion and a biodegradable polyurethane film prepared from the dispersion.
본 발명의 목적은 케스터오일과 디메틸올부탄산을 교반하면서 이소포론디이소시아네이트를 적하하여 교반하는 원료혼합단계, 상기 원료혼합단계를 통해 제조된 혼합물에 아세톤을 혼합하고 합성하는 우레탄합성단계, 상기 우레탄합성단계를 통해 합성된 우레탄을 냉각한 후에 트리에틸아민을 혼합하여 중화하는 중화단계, 상기 중화단계를 통해 중화된 우레탄에 증류수를 투입하고 교반하는 증류수교반단계 및 상기 증류수교반단계를 통해 증류수가 혼합된 우레탄에 함유된 아세톤을 제거하는 아세톤제거단계로 이루어지는 것을 특징으로 하는 음이온성 수분산 폴리우레탄 분산액의 제조방법을 제공함에 의해 달성된다.An object of the present invention is a raw material mixing step in which isophorone diisocyanate is added dropwise and stirred while stirring castor oil and dimethylol butanoic acid, acetone is mixed and synthesized in the mixture prepared through the raw material mixing step, a urethane synthesis step, the urethane synthesis After cooling the urethane synthesized through the step, a neutralization step of neutralizing by mixing triethylamine, a distilled water stirring step of adding distilled water to the urethane neutralized through the neutralization step and stirring, and distilled water mixed through the distilled water stirring step It is achieved by providing a method for preparing an anionic aqueous dispersion polyurethane dispersion, characterized in that it consists of an acetone removal step of removing the acetone contained in the urethane.
본 발명의 바람직한 특징에 따르면, 상기 원료혼합단계는 케스터오일 100 중량부에 디메틸올부탄산 10 내지 30 중량부를 75 내지 80℃의 온도와 200 내지 300rpm의 속도로 교반하면서 이소포론디이소시아네이트 50 내지 100 중량부를 적하하여 이루어지는 것으로 한다.According to a preferred feature of the present invention, the raw material mixing step is 50 to 100 parts by weight of isophorone diisocyanate while stirring 10 to 30 parts by weight of dimethylol butanoic acid to 100 parts by weight of castor oil at a temperature of 75 to 80° C. and a speed of 200 to 300 rpm. It is supposed to be done by dropping the wealth.
본 발명의 더 바람직한 특징에 따르면, 상기 우레탄합성단계는 상기 원료혼합단계를 통해 제조된 혼합물에 함유된 케스터오일 100 중량부 대비 아세톤 100 내지 500 중량부를 혼합하고 200 내지 300rpm의 속도로 60 내지 120분 동안 교반하여 이루어지는 것으로 한다.According to a more preferred feature of the present invention, in the urethane synthesis step, 100 to 500 parts by weight of acetone is mixed with 100 parts by weight of castor oil contained in the mixture prepared through the raw material mixing step, and 60 to 120 minutes at a speed of 200 to 300 rpm. It is supposed to be made while stirring.
본 발명의 더 바람직한 특징에 따르면, 상기 중화단계는 상기 우레탄합성단계를 통해 합성된 우레탄을 40 내지 50℃의 온도로 냉각한 후에 트리에틸아민을 혼합하고 300 내지 400rpm의 속도로 30 내지 60분 동안 교반하여 이루어지는 것으로 한다.According to a more preferred feature of the present invention, in the neutralization step, the urethane synthesized through the urethane synthesis step is cooled to a temperature of 40 to 50° C., and then triethylamine is mixed, and at a speed of 300 to 400 rpm for 30 to 60 minutes. It is supposed to be made by stirring.
본 발명의 더욱 바람직한 특징에 따르면, 상기 증류수교반단계에서는 상기 증류수 100 중량부에 사슬확장제 0.01 내지 5 중량부가 더 함유되며, 상기 사슬확장제는 나노셀룰로오스, 키틴나노섬유 및 카르복시메틸키토산으로 이루어진 그룹에서 선택된 하나 이상으로 이루어지는 것으로 한다.According to a more preferred feature of the present invention, in the distilled water stirring step, 0.01 to 5 parts by weight of a chain extender is further contained in 100 parts by weight of the distilled water, and the chain extender is selected from the group consisting of nanocellulose, chitin nanofiber, and carboxymethyl chitosan. It is supposed to consist of one or more.
또한, 본 발명의 목적은 상기의 제조방법으로 제조된 음이온성 수분산 폴리우레탄 분산액을 몰드가 설치된 유리판에 캐스팅한 후에 건조하여 제조되는 것을 특징으로 하는 생분해성 폴리우레탄 필름을 제공함에 의해서도 달성될 수 있다.In addition, the object of the present invention can be achieved by providing a biodegradable polyurethane film, characterized in that it is prepared by drying the anionic water-dispersed polyurethane dispersion prepared by the above manufacturing method after casting it on a glass plate on which a mold is installed. have.
본 발명의 바람직한 특징에 따르면, 상기 건조는 24 내지 26℃의 온도와 70 내지 80%의 상대습도를 나타내는 항온항습기에서 6 내지 8일동안 진행된 후에, 28 내지 32℃의 진공건조기에서 23 내지 25시간 동안 이루어지는 것으로 한다.According to a preferred feature of the present invention, the drying is carried out for 6 to 8 days in a thermo-hygrostat showing a temperature of 24 to 26 ° C and a relative humidity of 70 to 80%, and then 23 to 25 hours in a vacuum dryer at 28 to 32 ° C. to be done during
본 발명에 따른 수분산 폴리우레탄 분산액의 제조방법 및 그 분산액으로 제조된 생분해성 폴리우레탄 필름은 인체에 해로운 촉매제를 사용하지 않으면서도, 점도조절제로 아세톤을 사용하고 사슬확장제로 천연성분을 사용하여 우수한 생분해성, 기계적 물성 및 투명도를 나타내는 폴리우레탄 필름을 제공하는 탁월한 효과를 나타낸다.The method for producing a water-dispersed polyurethane dispersion according to the present invention and the biodegradable polyurethane film prepared from the dispersion are excellent by using acetone as a viscosity modifier and natural ingredients as a chain extender without using a catalyst harmful to the human body. It exhibits an excellent effect of providing a polyurethane film exhibiting biodegradability, mechanical properties and transparency.
도 1은 본 발명에 따른 수분산 폴리우레탄 분산액의 제조방법을 나타낸 순서도이다.
도 2는 본 발명에 따른 증류수를 혼합하여 음이온성 수분산 폴리우레탄 분산액을 제조하는 과정을 나타낸 반응식이다.
도 3은 본 발명에 따른 나노셀룰로오스를 혼합하여 음이온성 수분산 폴리우레탄 분산액을 제조하는 과정을 나타낸 반응식이다.
도 4는 본 발명에 따른 키틴나노섬유를 혼합하여 음이온성 수분산 폴리우레탄 분산액을 제조하는 과정을 나타낸 반응식이다.
도 5는 본 발명에 따른 카르복시메틸키토산을 사용하여 음이온성 수분산 폴리우레탄 분산액을 제조하는 과정을 나타낸 반응식이다.
도 6은 본 발명의 제조예 1 내지 3을 통해 제조된 음이온성 수분산 폴리우레탄 분산액의 점도변화(a)와 입자크기(b)를 측정하여 나타낸 그래프이다.
도 7 내지 8은 본 발명의 실시예 1 내지 14를 통해 제조된 생분해성 폴리우레탄 필름의 투명도를 측정하여 나타낸 사진이다.
도 9 내지 10은 본 발명의 실시예 1 내지 5 및 실시예 7 내지 10을 통해 제조된 생분해성 폴리우레탄 필름의 투과도를 측정하여 나타낸 그래프이다.
도 11 내지 13은 본 발명의 실시예 1 내지 14를 통해 제조된 생분해성 폴리우레탄 필름의 기계적 강도를 측정하여 나타낸 그래프이다.
도 14는 본 발명의 실시예 1 내지 5를 통해 제조된 생분해성 폴리우레탄 필름의 생분해도를 측정하여 나타낸 그래프이다.1 is a flowchart showing a method for preparing an aqueous dispersion polyurethane dispersion according to the present invention.
Figure 2 is a reaction scheme showing a process for preparing anionic aqueous dispersion polyurethane dispersion by mixing distilled water according to the present invention.
3 is a reaction scheme showing a process for preparing an anionic aqueous dispersion polyurethane dispersion by mixing nanocellulose according to the present invention.
Figure 4 is a reaction scheme showing the process of preparing anionic aqueous dispersion polyurethane dispersion by mixing chitin nanofibers according to the present invention.
5 is a reaction scheme showing a process for preparing an anionic aqueous dispersion polyurethane dispersion using carboxymethylchitosan according to the present invention.
6 is a graph showing the viscosity change (a) and particle size (b) of the anionic aqueous dispersion polyurethane dispersion prepared through Preparation Examples 1 to 3 of the present invention measured.
7 to 8 are photographs showing the measurement of the transparency of the biodegradable polyurethane film prepared through Examples 1 to 14 of the present invention.
9 to 10 are graphs showing the measurement of the transmittance of the biodegradable polyurethane film prepared through Examples 1 to 5 and Examples 7 to 10 of the present invention.
11 to 13 are graphs showing the measurement of the mechanical strength of the biodegradable polyurethane film prepared through Examples 1 to 14 of the present invention.
14 is a graph showing the measurement of the biodegradability of the biodegradable polyurethane film prepared through Examples 1 to 5 of the present invention.
이하에는, 본 발명의 바람직한 실시예와 각 성분의 물성을 상세하게 설명하되, 이는 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자가 발명을 용이하게 실시할 수 있을 정도로 상세하게 설명하기 위한 것이지, 이로 인해 본 발명의 기술적인 사상 및 범주가 한정되는 것을 의미하지는 않는다.Hereinafter, a preferred embodiment of the present invention and the physical properties of each component will be described in detail, which is intended to describe in detail enough that a person of ordinary skill in the art to which the present invention pertains can easily carry out the invention, This does not mean that the technical spirit and scope of the present invention is limited.
본 발명에 따른 음이온성 수분산 폴리우레탄 분산액의 제조방법은 케스터오일(Castor Oil)과 디메틸올부탄산(Dimethylolbutanoic Acid, DMBA)을 교반하면서 이소포론디이소시아네이트(Isophorone Diisocyanate, IPDI)를 적하(滴下)하여 교반하는 원료혼합단계(S101), 상기 원료혼합단계(S101)를 통해 제조된 혼합물에 아세톤을 혼합하고 합성하는 우레탄합성단계(S103), 상기 우레탄합성단계(S103)를 통해 합성된 우레탄을 냉각한 후에 트리에틸아민을 혼합하여 중화하는 중화단계(S105), 상기 중화단계(S105)를 통해 중화된 우레탄에 증류수를 투입하고 교반하는 증류수교반단계(S107) 및 상기 증류수교반단계(S107)를 통해 증류수가 혼합된 우레탄에 함유된 아세톤을 제거하는 아세톤제거단계(S109)로 이루어진다.The method for preparing an anionic water-dispersed polyurethane dispersion according to the present invention is to drop Isophorone Diisocyanate (IPDI) while stirring Castor Oil and dimethylolbutanoic acid (DMBA). Stirring raw material mixing step (S101), urethane synthesis step (S103) of mixing and synthesizing acetone with the mixture prepared through the raw material mixing step (S101), and cooling the urethane synthesized through the urethane synthesis step (S103) After the neutralization step (S105) of mixing and neutralizing triethylamine, distilled water is added to the urethane neutralized through the neutralization step (S105) and distilled water is stirred (S107) and distilled water through the stirring step (S107) consists of an acetone removal step (S109) of removing the acetone contained in the mixed urethane.
상기 원료혼합단계(S101)는 케스터오일과 디메틸올부탄산을 교반하면서 이소포론디이소시아네이트를 적하하여 교반하는 단계로, 케스터오일 100 중량부에 디메틸올부탄산 10 내지 30 중량부를 75 내지 80℃의 온도와 200 내지 300rpm의 속도로 교반하면서 이소포론디이소시아네이트 50 내지 80 중량부를 적하하는 과정으로 이루어진다.The raw material mixing step (S101) is a step of adding isophorone diisocyanate dropwise while stirring the castor oil and dimethylol butanoic acid and stirring, and 10 to 30 parts by weight of dimethylol butanoic acid to 100 parts by weight of the castor oil at a temperature of 75 to 80° C. It consists of a process of dropping 50 to 80 parts by weight of isophorone diisocyanate while stirring at a speed of 200 to 300 rpm.
이때, 상기의 케스터오일, 디메틸올부탄산 및 이소포론디이소시아네이트의 교반은 질소주입구(nitrogen inlet), 기계식 교반기(chanical stirrer) 및 컨덴서(condenser)가 장착된 4구 플라스크에서 이루어질 수 있다.At this time, the stirring of the castor oil, dimethylol butanoic acid and isophorone diisocyanate can be made in a four-necked flask equipped with a nitrogen inlet, a mechanical stirrer and a condenser.
상기 우레탄합성단계(S103)는 상기 원료혼합단계(S101)를 통해 제조된 혼합물에 아세톤을 혼합하고 합성하는 단계로, 상기 원료혼합단계(S101)를 통해 제조된 혼합물에 함유된 케스터오일 100 중량부 대비 아세톤 100 내지 500 중량부를 혼합하고 200 내지 300rpm의 속도로 60 내지 120분 동안 교반하여 이루어지는데, 상기 아세톤은 한번에 일시적으로 첨가하는 것보다는 우레탄의 합성과정이나 상기의 중화단계에서 혼합물의 점도 등을 관찰하면서 투입하는 것이 바람직하다. The urethane synthesis step (S103) is a step of mixing and synthesizing acetone with the mixture prepared through the raw material mixing step (S101), and 100 parts by weight of castor oil contained in the mixture prepared through the raw material mixing step (S101) It is made by mixing 100 to 500 parts by weight of acetone and stirring at a speed of 200 to 300 rpm for 60 to 120 minutes, and the acetone is not added temporarily at once, but rather in the synthesis process of urethane or the viscosity of the mixture in the neutralization step. It is preferable to inject while observing.
상기 우레탄합성단계(S103)에서 아세톤의 함량을 조절하여 합성되는 우레탄의 점도와 입자크기를 조절할 수 있다.The viscosity and particle size of the synthesized urethane can be adjusted by adjusting the content of acetone in the urethane synthesis step (S103).
상기 중화단계(S105)는 상기 우레탄합성단계(S103)를 통해 합성된 우레탄을 냉각한 후에 트리에틸아민을 혼합하여 중화하는 단계로, 상기 우레탄합성단계(S103)를 통해 합성된 우레탄을 40 내지 50℃의 온도로 냉각한 후에, 상기 우레탄에 함유된 케스터오일 100 중량부 대비 트리에틸아민 15 내지 20 중량부를 혼합하고 300 내지 400rpm의 속도로 30 내지 60분 동안 교반하는 과정으로 이루어진다.The neutralization step (S105) is a step of neutralizing by mixing triethylamine after cooling the urethane synthesized through the urethane synthesis step (S103). The urethane synthesized through the urethane synthesis step (S103) is 40 to 50 After cooling to a temperature of ℃, 15 to 20 parts by weight of triethylamine based on 100 parts by weight of castor oil contained in the urethane is mixed and stirred at a speed of 300 to 400 rpm for 30 to 60 minutes.
상기 증류수교반단계(S107)는 상기 중화단계(S105)를 통해 중화된 우레탄에 증류수를 투입하고 교반하는 단계로, 상기 중화단계(S105)를 통해 트리에틸아민으로 중화된 우레탄을 550 내지 650rpm의 속도로 교반하면서 증류수 100 내지 300 중량부를 혼합하고 100 내지 150분 동안 교반하는 과정으로 이루어진다.The distilled water stirring step (S107) is a step of adding distilled water to the urethane neutralized through the neutralization step (S105) and stirring, the urethane neutralized with triethylamine through the neutralization step (S105) at a speed of 550 to 650 rpm It consists of a process of mixing 100 to 300 parts by weight of distilled water while stirring and stirring for 100 to 150 minutes.
상기와 같이 증류수가 혼합되어 음이온성 수분산 폴리우레탄 분산액을 제조하는 과정을 아래 도 2에 나타내었다.The process of preparing an anionic aqueous dispersion polyurethane dispersion by mixing distilled water as described above is shown in FIG. 2 below.
이때, 상기 증류수 100 중량부 대비 사슬확장제 0.01 내지 5 중량부가 더 함유될 수도 있으며, 상기 사슬확장제는 나노셀룰로오스(RCNs), 키틴나노섬유(Chitin Nanofibers, ChNF) 및 카르복시메틸키토산(Carboxymethyl Chitosan, CS)으로 이루어진 그룹에서 선택된 하나 이상으로 이루어지는 것이 바람직하다.In this case, 0.01 to 5 parts by weight of a chain extender may be further contained relative to 100 parts by weight of the distilled water, and the chain extender is nanocellulose (RCNs), chitin nanofibers (ChNF) and carboxymethyl chitosan (Carboxymethyl Chitosan, CS) It is preferably made of one or more selected from the group consisting of.
상기와 같이 사슬확장제로 나노셀룰로오스를 사용하여 음이온성 수분산 폴리우레탄 분산액을 제조하는 과정은 아래 도 3에 나타내었으며, 상기 사슬확장제로 키틴나노섬유를 사용하여 음이온성 수분산 폴리우레탄 분산액을 제조하는 과정은 아래 도 4에 나타내었고, 상기 사슬확장제로 카르복시메틸키토산을 사용하여 음이온성 수분산 폴리우레탄 분산액을 제조하는 과정은 아래 도 5에 나타내었다.The process of preparing an anionic water-dispersed polyurethane dispersion using nanocellulose as a chain extender as described above is shown in FIG. 3 below, and an anionic water-dispersed polyurethane dispersion using chitin nanofibers as the chain extender. The process is shown in FIG. 4 below, and the process of preparing an anionic aqueous dispersion polyurethane dispersion using carboxymethylchitosan as the chain extender is shown in FIG. 5 below.
이때, 상기 나노셀룰로오스는 마이크로셀룰로오스(MCC)로부터 수산화나트륨(NaOH)과 우레아(Urea)를 이용하여 pH 8 수준으로 재생된 나노셀룰로오스(RCNs)로서 결정화도가 낮은 반결정성의 입자특성을 나타내는데, 질량농도가 7%인 수산화나트륨과 질량농도가 12%인 우레아를 이용하고 질량농도가 5%인 마이크로 셀룰로오스(MCC) 함유용액을 실온에서 2시간 동안 교반하고, -20℃의 온도에서 12시간 동안 냉동기에 보관한 후에 원심분리를 통해 재생된 셀룰로오스의 침전 및 분리공정을 거쳐 얻어진 용액을 초음파처리하고 pH를 약 8로 조정하는 과정을 통해 제조될 수 있다.At this time, the nanocellulose is nanocellulose (RCNs) regenerated from microcellulose (MCC) to a pH of 8 using sodium hydroxide (NaOH) and urea (Urea), and exhibits semi-crystalline particle characteristics with low crystallinity, mass concentration Using sodium hydroxide of 7% and urea having a mass concentration of 12%, and a solution containing microcellulose (MCC) having a mass concentration of 5% was stirred at room temperature for 2 hours, and placed in a refrigerator at a temperature of -20°C for 12 hours. After storage, it can be prepared by sonicating the solution obtained through precipitation and separation of cellulose regenerated through centrifugation and adjusting the pH to about 8.
상기의 성분으로 이루어지는 사슬확장제는 본 발명에 따른 음이온성 수분산 폴리우레탄 분산액으로 제조되는 폴리우레탄 필름의 분자량을 증가시켜 기계적 물성을 향상시킬 뿐만 아니라, 생분해성이 우수한 성분으로 이루어져 생분해성이 향상된 폴리우레탄 필름을 제공하는 역할을 한다.The chain extender composed of the above components not only improves mechanical properties by increasing the molecular weight of the polyurethane film prepared from the anionic water-dispersed polyurethane dispersion according to the present invention, but also improves biodegradability of poly It serves to provide a urethane film.
상기 아세톤제거단계(S109)는 상기 증류수교반단계(S107)를 통해 증류수가 혼합된 우레탄에 함유된 아세톤을 제거하는 단계로, 상기 증류수교반단계(S107)를 통해 증류수가 혼합된 우레탄에 함유된 아세톤을 진공건조기를 이용하여 제거하는 과정으로 이루어지는데, 상기의 과정을 통해 아세톤이 제거된 우레탄은 질량농도가 18 내지 20%인 음이온성 수분산 폴리우레탄 분산액으로 제조된다.The acetone removal step (S109) is a step of removing the acetone contained in the urethane mixed with distilled water through the distilled water stirring step (S107), and the acetone contained in the distilled water mixed urethane through the distilled water stirring step (S107) is removed using a vacuum dryer, and the urethane from which acetone has been removed through the above process is prepared as an anionic aqueous dispersion polyurethane dispersion having a mass concentration of 18 to 20%.
또한, 본 발명에 따른 생분해성 폴리우레탄 필름은 상기의 아세톤제거단계(S109)를 통해 제조된 음이온성 수분산 폴리우레탄 분산액을 몰드가 설치된 유리판에 캐스팅한 후에 건조하는 과정으로 이루어지는데, 상기 건조는 24 내지 26℃의 온도와 70 내지 80%의 상대습도를 나타내는 항온항습기에서 6 내지 8일 동안 1차로 건조하여 폴리우레탄 필름을 제조한 후에, 상기 폴리우레탄 필름을 28 내지 32℃의 진공건조기에서 23 내지 25시간 동안 추가로 건조하는 과정으로 이루어지는 것이 바람직하다.In addition, the biodegradable polyurethane film according to the present invention consists of a process of drying after casting the anionic water-dispersed polyurethane dispersion prepared through the acetone removal step (S109) on a glass plate on which a mold is installed, wherein the drying is After the polyurethane film was prepared by first drying for 6 to 8 days in a constant temperature and humidifier showing a temperature of 24 to 26 ° C and a relative humidity of 70 to 80%, the polyurethane film was dried in a vacuum dryer at 28 to 32 ° C. 23 It is preferable to consist of a process of further drying for 25 hours.
상기의 과정을 통해 제조되는 폴리우레탄 필름은 투명도가 75% 이상을 나타내며, 370시간 후에 생분해도가 최대 15% 이상을 나타낼 수 있다.The polyurethane film produced through the above process may exhibit a transparency of 75% or more, and a biodegradability of up to 15% or more after 370 hours.
이하에서는, 본 발명에 따른 음이온성 수분산 폴리우레탄 분산액의 제조방법 및 그 제조방법으로 제조된 분산액으로 제조된 생분해성 폴리우레탄 필름의 물성을 실시예를 들어 설명하기로 한다.Hereinafter, the method for preparing an anionic water-dispersed polyurethane dispersion according to the present invention and the physical properties of the biodegradable polyurethane film prepared with the dispersion prepared by the manufacturing method will be described with reference to Examples.
<제조예 1><Production Example 1>
질소 주입구, 기계식 교반기 및 컨덴서가 구비된 4구 플라스크에 케스터오일22.497g과 DMBA 3.465g를 넣고 250rpm으로 78℃에서 교반하면서 IPDI 16.748g을 적하한 후에, 아세톤 40.086g을 혼합하고 250rpm의 속도로 90분 동안 교반하여 우레탄을 합성하고, 상기 합성된 우레탄을 40℃로 냉각한 후에 트리에틸아민 4.095g을 혼합하고 30분 동안 350rpm으로 교반하여 중화하고, 중화된 우레탄을 600rpm의 속도로 교반하면서 증류수 150mL를 투입하고 120분 동안 교반한 후에 진공건조기(DAIHAN Scientific, KOREA)를 이용하여 아세톤을 제거하는 과정을 통해 음이온성 수분산 폴리우레탄 분산액(CWPU 1/2.08/0.65)을 제조하였다.22.497 g of castor oil and 3.465 g of DMBA were put into a four-neck flask equipped with a nitrogen inlet, mechanical stirrer and condenser, and 16.748 g of IPDI was added dropwise while stirring at 250 rpm at 78 ° C., 40.086 g of acetone was mixed and 90 at a speed of 250 rpm. After stirring for a minute to synthesize urethane, after cooling the synthesized urethane to 40° C., 4.095 g of triethylamine was mixed and neutralized by stirring at 350 rpm for 30 minutes, and 150 mL of distilled water while stirring the neutralized urethane at a speed of 600 rpm After adding and stirring for 120 minutes, an anionic aqueous dispersion polyurethane dispersion (
<제조예 2><Production Example 2>
상기 제조예 1과 동일하게 진행하되, DMBA 5.317g을 투입하고, 아세톤 34.584g을 사용하여 음이온성 수분산 폴리우레탄 분산액(CWPU 1/2.08/0.99)을 제조하였다.Proceeds in the same manner as in Preparation Example 1, except that 5.317 g of DMBA was added and 34.584 g of acetone was used to prepare an anionic aqueous dispersion polyurethane dispersion (
<제조예 3><Production Example 3>
상기 제조예 1과 동일하게 진행하되, DMBA 6.3912g을 투입하고, IPDI 17.727g 및 아세톤 61.308g을 사용하여 음이온성 수분산 폴리우레탄 분산액(CWPU 1/2.20/1.19)을 제조하였다.Proceeds in the same manner as in Preparation Example 1, except that 6.3912 g of DMBA was added, IPDI 17.727 g and acetone 61.308 g were used to prepare an anionic aqueous dispersion polyurethane dispersion (
<실시예 1><Example 1>
상기 제조예 1을 통해 제조된 음이온성 수분산 폴리우레탄 분산액을 몰드가 설치된 유리판 위에 캐스팅하고 항온항습기(섭씨온도 25℃, 상대습도 75%)에서 7일 동안 건조한 후에 진공건조기(섭씨온도 30℃)에서 24시간 동안 건조하여 생분해성 폴리우레탄 필름(CWPU)을 제조하였다.The anionic water-dispersed polyurethane dispersion prepared in Preparation Example 1 was cast on a glass plate with a mold installed and dried in a constant temperature and humidity machine (25° C., relative humidity 75%) for 7 days, followed by a vacuum dryer (30° C.) and dried for 24 hours to prepare a biodegradable polyurethane film (CWPU).
<실시예 2><Example 2>
질소 주입구, 기계식 교반기 및 컨덴서가 구비된 4구 플라스크에 케스터오일22.497g과 DMBA 3.465g를 넣고 250rpm으로 78℃에서 교반하면서 IPDI 16.748g을 적하한 후에, 아세톤 40.086g을 혼합하고 250rpm의 속도로 90분 동안 교반하여 우레탄을 합성하고, 상기 합성된 우레탄을 40℃로 냉각한 후에 트리에틸아민 4.095g을 혼합하고 30분 동안 350rpm으로 교반하여 중화하고, 중화된 우레탄을 600rpm의 속도로 교반하면서 증류수 145mL 및 나노셀룰로오스 0.05g을 투입하고 120분 동안 교반한 후에 진공건조기(DAIHAN Scientific, KOREA)를 이용하여 아세톤을 제거하는 과정을 통해 음이온성 수분산 폴리우레탄 분산액을 제조하고, 제조된 음이온성 수분산 폴리우레탄 분산액을 몰드가 설치된 유리판 위에 캐스팅하고 항온항습기(섭씨온도 25℃, 상대습도 75%)에서 7일 동안 건조한 후에 진공건조기(섭씨온도 30℃)에서 24시간 동안 건조하여 생분해성 폴리우레탄 필름(CWPU/RNC 0.18)을 제조하였다.22.497 g of castor oil and 3.465 g of DMBA were put into a four-neck flask equipped with a nitrogen inlet, mechanical stirrer and condenser, and 16.748 g of IPDI was added dropwise while stirring at 250 rpm at 78 ° C., 40.086 g of acetone was mixed and 90 at a speed of 250 rpm. After stirring for a minute to synthesize urethane, after cooling the synthesized urethane to 40 ° C, 4.095 g of triethylamine was mixed and neutralized by stirring at 350 rpm for 30 minutes, and 145 mL of distilled water while stirring the neutralized urethane at a speed of 600 rpm And 0.05 g of nanocellulose was added and stirred for 120 minutes, and then an anionic water-dispersed polyurethane dispersion was prepared through a process of removing acetone using a vacuum dryer (DAIHAN Scientific, KOREA), and the prepared anionic water-dispersed poly The urethane dispersion is cast on a glass plate with a mold installed and dried for 7 days in a constant temperature and humidity machine (25 ° C., relative humidity 75%), and then dried in a vacuum dryer (30 ° C.) for 24 hours to form a biodegradable polyurethane film (CWPU). /RNC 0.18) was prepared.
<실시예 3><Example 3>
상기 실시예 2와 동일하게 진행하되, 증류수 140mL 및 나노셀룰로오스 0.1g을 투입하여 생분해성 폴리우레탄 필름(CWPU/RNC 0.37)을 제조하였다.The same procedure as in Example 2, except that 140 mL of distilled water and 0.1 g of nanocellulose were added to prepare a biodegradable polyurethane film (CWPU/RNC 0.37).
<실시예 4><Example 4>
상기 실시예 2와 동일하게 진행하되, 증류수 135mL 및 나노셀룰로오스 0.15g을 투입하여 생분해성 폴리우레탄 필름(CWPU/RNC 0.58)을 제조하였다.The same procedure as in Example 2, except that 135 mL of distilled water and 0.15 g of nanocellulose were added to prepare a biodegradable polyurethane film (CWPU/RNC 0.58).
<실시예 5><Example 5>
상기 실시예 2와 동일하게 진행하되, 증류수 130mL 및 나노셀룰로오스 0.2g을 투입하여 생분해성 폴리우레탄 필름(CWPU/RNC 0.76)을 제조하였다.The same procedure as in Example 2, except that 130 mL of distilled water and 0.2 g of nanocellulose were added to prepare a biodegradable polyurethane film (CWPU/RNC 0.76).
<실시예 6><Example 6>
질소 주입구, 기계식 교반기 및 컨덴서가 구비된 4구 플라스크에 케스터오일14.998g과 DMBA 2.79g를 넣고 250rpm으로 78℃에서 교반하면서 IPDI 11.13g을 적하한 후에, 아세톤 28.296g을 혼합하고 250rpm의 속도로 90분 동안 교반하여 우레탄을 합성하고, 상기 합성된 우레탄을 50℃로 냉각한 후에 트리에틸아민 2.7225g을 혼합하고 60분 동안 350rpm으로 교반하여 중화하고, 중화된 우레탄을 600rpm의 속도로 교반하면서 증류수 150mL 및 키틴나노섬유 0.5g을 투입하고 120분 동안 교반한 후에 진공건조기(DAIHAN Scientific, KOREA)를 이용하여 아세톤을 제거하는 과정을 통해 음이온성 수분산 폴리우레탄 분산액을 제조하고, 제조된 음이온성 수분산 폴리우레탄 분산액을 몰드가 설치된 유리판 위에 캐스팅하고 항온항습기(섭씨온도 25℃, 상대습도 75%)에서 7일 동안 건조한 후에 진공건조기(섭씨온도 30℃)에서 24시간 동안 건조하여 생분해성 폴리우레탄 필름(CWPU/ChNF 0.13)을 제조하였다.Put 14.998 g of castor oil and 2.79 g of DMBA into a four-necked flask equipped with a nitrogen inlet, mechanical stirrer, and condenser, and add 11.13 g of IPDI dropwise while stirring at 250 rpm at 78 ° C. Then, 28.296 g of acetone is mixed and 90 at a speed of 250 rpm After stirring for a minute to synthesize urethane, and after cooling the synthesized urethane to 50 ° C, 2.7225 g of triethylamine was mixed and neutralized by stirring at 350 rpm for 60 minutes, and 150 mL of distilled water while stirring the neutralized urethane at a speed of 600 rpm And 0.5 g of chitin nanofibers were added and stirred for 120 minutes, and then an anionic aqueous dispersion polyurethane dispersion was prepared through a process of removing acetone using a vacuum dryer (DAIHAN Scientific, KOREA), and the prepared anionic aqueous dispersion The polyurethane dispersion was cast on a glass plate with a mold installed and dried for 7 days in a constant temperature and humidity machine (25 ° C., relative humidity 75%), and then dried in a vacuum dryer (30 ° C.) for 24 hours to make a biodegradable polyurethane film ( CWPU/ChNF 0.13) was prepared.
<실시예 7><Example 7>
상기 실시예 6과 동일하게 진행하되, 키틴나노섬유 0.75g을 투입하여 생분해성 폴리우레탄 필름(CWPU/ChNF 0.35)을 제조하였다.Proceeded in the same manner as in Example 6, but 0.75 g of chitin nanofibers were added to prepare a biodegradable polyurethane film (CWPU/ChNF 0.35).
<실시예 8><Example 8>
상기 실시예 6과 동일하게 진행하되, 키틴나노섬유 1.5g을 투입하여 생분해성 폴리우레탄 필름(CWPU/ChNF 1.08)을 제조하였다.The same procedure as in Example 6, except that 1.5 g of chitin nanofibers were added to prepare a biodegradable polyurethane film (CWPU/ChNF 1.08).
<실시예 9><Example 9>
상기 실시예 6과 동일하게 진행하되, 키틴나노섬유 2.0g을 투입하여 생분해성 폴리우레탄 필름(CWPU/ChNF 2.17)을 제조하였다.The same procedure as in Example 6, but 2.0 g of chitin nanofibers were added to prepare a biodegradable polyurethane film (CWPU/ChNF 2.17).
<실시예 10><Example 10>
상기 실시예 6과 동일하게 진행하되, 키틴나노섬유 5.0g을 투입하여 생분해성 폴리우레탄 필름(CWPU/ChNF 21.7)을 제조하였다.Except in the same manner as in Example 6, 5.0 g of chitin nanofibers were added to prepare a biodegradable polyurethane film (CWPU/ChNF 21.7).
<실시예 11><Example 11>
질소 주입구, 기계식 교반기 및 컨덴서가 구비된 4구 플라스크에 케스터오일10g과 DMBA 1.86g를 넣고 250rpm으로 78℃에서 교반하면서 IPDI 7.42g을 적하한 후에, 아세톤 49.518g을 혼합하고 250rpm의 속도로 90분 동안 교반하여 우레탄을 합성하고, 상기 합성된 우레탄을 40℃로 냉각한 후에 트리에틸아민 1.72g을 혼합하고 60분 동안 350rpm으로 교반하여 중화하고, 중화된 우레탄을 600rpm의 속도로 교반하면서 증류수 180mL 및 카르복시메틸키토산 0.405g을 투입하고 120분 동안 교반한 후에 진공건조기(DAIHAN Scientific, KOREA)를 이용하여 아세톤을 제거하는 과정을 통해 음이온성 수분산 폴리우레탄 분산액을 제조하고, 제조된 음이온성 수분산 폴리우레탄 분산액을 몰드가 설치된 유리판 위에 캐스팅하고 항온항습기(섭씨온도 25℃, 상대습도 75%)에서 7일 동안 건조한 후에 진공건조기(섭씨온도 30℃)에서 24시간 동안 건조하여 생분해성 폴리우레탄 필름(CWPU/CS 1.13)을 제조하였다.Put 10 g of castor oil and 1.86 g of DMBA into a 4-neck flask equipped with a nitrogen inlet, mechanical stirrer and condenser, and add 7.42 g of IPDI while stirring at 250 rpm at 78 ° C. urethane is synthesized by stirring for After adding 0.405 g of carboxymethyl chitosan and stirring for 120 minutes, an anionic water-dispersed polyurethane dispersion was prepared through the process of removing acetone using a vacuum dryer (DAIHAN Scientific, KOREA), and the prepared anionic water-dispersed poly The urethane dispersion is cast on a glass plate with a mold installed and dried for 7 days in a constant temperature and humidity machine (25 ° C., relative humidity 75%), and then dried in a vacuum dryer (30 ° C.) for 24 hours to form a biodegradable polyurethane film (CWPU). /CS 1.13) was prepared.
<실시예 12><Example 12>
상기 실시예 11과 동일하게 진행하되, 카르복시메틸키토산 0.810g을 투입하여 생분해성 폴리우레탄 필름(CWPU/CS 2.25)을 제조하였다.The same procedure as in Example 11, but 0.810 g of carboxymethylchitosan was added to prepare a biodegradable polyurethane film (CWPU/CS 2.25).
<실시예 13><Example 13>
상기 실시예 11과 동일하게 진행하되, 카르복시메틸키토산 1.620g을 투입하여 생분해성 폴리우레탄 필름(CWPU/CS 4.47)을 제조하였다.The same procedure as in Example 11, except that 1.620 g of carboxymethyl chitosan was added to prepare a biodegradable polyurethane film (CWPU/CS 4.47).
<실시예 14><Example 14>
상기 실시예 11과 동일하게 진행하되, 카르복시메틸키토산 2.430g을 투입하여 생분해성 폴리우레탄 필름(CWPU/CS 6.75)을 제조하였다.The same procedure as in Example 11, but 2.430 g of carboxymethyl chitosan was added to prepare a biodegradable polyurethane film (CWPU/CS 6.75).
상기 제조예 1 내지 3을 통해 제조된 음이온성 수분산 폴리우레탄 분산액의 점도변화(a)와 입자크기(b)를 측정하여 아래 도 6에 나타내었다.The viscosity change (a) and particle size (b) of the anionic aqueous dispersion polyurethane dispersion prepared in Preparation Examples 1 to 3 were measured and shown in FIG. 6 below.
아래 도 6에 나타낸 것처럼, 본 발명의 제조예 1 내지 3을 통해 제조된 음이온성 수분산 폴리우레탄 분산액은 케스터오일, 디메틸올부탄산, 이소포론디이소시아네이트 및 아세톤의 함량에 따라 다양한 점도와 입자크기를 나타내는 것을 알 수 있다.As shown in FIG. 6 below, the anionic aqueous dispersion polyurethane dispersions prepared in Preparation Examples 1 to 3 of the present invention have various viscosities and particle sizes according to the contents of castor oil, dimethylol butanoic acid, isophorone diisocyanate and acetone. can be seen to indicate
또한, 상기 실시예 1 내지 14를 통해 제조된 생분해성 폴리우레탄 필름의 투명도를 측정하여 아래 도 7 내지 8에 나타내었다.In addition, the transparency of the biodegradable polyurethane film prepared in Examples 1 to 14 was measured and shown in FIGS. 7 to 8 below.
아래 도 7 내지 8에 나타낸 것처럼, 본 발명의 실시예 2 내지 14와 같이 폴리우레탄 필름의 물성개선을 위해 나노셀룰로오스, 키틴나노섬유 및 카르복시메틸키토산이 함유되더라도 실시예 1을 통해 제조된 생분해성 폴리우레탄 필름에 비해 투명도가 크게 저하되지 않는 것을 알 수 있다.As shown in FIGS. 7 to 8 below, as in Examples 2 to 14 of the present invention, even if nanocellulose, chitin nanofiber and carboxymethyl chitosan are contained to improve the physical properties of the polyurethane film, the biodegradable poly prepared in Example 1 It can be seen that the transparency is not significantly reduced compared to the urethane film.
또한, 상기 실시예 1 내지 5 및 실시예 7 내지 10을 통해 제조된 생분해성 폴리우레탄 필름의 투과도를 측정하여 아래 도 9 내지 10에 나타내었다.In addition, the transmittance of the biodegradable polyurethane film prepared in Examples 1 to 5 and Examples 7 to 10 was measured and shown in FIGS. 9 to 10 below.
아래 도 9 내지 10에 나타낸 것처럼, 본 발명의 실시예 2 내지 5 및 실시예 7 내지 10을 통해 제조된 폴리우레탄 필름은 실시예 1을 통해 제조된 폴리우레탄 필름과 대등한 투과도를 나타내었으며, 모두 75% 이상의 투과도를 나타내는 것을 알 수 있다.As shown in FIGS. 9 to 10 below, the polyurethane films prepared through Examples 2 to 5 and Examples 7 to 10 of the present invention exhibited transmittance comparable to that of the polyurethane film prepared through Example 1, and all It can be seen that the transmittance is 75% or more.
또한, 상기 실시예 1 내지 14를 통해 제조된 생분해성 폴리우레탄 필름의 기계적 강도를 측정하여 아래 도 11 내지 13에 나타내었다.In addition, the mechanical strength of the biodegradable polyurethane film prepared in Examples 1 to 14 was measured and shown in FIGS. 11 to 13 below.
{단, 기계적 강도는 상기 실시예 1 내지 14를 통해 제조된 생분해성 폴리우레탄 필름을 20mm의 길이와 폭 5mm의 크기로 시편화한 후에, 50mm/min의 인장속도 조건에서 인장강도, 변형률, 초기탄성률 및 인성 등을 인장시험기인 AGS-500D(Autograph,japan)을 이용하여 측정하는 방법을 이용하였다.}{However, the mechanical strength is measured after specimens of the biodegradable polyurethane films prepared in Examples 1 to 14 to a size of 20 mm in length and 5 mm in width, tensile strength, strain, and initial A method of measuring elastic modulus and toughness using a tensile tester AGS-500D (Autograph, Japan) was used.}
아래 도 11 내지 13에 나타낸 것처럼, 본 발명의 실시예 2 내지 14와 같이 나노셀룰로오스, 키틴나노섬유 및 카르복시메틸키토산이 함유되면 폴리우레탄 필름의 기계적 강도가 월등하게 향상되는 것을 알 수 있다.11 to 13 below, as in Examples 2 to 14 of the present invention, when nanocellulose, chitin nanofiber and carboxymethyl chitosan are contained, it can be seen that the mechanical strength of the polyurethane film is remarkably improved.
또한, 상기 실시예 1 내지 5를 통해 제조된 생분해성 폴리우레탄 필름의 생분해도를 측정하여 아래 도 14에 나타내었다.In addition, the degree of biodegradation of the biodegradable polyurethane film prepared in Examples 1 to 5 was measured and shown in FIG. 14 below.
{단, 상기 실시예 1 내지 5를 통해 제조된 생분해성 폴리우레탄 필름의 생분해도는 {However, the degree of biodegradation of the biodegradable polyurethane film prepared in Examples 1 to 5 is
1. 실시예 1 내지 5를 통해 제조된 생분해성 폴리우레탄 필름을 0.225g으로 맞추어서 각 조건별로 3개씩 준비하고,1. By adjusting the biodegradable polyurethane film prepared in Examples 1 to 5 to 0.225 g, prepare three for each condition,
2. Citrate Buffer 제조2. Preparation of Citrate Buffer
2-1. DDW 800ml + Sodium Citrate 6.702g2-1. DDW 800ml + Sodium Citrate 6.702g
2-2. 1번 용액 + Citric Acid 5.227g2-2.
2-3. stirring 2h2-3. stirring 2h
2-4. pH 4.32-4. pH 4.3
3. 50 mL conical tube에 Citrate Buffer 45mL 첨가3. Add 45mL Citrate Buffer to 50mL conical tube
4. 3번에 각각의 필름 첨가하고 1hr 후 팽윤 무게 측정4. Add each film in No. 3 and measure the swelling weight after 1 hr
5. Cellulase 0.0135g 첨가(*40h 후 0.027g 추가)5. Add 0.0135g of Cellulase (add 0.027g after *40h)
6. 각 필름의 무게 측정6. Weigh each film
7. 각 필름의 최대 팽윤시를 기준으로 무게감소를 %로 나타내는 방법을 이용하였다. ※ film 0.225g : Citric buffer (pH4.3) 45ml : Cellulase 0.040g}7. Based on the maximum swelling time of each film, a method of expressing weight loss in % was used. ※ film 0.225g: Citric buffer (pH4.3) 45ml: Cellulase 0.040g}
아래 도 14에 나타낸 것처럼, 본 발명의 실시예 1 내지 5를 통해 제조된 폴리우레탄 필름은 우수한 생분해도를 나타내었으며, 특히 본 발명의 실시예 5를 통해 제조된 폴리우레탄 필름의 생분해도가 가장 우수한 것을 알 수 있다.As shown in FIG. 14 below, the polyurethane films prepared through Examples 1 to 5 of the present invention exhibited excellent biodegradability, and in particular, the polyurethane film prepared through Example 5 of the present invention exhibited the best biodegradability. it can be seen that
따라서, 본 발명에 따른 수분산 폴리우레탄 분산액의 제조방법 및 그 분산액으로 제조된 생분해성 폴리우레탄 필름은 인체에 해로운 촉매제를 사용하지 않으면서도, 점도조절제로 아세톤을 사용하고 사슬확장제로 천연성분을 사용하여 우수한 생분해성, 기계적 물성 및 투명도를 나타내는 폴리우레탄 필름을 제공할 수 있다.Therefore, the method for producing a water-dispersed polyurethane dispersion according to the present invention and the biodegradable polyurethane film prepared from the dispersion use acetone as a viscosity modifier and a natural component as a chain extender without using a catalyst harmful to the human body. Thus, it is possible to provide a polyurethane film exhibiting excellent biodegradability, mechanical properties, and transparency.
S101 ; 원료혼합단계
S103 ; 우레탄합성단계
S105 ; 중화단계
S107 ; 증류수교반단계
S109 ; 아세톤제거단계S101; Raw material mixing step
S103; Urethane synthesis step
S105 ; neutralization stage
S107; Distilled water stirring step
S109; Acetone removal step
Claims (7)
상기 원료혼합단계를 통해 제조된 혼합물에 아세톤을 혼합하고 합성하는 우레탄합성단계;
상기 우레탄합성단계를 통해 합성된 우레탄을 냉각한 후에 트리에틸아민을 혼합하여 중화하는 중화단계;
상기 중화단계를 통해 중화된 우레탄에 증류수를 투입하고 교반하는 증류수교반단계; 및
상기 증류수교반단계를 통해 증류수가 혼합된 우레탄에 함유된 아세톤을 제거하는 아세톤제거단계;로 이루어지는 것을 특징으로 하는 음이온성 수분산 폴리우레탄 분산액의 제조방법.
A raw material mixing step of adding isophorone diisocyanate dropwise while stirring castor oil and dimethylol butanoic acid and stirring;
A urethane synthesis step of mixing and synthesizing acetone with the mixture prepared through the raw material mixing step;
a neutralization step of neutralizing the urethane synthesized through the urethane synthesis step by mixing triethylamine after cooling;
Distilled water stirring step of adding distilled water to the urethane neutralized through the neutralization step and stirring; and
An acetone removal step of removing the acetone contained in the urethane mixed with distilled water through the distilled water stirring step;
상기 원료혼합단계는 케스터오일 100 중량부에 디메틸올부탄산 10 내지 30 중량부를 75 내지 80℃의 온도와 200 내지 300rpm의 속도로 교반하면서 이소포론디이소시아네이트 50 내지 80 중량부를 적하하여 이루어지는 것을 특징으로 하는 음이온성 수분산 폴리우레탄 분산액의 제조방법.
The method according to claim 1,
The raw material mixing step is performed by dropping 50 to 80 parts by weight of isophorone diisocyanate to 100 parts by weight of castor oil while stirring 10 to 30 parts by weight of dimethylol butanoic acid at a temperature of 75 to 80° C. and a speed of 200 to 300 rpm. A method for preparing an anionic water-dispersed polyurethane dispersion.
상기 우레탄합성단계는 상기 원료혼합단계를 통해 제조된 혼합물에 함유된 케스터오일 100 중량부 대비 아세톤 100 내지 500 중량부를 혼합하고 200 내지 300rpm의 속도로 60 내지 120분 동안 교반하여 이루어지는 것을 특징으로 하는 음이온성 수분산 폴리우레탄 분산액의 제조방법.
The method according to claim 1,
The urethane synthesis step is an anion, characterized in that by mixing 100 to 500 parts by weight of acetone with respect to 100 parts by weight of castor oil contained in the mixture prepared through the raw material mixing step and stirring at a speed of 200 to 300 rpm for 60 to 120 minutes A method for preparing an aqueous dispersion polyurethane dispersion.
상기 중화단계는 상기 우레탄합성단계를 통해 합성된 우레탄을 40 내지 50℃의 온도로 냉각한 후에 트리에틸아민을 혼합하고 300 내지 400rpm의 속도로 30 내지 60분 동안 교반하여 이루어지는 것을 특징으로 하는 음이온성 수분산 폴리우레탄 분산액의 제조방법.
The method according to claim 1,
The neutralization step is anionic, characterized in that the urethane synthesized through the urethane synthesis step is cooled to a temperature of 40 to 50° C., then triethylamine is mixed and stirred at a speed of 300 to 400 rpm for 30 to 60 minutes. A method for preparing an aqueous dispersion polyurethane dispersion.
상기 증류수교반단계에서는 상기 증류수 100 중량부에 사슬확장제 0.01 내지 5 중량부가 더 함유되며,
상기 사슬확장제는 나노셀룰로오스, 키틴나노섬유 및 카르복시메틸키토산으로 이루어진 그룹에서 선택된 하나 이상으로 이루어지는 것을 특징으로 하는 음이온성 수분산 폴리우레탄 분산액의 제조방법.
The method according to claim 1,
In the distilled water stirring step, 0.01 to 5 parts by weight of a chain extender is further contained in 100 parts by weight of the distilled water,
The chain extender is a method for producing an anionic aqueous dispersion polyurethane dispersion, characterized in that consisting of at least one selected from the group consisting of nanocellulose, chitin nanofibers and carboxymethyl chitosan.
A biodegradable polyurethane film, characterized in that it is prepared by casting the anionic water-dispersed polyurethane dispersion prepared by the manufacturing method according to any one of claims 1 to 5 on a glass plate on which a mold is installed and then drying.
상기 건조는 24 내지 26℃의 온도와 70 내지 80%의 상대습도를 나타내는 항온항습기에서 6 내지 8일동안 진행된 후에, 28 내지 32℃의 진공건조기에서 23 내지 25시간 동안 이루어지는 것을 특징으로 하는 생분해성 폴리우레탄 필름.7. The method of claim 6,
The drying is carried out for 6 to 8 days in a thermo-hygrostat showing a temperature of 24 to 26° C. and a relative humidity of 70 to 80%, followed by 23 to 25 hours in a vacuum dryer at 28 to 32° C. Biodegradable polyurethane film.
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CN116496550A (en) * | 2022-12-25 | 2023-07-28 | 广东工业大学 | Polymer capable of generating high-bionic intelligent hydrogel, double-network intelligent hydrogel, and preparation method and application thereof |
CN116496550B (en) * | 2022-12-25 | 2023-11-14 | 广东工业大学 | Polymer capable of generating high-bionic intelligent hydrogel, double-network intelligent hydrogel, and preparation method and application thereof |
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