KR100405195B1 - Elastic graft polymer with network structure for oil absorption, and process for preparing them - Google Patents
Elastic graft polymer with network structure for oil absorption, and process for preparing them Download PDFInfo
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- KR100405195B1 KR100405195B1 KR10-2000-0053586A KR20000053586A KR100405195B1 KR 100405195 B1 KR100405195 B1 KR 100405195B1 KR 20000053586 A KR20000053586 A KR 20000053586A KR 100405195 B1 KR100405195 B1 KR 100405195B1
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- South Korea
- Prior art keywords
- graft polymer
- oil
- network structure
- absorbent
- derivatives
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- 238000010521 absorption reaction Methods 0.000 title claims abstract description 37
- 229920000578 graft copolymer Polymers 0.000 title claims abstract description 31
- 238000004519 manufacturing process Methods 0.000 title abstract description 12
- 229920001971 elastomer Polymers 0.000 claims abstract description 57
- 239000002250 absorbent Substances 0.000 claims abstract description 28
- 239000000178 monomer Substances 0.000 claims abstract description 28
- 239000005060 rubber Substances 0.000 claims abstract description 28
- 229920002554 vinyl polymer Polymers 0.000 claims abstract description 24
- 230000002745 absorbent Effects 0.000 claims abstract description 23
- 239000003431 cross linking reagent Substances 0.000 claims abstract description 15
- 239000003999 initiator Substances 0.000 claims abstract description 11
- 125000001424 substituent group Chemical group 0.000 claims abstract description 9
- 125000001931 aliphatic group Chemical group 0.000 claims abstract description 7
- 239000000806 elastomer Substances 0.000 claims description 29
- 239000004745 nonwoven fabric Substances 0.000 claims description 22
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 21
- 229920000642 polymer Polymers 0.000 claims description 20
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims description 16
- 239000002904 solvent Substances 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 9
- 238000010559 graft polymerization reaction Methods 0.000 claims description 8
- 239000004342 Benzoyl peroxide Substances 0.000 claims description 7
- 235000019400 benzoyl peroxide Nutrition 0.000 claims description 7
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 6
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 6
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical class C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 claims description 5
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 4
- ZQMIGQNCOMNODD-UHFFFAOYSA-N diacetyl peroxide Chemical compound CC(=O)OOC(C)=O ZQMIGQNCOMNODD-UHFFFAOYSA-N 0.000 claims description 4
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical group C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 claims description 3
- 239000005062 Polybutadiene Substances 0.000 claims description 3
- 150000003926 acrylamides Chemical class 0.000 claims description 3
- 150000001252 acrylic acid derivatives Chemical class 0.000 claims description 3
- 229920002857 polybutadiene Polymers 0.000 claims description 3
- 229920003048 styrene butadiene rubber Polymers 0.000 claims description 3
- PRBHEGAFLDMLAL-GQCTYLIASA-N (4e)-hexa-1,4-diene Chemical compound C\C=C\CC=C PRBHEGAFLDMLAL-GQCTYLIASA-N 0.000 claims description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 claims description 2
- PAOHAQSLJSMLAT-UHFFFAOYSA-N 1-butylperoxybutane Chemical compound CCCCOOCCCC PAOHAQSLJSMLAT-UHFFFAOYSA-N 0.000 claims description 2
- LGJCFVYMIJLQJO-UHFFFAOYSA-N 1-dodecylperoxydodecane Chemical compound CCCCCCCCCCCCOOCCCCCCCCCCCC LGJCFVYMIJLQJO-UHFFFAOYSA-N 0.000 claims description 2
- AKUNSTOMHUXJOZ-UHFFFAOYSA-N 1-hydroperoxybutane Chemical compound CCCCOO AKUNSTOMHUXJOZ-UHFFFAOYSA-N 0.000 claims description 2
- HECLRDQVFMWTQS-RGOKHQFPSA-N 1755-01-7 Chemical compound C1[C@H]2[C@@H]3CC=C[C@@H]3[C@@H]1C=C2 HECLRDQVFMWTQS-RGOKHQFPSA-N 0.000 claims description 2
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 claims description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 claims description 2
- 150000001993 dienes Chemical class 0.000 claims description 2
- 150000002734 metacrylic acid derivatives Chemical class 0.000 claims description 2
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical class CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 claims description 2
- 150000007523 nucleic acids Chemical class 0.000 claims description 2
- 102000039446 nucleic acids Human genes 0.000 claims description 2
- 108020004707 nucleic acids Proteins 0.000 claims description 2
- 150000003440 styrenes Chemical class 0.000 claims description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 2
- XXJWUZQJPJLUNE-UHFFFAOYSA-N 2-[2-[2-(2-hydroxyethoxy)ethoxy]ethoxy]ethyl 3-methylbut-2-enoate Chemical compound CC(=CC(=O)OCCOCCOCCOCCO)C XXJWUZQJPJLUNE-UHFFFAOYSA-N 0.000 claims 1
- YYPNJNDODFVZLE-UHFFFAOYSA-N 3-methylbut-2-enoic acid Chemical class CC(C)=CC(O)=O YYPNJNDODFVZLE-UHFFFAOYSA-N 0.000 claims 1
- 238000004132 cross linking Methods 0.000 abstract description 10
- 238000001179 sorption measurement Methods 0.000 abstract description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 239000003921 oil Substances 0.000 description 41
- 238000006116 polymerization reaction Methods 0.000 description 19
- 239000000047 product Substances 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000010779 crude oil Substances 0.000 description 9
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 8
- 229920002943 EPDM rubber Polymers 0.000 description 4
- 229910052786 argon Inorganic materials 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 2
- 125000002877 alkyl aryl group Chemical group 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 230000002860 competitive effect Effects 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000001000 micrograph Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 description 2
- WOGITNXCNOTRLK-VOTSOKGWSA-N (e)-3-phenylprop-2-enoyl chloride Chemical compound ClC(=O)\C=C\C1=CC=CC=C1 WOGITNXCNOTRLK-VOTSOKGWSA-N 0.000 description 1
- HWSSEYVMGDIFMH-UHFFFAOYSA-N 2-[2-[2-(2-methylprop-2-enoyloxy)ethoxy]ethoxy]ethyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCOCCOCCOC(=O)C(C)=C HWSSEYVMGDIFMH-UHFFFAOYSA-N 0.000 description 1
- LTHJXDSHSVNJKG-UHFFFAOYSA-N 2-[2-[2-[2-(2-methylprop-2-enoyloxy)ethoxy]ethoxy]ethoxy]ethyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCOCCOCCOCCOC(=O)C(C)=C LTHJXDSHSVNJKG-UHFFFAOYSA-N 0.000 description 1
- DXIJHCSGLOHNES-UHFFFAOYSA-N 3,3-dimethylbut-1-enylbenzene Chemical compound CC(C)(C)C=CC1=CC=CC=C1 DXIJHCSGLOHNES-UHFFFAOYSA-N 0.000 description 1
- DBCAQXHNJOFNGC-UHFFFAOYSA-N 4-bromo-1,1,1-trifluorobutane Chemical compound FC(F)(F)CCCBr DBCAQXHNJOFNGC-UHFFFAOYSA-N 0.000 description 1
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- CNTQQRYOWMXVBJ-UHFFFAOYSA-N CC(=C)C(=O)OCOC(=O)C=CC1=CC=CC=C1 Chemical compound CC(=C)C(=O)OCOC(=O)C=CC1=CC=CC=C1 CNTQQRYOWMXVBJ-UHFFFAOYSA-N 0.000 description 1
- 241001391944 Commicarpus scandens Species 0.000 description 1
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-M acrylate group Chemical group C(C=C)(=O)[O-] NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- FACXGONDLDSNOE-UHFFFAOYSA-N buta-1,3-diene;styrene Chemical compound C=CC=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 FACXGONDLDSNOE-UHFFFAOYSA-N 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- STVZJERGLQHEKB-UHFFFAOYSA-N ethylene glycol dimethacrylate Substances CC(=C)C(=O)OCCOC(=O)C(C)=C STVZJERGLQHEKB-UHFFFAOYSA-N 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 210000003660 reticulum Anatomy 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002594 sorbent Substances 0.000 description 1
- 125000003011 styrenyl group Chemical group [H]\C(*)=C(/[H])C1=C([H])C([H])=C([H])C([H])=C1[H] 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F255/00—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00
- C08F255/02—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms
- C08F255/06—Macromolecular compounds obtained by polymerising monomers on to polymers of hydrocarbons as defined in group C08F10/00 on to polymers of olefins having two or three carbon atoms on to ethene-propene-diene terpolymers
-
- 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
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/24—Crosslinking, e.g. vulcanising, of macromolecules
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L51/04—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to rubbers
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Graft Or Block Polymers (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
본 발명은 망상구조를 가진 유흡수용 탄성 그라프트중합체와 이의 제조방법에 관한 것으로서, 더욱 상세하게는 불포화 결합의 함량(8%∼12%)이 적고, 내광성(△E=5∼14)이 우수한 특정 고무와, 탄소수 3 내지 18의 직쇄 또는 측쇄 치환기를 가진 지방족 또는 방향족 비닐 단량체를 가교제 및 개시제 첨가하에 그라프트 중합과 동시에 가교반응시켜 제조됨으로써, 탄성이 우수함은 물론 기름에 대한 선택적 흡착 및 흡수성이 크게 향상된 망상구조를 가진 유흡수용 탄성 그라프트중합체와 이의 제조방법에 관한 것이다.The present invention relates to an oil-absorbing elastic graft polymer having a network structure and a method for producing the same, more specifically, a content of unsaturated bonds (8% to 12%) is low, and light resistance (ΔE = 5 to 14) is low. It is prepared by crosslinking and reacting certain excellent rubbers with aliphatic or aromatic vinyl monomers having 3 to 18 carbon straight or branched chain substituents simultaneously with the addition of a crosslinking agent and an initiator, thereby providing excellent elasticity and selective adsorption and absorption of oil. The present invention relates to an absorbent elastic graft polymer having a greatly improved network structure and a method of manufacturing the same.
Description
본 발명은 망상구조를 가진 유흡수용 탄성 그라프트중합체와 이의 제조방법에 관한 것으로서, 더욱 상세하게는 불포화 결합의 함량(8%∼12%)이 적고, 내광성(△E=5∼14)이 우수한 특정 고무와, 탄소수 3 내지 18의 직쇄 또는 측쇄 치환기를 가진 지방족 또는 방향족 비닐 단량체를 가교제 및 개시제 첨가하에 그라프트 중합과 동시에 가교반응시켜 제조됨으로써, 탄성이 우수함은 물론 기름에 대한 선택적 흡착 및 흡수성이 크게 향상된 망상구조를 가진 유흡수용 탄성 그라프트중합체와이의 제조방법에 관한 것이다.The present invention relates to an oil-absorbing elastic graft polymer having a network structure and a method for producing the same, more specifically, a content of unsaturated bonds (8% to 12%) is low, and light resistance (ΔE = 5 to 14) is low. It is prepared by crosslinking and reacting certain excellent rubbers with aliphatic or aromatic vinyl monomers having 3 to 18 carbon straight or branched chain substituents simultaneously with the addition of a crosslinking agent and an initiator, thereby providing excellent elasticity and selective adsorption and absorption of oil. The present invention relates to an elastic graft polymer for absorbing water having a greatly improved network structure.
근래에는 산업의 발전에 의해서 육상이나 해상으로 수송되고 있는 기름 수송량이나 수송 횟수가 급격히 증가하고 있고, 또한 환경에 대한 관심이 커져 감에 따라 육상이나 해상에서의 기름 오염에 대한 관심 또한 커져가고 있다. 해수는 폐수 또는 폐기물 등의 유입에 의해 오염될 수도 있지만, 원유의 수송과정 중에 선적의 파손 등으로 인해 유출되는 다량의 기름에 의해서도 심각하게 오염된다. 그리고 육상에서는 기름 유출에 의한 하천수 및 토양 등이 크게 오염되고 있다. 따라서 육상에서나 해상에 유출된 기름을 효과적으로 제거하는 방법이 절실히 요구되어 왔다.In recent years, with the development of the industry, the amount of oil transportation and the number of transportations that are being transported to the land and the sea are rapidly increasing, and as the interest in the environment increases, the interest in the oil pollution on the land and the sea is also increasing. Although seawater may be contaminated by inflow of wastewater or waste, it is also seriously contaminated by a large amount of oil that flows out due to breakage of shipment during the transportation of crude oil. And on land, river water and soil are greatly polluted by oil spills. Therefore, there is an urgent need for a method for effectively removing oil spilled on land or at sea.
해상에 유출된 기름을 효과적으로 제거하는 방법으로서 저분자 유화제, 또는 기름에 대한 흡착·흡수성이 우수한 중합체 또는 이들 중합체를 발포시킨 발포 중합체를 이용하여 제거하는 방법이 널리 알려져 있다. 현재 일반적으로 사용되고 있는 유흡수용 중합체는 단량체로 알킬(메타)아크릴레이트, 알킬아릴(메타)아크릴레이트, 알킬(메타)아크릴아마이드, 알킬아릴(메타)아크릴아마이드, 지방족 비닐에스터, 알킬스티렌, 알파올레핀, 스티렌과 부타디엔, 폴리우레탄 등을 중합하여 제조된 것이다. 그러나 이러한 기존의 중합체는 유흡수율이 낮고 깨지기 쉽기 때문에 오일펜스 제작에 직접 사용할 수 없는 문제점이 지적되었다.As a method for effectively removing oil spilled on the sea, a method of removing the oil using a low molecular emulsifier, a polymer excellent in adsorption and absorption to oil, or a foamed polymer in which these polymers are foamed is widely known. Currently absorbing polymers generally used are alkyl (meth) acrylates, alkylaryl (meth) acrylates, alkyl (meth) acrylamides, alkylaryl (meth) acrylamides, aliphatic vinyl esters, alkylstyrenes, and alpha as monomers. It is produced by polymerizing olefin, styrene and butadiene, polyurethane, and the like. However, it is pointed out that these conventional polymers have low oil absorption and are fragile and thus cannot be used directly in oil fence fabrication.
따라서 약간의 탄성을 가지면서 기름에 대한 흡착·흡수성이 우수한 유흡수 제품 제조를 위한 새로운 재료의 개발이 절실히 요구된다.Therefore, there is an urgent need for the development of new materials for the production of oil-absorbing products having a slight elasticity and excellent absorption and absorption of oil.
본 발명은 종래의 유흡수용 중합체가 갖는 낮은 유흡수성과 탄성이 적어 깨지기 쉬운 문제점을 한꺼번에 해결하기 위하여 다년간 노력하였고, 그 결과 통상의 고무 단량체보다 불포화 결합의 함량(8%∼12%)이 적고, 내광성(△E=5∼14)이 우수한 특정 고무를 기제로 선택 사용하고, 이를 직쇄 또는 측쇄 치환기 사슬을 가진 비닐 단량체와 그라프트 중합과 동시에 가교반응시켜 기름이 잘 흡수 및 흡착될 수 있도록 고분자 자체가 적당한 망상구조를 가지는 탄성 그라프트중합체를 얻음으로써 본 발명을 완성하게 되었다.The present invention has been made for many years to solve the problems of the low water-absorbent and elasticity of the conventional water-absorbing polymer at the same time easy to break, and as a result less unsaturated bond content (8% to 12%) than the conventional rubber monomer Select and use a specific rubber with excellent light resistance (△ E = 5-14) as a base, and polymerize it so that oil can be absorbed and adsorbed by crosslinking the vinyl monomer having a straight or branched chain with the graft polymerization. The present invention has been completed by obtaining an elastic graft polymer having an appropriate network structure.
따라서, 본 발명은 오일펜스 또는 흡착포 등의 유흡수성 제품 제작에 유용한 망상구조를 가진 탄성 그라프트중합체와 이의 제조방법을 제공하는데 그 목적이 있다.Accordingly, an object of the present invention is to provide an elastic graft polymer having a network structure and a method for producing the same, which are useful for producing an oil-absorbent product such as an oil fence or an absorbent cloth.
도 1은 그라프트중합방법으로 제조된 가교 되지 않은 중합체(a)와 본 발명의 망상 구조를 가진 탄성 그라프트중합체(b) 각각에 대한 전자주사현미경 사진(×1000)이다.1 is an electron scanning micrograph (× 1000) of each of an uncrosslinked polymer (a) prepared by the graft polymerization method and an elastic graft polymer (b) having a network structure of the present invention.
본 발명은 불포화 결합의 함량(8%∼12%)이 적고, 내광성(△E=5∼14)이 우수한 고무 10 ∼ 50 중량%와, 탄소수 3 내지 18의 직쇄 또는 측쇄 치환기를 가진 지방족 또는 방향족 비닐 단량체 37 ∼ 83 중량%와, 가교제 2.5 ∼ 20 중량%, 및 개시제 1 ∼ 10 중량%를 그라프트 가교 중합하여 제조한 망상구조를 가진 유흡수용 탄성 그라프트중합체를 그 특징으로 한다.The present invention is aliphatic or aromatic having 10 to 50% by weight of rubber having a low content of unsaturated bonds (8% to 12%) and excellent light resistance (ΔE = 5 to 14) and a straight or branched chain substituent having 3 to 18 carbon atoms. It is characterized by an elastic graft polymer for absorption of water having a network structure prepared by graft crosslinking polymerization of 37 to 83% by weight of vinyl monomer, 2.5 to 20% by weight of crosslinking agent, and 1 to 10% by weight of initiator.
또한, 본 발명은 상기한 고무 및 비닐 단량체에, 가교제와 개시제를 혼합하고, 질소 또는 아르곤가스를 투입한 다음, 50 ∼ 120 ℃에서, 6 ∼ 120 시간 동안그라프트 중합과 동시에 가교반응시켜 망상구조를 가진 유흡수용 탄성 그라프트중합체를 제조하는 방법을 또다른 특징으로 한다.In the present invention, a crosslinking agent and an initiator are mixed with the above-described rubber and vinyl monomers, nitrogen or argon gas is added, and then the crosslinking reaction is carried out simultaneously with the graft polymerization at 50 to 120 ° C. for 6 to 120 hours to form a network structure. It is another feature of the method for producing an elastic graft polymer for absorption.
또한, 본 발명은 상기한 망상구조를 가진 유흡수성 탄성 그라프트중합체를 용매에 녹여 각종 부직포류 또는 스폰지류에 코팅 처리한 유흡수성 제품을 또다른 특징으로 한다.In another aspect, the present invention is characterized in that the absorbent elastic graft polymer having a network structure is dissolved in a solvent and coated with various nonwoven fabrics or sponges.
이와 같은 본 발명을 더욱 상세하게 설명하면 다음과 같다.The present invention will be described in more detail as follows.
본 발명의 망상구조를 가진 유흡수용 탄성 그라프트중합체는 폴리부타디엔, 폴리(스틸렌-코-부타디엔), 폴리(에틸렌-코-프로필렌)과 같이 불포화 결합의 함량이 적고 내광성이 우수한 고무와, 탄소수 3 내지 18의 직쇄 또는 측쇄 치환기를 가지고 있는 지방족 또는 방향족 비닐 단량체를 가교제와 개시제 첨가하에 그라프트 중합과 동시에 가교반응시켜 제조된 것이다.The absorbent elastic graft polymer having the network structure of the present invention has a low content of unsaturated bonds such as polybutadiene, poly (styrene-co-butadiene), poly (ethylene-co-propylene), and excellent rubber resistance and carbon number. An aliphatic or aromatic vinyl monomer having 3 to 18 straight or branched chain substituents is prepared by crosslinking at the same time as the graft polymerization under the addition of a crosslinking agent and an initiator.
본 발명이 특징적으로 사용하고 있는 고무는 불포화 결합의 함량이 적고, 내광성이 우수한 것으로서 유흡수용 망상구조를 가진 중합체에 포함될 경우 필름을 형성할 수 있는 성질을 부여함으로써 오일펜스나 흡착포에서 필수적인 유연성을 부여하는 장점이 있다. 다시말하면, 통상의 고무는 불포화 결합의 함량이 30% 이상인 바, 불포화 결합의 함량이 높은 고무에 다량의 비닐 단량체를 그라프트시켜 제조한 중합체의 경우 유흡수성은 향상될 수 있으나 탄성이 저조하여 깨지기 쉬워 오일펜스 등의 유흡수 제품 가공에 직접 사용할 수 없고, 불포화 결합의 함량이 높은 고무에 소량의 비닐 단량체를 그라프트시켜 제조한 중합체의 경우는 탄성은 있으나 유흡수성이 낮게 된다. 따라서, 본 발명에서는 불포화 결합의 함량이 통상의 고무와 비교하여 적고(8%∼12%) 또, 페이드-오-메터(Fade-o-meter; ATLAS, MINOLTA) 또는 웨더-오-메터(Weather-o-meter; ATLAS, CDMC-A)로 측정한 변색값(△E)이 5 ∼ 14로 내광성이 우수한 고무를 선택 사용한 것이다. 본 발명이 사용하게 되는 고무는 폴리부타디엔, 폴리(스틸렌-코-부타디엔) 및 폴리(에틸렌-코-프로필렌) 중에서 선택된 것이며, 상기 폴리(에틸렌-코-프로필렌)에 이중결합을 부여하기 위하여 노르보렌, 디사이크로펜타디엔, 1,4-헥사디엔 등과 같은 디엔 단량체가 결합된 형태의 고무 사용도 가능하다. 이상에서 설명한 고무는 전체 탄성 그라프트중합체에 대해 10 ∼ 50 중량% 범위로 사용하도록 하는 바, 상기 사용량 미만으로 고무를 사용하게 되면 생성된 중합체가 유연성이 결여되어 깨지기 쉬운 문제점이 있고, 상기 범위를 초과하여 과량 사용하게 되면 유흡수성이 떨어지고 가공하지 않은 탄성고무와 같은 성질로 인하여 오일펜스와 같은 유흡수 제품으로 가공하는데 문제점이 있다.The rubber used in the present invention has a low content of unsaturated bonds and excellent light resistance, and it provides the necessary flexibility in oil fence or adsorption cloth by imparting the property to form a film when it is included in a polymer having an oil absorption network structure. There is an advantage to grant. In other words, the conventional rubber has an unsaturated bond content of 30% or more, so that a polymer prepared by grafting a large amount of vinyl monomer onto a rubber having a high unsaturated bond content may have improved water absorption, but is poorly broken due to poor elasticity. Polymers prepared by grafting a small amount of vinyl monomers onto rubber having a high content of unsaturated bonds cannot be directly used for processing oil-absorbing products such as oil fences, but are elastic but have low oil-absorbing properties. Therefore, in the present invention, the content of unsaturated bonds is smaller than that of conventional rubber (8% to 12%), and also fade-o-meter (ATLAS, MINOLTA) or weather-o-meter (Weather) -O-meter: The rubber | dye which was excellent in light resistance was selected and used for the discoloration value ((E)) measured by ATLAS and CDMC-A) 5-14. The rubber used in the present invention is selected from polybutadiene, poly (styrene-co-butadiene) and poly (ethylene-co-propylene), and norborene for imparting a double bond to the poly (ethylene-co-propylene). It is also possible to use a rubber in the form of a diene monomer bonded, such as dicyclopentadiene, 1,4-hexadiene. The rubber described above is to be used in the range of 10 to 50% by weight with respect to the total elastic graft polymer, when the rubber is used in less than the amount used, there is a problem that the resulting polymer lacks flexibility and is fragile. Excessive use in excess of the absorbency is poor, due to the properties such as raw rubber, there is a problem in processing into an absorbent product such as oil fence.
또한, 본 발명이 특징적으로 사용하고 있는 또 다른 단량체로서 지방족 또는 방향족 비닐 단량체는 탄소수 3 내지 18의 직쇄 또는 측쇄 치환기를 가지고 있는 것으로, 상기한 고무에 그라프트 중합하여 열가소성 고분자와 같은 특성을 부여하며 이로써 오일펜스나 부직포 및 스폰지류 등의 유흡수 제품으로 가공할 수 있는 약간의 탄성을 갖도록 한다. 상기한 바와 같은 유흡제로서의 특성은 비닐 단량체의 기름에 대한 친화성에 기인한 것이다. 본 발명이 사용하는 비닐 단량체로서 지방족 비닐 단량체로는 아크릴레이트 및 메타아크릴레이트 유도체, 아크릴아마이드 및 메타아크릴아마이드 유도체 등 중에서 선택 사용하고, 방향족 비닐 단량체로는 스티렌 및 스티렌 유도체 중에서 선택 사용한다. 특히, 본 발명에서는 유흡수성이 좋고 최종 그라프트 중합체가 약간의 탄성을 가지도록 하기 위하여, 탄소수 3 내지 18의 직쇄 또는 측쇄 치환기를 가지는 비닐 단량체를 사용하는 것이 바람직하다. 이상에서 설명한 비닐 단량체는 전체 탄성 그라프트중합체에 대해 37 ∼ 83 중량% 범위로 사용하도록 하는 바, 그 사용량이 상기 범위 미만이면 가공하지 않은 고무성질과 같아서 오일펜스나 흡착포로 가공하는데 문제점과 유흡수성이 떨어지는 문제점이 있고, 상기 범위를 초과하여 과량 사용하게 되면 깨지기 쉽기 때문에 오일펜스로 가공하는데 문제점이 있다.In addition, aliphatic or aromatic vinyl monomers, which are characteristically used in the present invention, have a straight or branched chain substituent having 3 to 18 carbon atoms, and are grafted onto the rubber to impart properties such as thermoplastic polymers. This provides a slight elasticity that can be processed into oil-absorbing products such as oil fences, nonwoven fabrics, and sponges. The properties as a sorbent as described above are due to the affinity for the vinyl monomer to the oil. As the vinyl monomer used in the present invention, the aliphatic vinyl monomer is selected from acrylate and methacrylate derivatives, acrylamide and methacrylamide derivatives, and the like, and the aromatic vinyl monomer is selected from styrene and styrene derivatives. In particular, in the present invention, it is preferable to use a vinyl monomer having a straight or branched chain substituent having 3 to 18 carbon atoms in order to have good water absorption and a final elasticity of the graft polymer. The vinyl monomer described above should be used in the range of 37 to 83% by weight based on the total elastic graft polymer. If the amount of the vinyl monomer is less than the above range, it is the same as the unprocessed rubber property. There is a problem of falling, there is a problem in processing into an oil fence because it is fragile when used in excess of the above range.
본 발명이 이상에서 설명한 고무와 비닐 단량체의 그라프트 가교 중합을 위하여 사용할 수 있는 가교제는 다이비닐벤젠, 테트라에틸렌글리콜 다이메타아크릴레이트, 트리에틸렌글리콜 다이메타아크릴레이트 및 에틸렌글리콜 다이메타아크릴레이트 중에서 선택한 하나 또는 2 이상이다. 가교제는 전체 탄성 그라프트중합체에 대해 2.5 ∼ 20 중량% 범위로 사용하도록 하는 바, 그 사용량이 상기 범위를 초과하여 과량이면 깨지기 쉽고 또한 유흡수성이 낮은 문제점이 있으며, 상기 범위 미만이면 가교가 너무 적게 일어나 기름에 녹을수 있고 유흡수율이 감소하며 가공이 어려운 문제점이 있다.The crosslinking agent that can be used for graft crosslinking polymerization of the rubber and vinyl monomers described above by the present invention is selected from divinylbenzene, tetraethylene glycol dimethacrylate, triethylene glycol dimethacrylate and ethylene glycol dimethacrylate. One or two or more. The crosslinking agent may be used in the range of 2.5 to 20% by weight based on the total elastic graft polymer. If the amount of the crosslinking agent is in excess of the above range, the crosslinking agent is easily broken and has low water absorption. There is a problem that can be dissolved in oil, oil absorption rate is reduced and processing is difficult.
본 발명이 사용하게 되는 중합 개시제는 벤조일퍼옥사이드, 아조비스이소부티로니트릴, 라우릴퍼옥사이드, 아세틸퍼옥사이드, 부틸퍼옥사이드, 큐밀퍼옥사이드, 부틸퍼아세테이트, 부틸하이드로퍼옥사이드 중에서 선택한 하나 또는 2 이상이며, 전체 탄성 그라프트중합체에 대해 1 ∼ 10 중량% 범위로 사용하도록 한다.The polymerization initiator to be used in the present invention is one selected from benzoyl peroxide, azobisisobutyronitrile, lauryl peroxide, acetyl peroxide, butyl peroxide, cumyl peroxide, butyl peracetate, butyl hydroperoxide The above is used in the range of 1 to 10% by weight based on the total elastic graft polymer.
한편, 본 발명은 이상에서 설명한 고무 및 비닐 단량체에, 가교제와 개시제를 혼합하고, 질소 또는 아르곤가스를 투입한 다음, 50 ∼ 120 ℃에서, 6 ∼ 120 시간 동안 그라프트 중합과 동시에 가교반응시켜 망상구조를 가진 유흡수용 탄성 그라프트중합체를 제조하는 방법을 포함한다. 다시말하면, 본 발명에 따른 제조방법에 의해 상기한 조건으로 그라프트 중합 및 가교반응을 동시에 수행하여 망상구조와 탄성이 있는 유흡수성 고분자를 합성할 수 있다.In the present invention, the crosslinking agent and the initiator are mixed with the rubber and vinyl monomers described above, nitrogen or argon gas is added, and the crosslinking reaction is carried out simultaneously with the graft polymerization at 50 to 120 ° C. for 6 to 120 hours to form a network. It includes a method for producing an absorbent elastic graft polymer having a structure. In other words, the graft polymerization and the crosslinking reaction may be simultaneously performed under the above-described conditions by the production method according to the present invention to synthesize a network and elastic absorbent polymer having elasticity.
본 발명에 따른 중합 과정은 질소 또는 아르곤가스 분위기에서 진행되는 것이 바람직한 바, 질소 또는 아르곤가스를 상기 중합조에 기포가 1초에 1방울씩 발생하도록 조절하면서 중합과정 동안 계속 투입시킨다. 탄성 그라프트중합체를 얻기위한 중합은 50 ∼ 120 ℃에서 진행하는 것이 바람직한 바, 중합 온도가 상기 범위 미만이면 그라프트된 중합체의 수율이 적은 문제점이 발생하고, 상기 온도 범위를 초과하면 단일 중합체가 많이 생기는 문제점이 발생한다. 또한, 상기 중합은 6 ∼ 120 시간 동안 수행하는 것이 바람직한데, 중합시간이 상기 범위 미만이면 중합이 완전히 진행되지 않아 본 발명이 목적하는 합체의 수율이 감소하는 문제점이 발생하고, 상기 범위를 초과하면 가교가 너무 많이 일어나서 생성된 중합체는 탄성이 없고 깨지기 쉬운 문제점이 발생한다. 중합 반응이 끝난 후 얻어진 중합체는 비용매에 침전시킨 다음 여과하여 항량(恒量)이 될 때까지 건조시킨다. 이때, 비용매로는 메탄올, 에탄올, 아세톤 중에서 선택한 하나 또는 2 이상을 사용할 수 있다.In the polymerization process according to the present invention, it is preferable to proceed in a nitrogen or argon gas atmosphere. The nitrogen or argon gas is continuously added to the polymerization tank during the polymerization process while controlling bubbles to be generated one drop per second. It is preferable that the polymerization to obtain the elastic graft polymer proceeds at 50 to 120 ° C. If the polymerization temperature is less than the above range, the yield of the grafted polymer is low. The problem arises. In addition, the polymerization is preferably carried out for 6 to 120 hours, if the polymerization time is less than the above range, the polymerization does not proceed completely, causing a problem that the yield of the coalescence of the present invention is reduced, if the above range Too much crosslinking results in polymers that are inelastic and brittle. After the completion of the polymerization reaction, the obtained polymer is precipitated in a non-solvent and then filtered and dried until it reaches a constant weight. In this case, one or two or more selected from methanol, ethanol and acetone may be used as the non-solvent.
첨부도면 도 1은 상기한 과정으로 제조된 가교되지 않은(망상 구조가 형성되지 않은) 중합체(a)와 상기한 과정에 의해 제조된 본 발명의 망상구조를 가진 유흡수용 탄성 그라프트중합체(b)에 대한 전자주사현미경 사진(×1000)이다. 도 1에 의하면, 본 발명에 따른 망상구조를 가진 유흡수용 탄성 그라프트중합체(b)는 적당한 크기의 미세구멍을 가지고 있기 때문에 그 속으로 기름이 들어갈 수 있고 들어간 기름에 의해서 구멍의 표면이 팽윤되어 흡수된 기름은 밖으로 나오지 못하게 되기 때문에 다양한 유흡수 제품 제조를 위한 재료로서 유용하게 사용될 수 있다.1 is a non-crosslinked (no network structure) polymer (a) prepared by the above-described process and the absorbent elastic graft polymer (b) having the network structure of the present invention prepared by the above process (b) Electron scanning micrograph (x1000). According to Fig. 1, the oil-absorbing elastic graft polymer (b) having a network structure according to the present invention has fine pores of a suitable size, so that oil can enter therein and the surface of the pores is swelled by the oil. Since the absorbed oil does not come out, it can be usefully used as a material for manufacturing various absorbent products.
따라서, 본 발명은 상기에서 얻어진 유흡수용 졸(sol)형 탄성중합체를 별도로 다공성 구조를 가지는 부직포류 또는 스폰지류에 코팅 처리하여 제조된 유흡수 제품을 포함한다. 즉, 본 발명에 따른 제조방법에 의해 얻어진 유흡수용 졸(sol)형 탄성중합체를 용매에 녹여 스프레이 혹은 침적하는 방법으로 부직포류 또는 스폰지류 등에 코팅한다. 이때, 용매로는 에틸아세테이트, 톨루엔, 다이옥산, 노말핵산, 테트라하이드로푸란 중에서 선택한 하나 또는 2 이상을 사용한다. 이와 같은 방법으로 제조한 유흡수 제품은 다공성 구조를 가짐으로써, 기름과 유흡수제용 졸(sol)형 탄성중합체의 접촉 면적을 증가시켜 탄성중합체의 유흡착, 유흡수를 도울 뿐만 아니라, 부직포 또는 스폰지 자체에도 기름이 흡착·흡수되기 때문에 만들어진 유흡수 제품이 기름을 제거하는데 더욱 효과적이다. 또한, 본 발명에 의한 부직포 또는 스폰지에 졸(sol)형 탄성체가 코팅된 유흡수 제품은 망상 탄성 중합체의 함량이 적은데도 비교적 높은 유흡수율을 나타내기 때문에 기존 제품에 비해 이동이나, 실제 사용시 편리한 장점이 있으며, 또한 가격이 저렴하다는 면에서 경쟁력을 가질 수 있다.Accordingly, the present invention includes a water-absorbent product prepared by coating a non-woven fabric or sponge having a porous structure separately from the oil-absorbing sol-type elastomer obtained above. That is, the non-woven fabric or the sponge is coated on the water-absorbing sol-type elastomer obtained by the manufacturing method according to the present invention by dissolving in a solvent and spraying or depositing. In this case, one or two or more selected from ethyl acetate, toluene, dioxane, normal nucleic acid, and tetrahydrofuran are used as the solvent. The absorbent product manufactured in this way has a porous structure, thereby increasing the contact area between the oil and the sol-type elastomer for the absorbent, thereby helping to absorb and absorb the elastomer, as well as the nonwoven fabric or sponge. Since oil is also adsorbed and absorbed by itself, the absorbent product made is more effective in removing oil. In addition, a non-woven fabric or a sponge-based absorbent product coated with a sol-type elastomer exhibits a relatively high water absorption rate even when the content of the reticulum polymer is low, so that it is convenient to move or use in actual use. This can also be competitive in terms of low price.
이와 같은 본 발명을 다음의 실시예에 의거하여 더욱 상세히 설명하는 바, 본 발명이 실시예에 의해 한정되는 것은 아니다.The present invention will be described in more detail based on the following examples, but the present invention is not limited by the examples.
실시예 1 ∼ 5Examples 1-5
중합조에 폴리(에틸렌-코-프로필렌-코-5-메틸렌-2-노르보렌)(이하, "EPDM"이라 약칭함), 3차 부틸스티렌(이하, "tBS"라 약칭함)과 가교제인 다이비닐벤젠(이하, "DVB"라 약칭함)을 넣고 개시제로서 벤조일퍼옥사이드(이하, "BPO"라 약칭함)를 첨가하였다. 이때, 각각의 함량은 다음 표 1에 제시하였다. 기밀장치를 한 중합조에 질소가스를 1초에 1개의 기포가 중합용액에서 나오도록 조절하면서 반응시켜 tBS-g-EPDM-g-DVB(이하, "PBED"라 약칭함) 탄성중합체를 얻었다.Poly (ethylene-co-propylene-co-5-methylene-2-norborene) (hereinafter abbreviated as "EPDM"), tertiary butylstyrene (hereinafter abbreviated as "tBS") and a crosslinking agent in a polymerization tank Vinylbenzene (hereinafter abbreviated as "DVB") was added and benzoyl peroxide (hereinafter abbreviated as "BPO") was added as an initiator. At this time, each content is shown in Table 1 below. Nitrogen gas was reacted in a polymerization tank equipped with an airtight device while controlling one bubble per second to emerge from the polymerization solution to obtain a tBS-g-EPDM-g-DVB (hereinafter, abbreviated as "PBED") elastomer.
이렇게 중합된 PBED 탄성중합체는 중합하는 동안에 가교되는 gel-PBED 탄성중합체와 중합 후 추출 과정에서 용매에 녹아 나오는 sol-PBED 탄성중합체로 분리하였다. 가교된 gel-PBED 탄성중합체는 비용매인 메탄올에 침전시킨 후, 여과하여 항량이 될 때까지 건조시킴으로써 유흡수제용 탄성중합체로 제조하였다. 톨루엔이나 THF로 추출한 용매에 녹을 수 있는 sol-PBED 탄성중합체는 UV광에 의해서 다시 가교시킴으로써, 유흡수제용 탄성중합체를 제조하였다. 또한, 상기 sol-PBED 탄성중합체를 다시 톨루엔이나 THF 용매에 녹여 스프레이나 침적 방법으로 부직포(코오롱, P512-RB-115 )에 코팅함으로써, sol-PBED 코팅 부직포를 제조하였다.The polymerized PBED elastomer was separated into a gel-PBED elastomer crosslinked during polymerization and a sol-PBED elastomer dissolved in a solvent during the extraction process after polymerization. The cross-linked gel-PBED elastomer was prepared as an absorbent elastomer by being precipitated in non-solvent methanol, followed by filtration and drying until a constant weight. The sol-PBED elastomer which can be dissolved in a solvent extracted with toluene or THF is crosslinked again by UV light, thereby preparing an absorbent elastomer. In addition, the sol-PBED elastomer was dissolved in toluene or THF solvent and coated on a nonwoven fabric (Kolon, P512-RB-115) by spraying or dipping to prepare a sol-PBED coated nonwoven fabric.
실시예 6 ∼ 9Examples 6-9
먼저 2-하이드록시에틸메틸아크릴레이트와 시나모일 클로라이드, 트리에틸아민을 혼합하여 0 ℃에서 4 시간 동안 환류, 여과, 증류 등의 과정을 거치는 방법으로 시나모일옥시메틸메타아크릴레이트(이하, "CEMA"라 약칭함)를 합성하였다.First, 2-hydroxyethylmethylacrylate, cinnamoyl chloride, and triethylamine are mixed and refluxed, filtered, and distilled at 0 ° C. for 4 hours. Cinnamoyloxymethyl methacrylate (hereinafter, “CEMA "Abbreviated").
중합조에 EPDM와 tBS, 상기에서 제조된 CEMA를 넣고 개시제로써 BPO를 첨가하였다. 이때, 각각의 함량은 다음 표 2에 제시하였다. 그 다음에 기밀장치를 한 중합조에 질소가스를 1초에 1개의 기포가 중합용액에서 나오도록 조절하면서 70℃에서 48시간 동안 반응시킴으로써, tBS-g-EPDM-g-CEMA(이하, "PBEC"라 약칭함) 탄성중합체를 제조하였다.EPDM and tBS, CEMA prepared above was added to the polymerization tank, and BPO was added as an initiator. At this time, each content is shown in Table 2 below. Then, nitrogen gas was reacted in the airtight polymerization tank for 1 hour at 70 DEG C while controlling one bubble out of the polymerization solution for twenty-eight hours to obtain tBS-g-EPDM-g-CEMA (hereinafter referred to as "PBEC"). Abbreviated D) to prepare an elastomer.
위와 같이 얻어진 PBEC 탄성중합체를 비용매인 메탄올에 침전시킨 후, 여과하였다. 그 다음에 톨루엔이나 THF용매를 이용하여 추출하고, 항량(恒量)이 될 때까지 건조시킴으로써, 유흡수제용 PBEC 탄성중합체를 제조하였다.The PBEC elastomer obtained as described above was precipitated in methanol as a non-solvent, and then filtered. Then, PBEC elastomer for water absorbent was prepared by extracting with toluene or THF solvent and drying until it became a constant amount.
실시예 1 ∼ 5와 동일한 방법을 사용하여, PBEC 탄성중합체를 부직포에 코팅함으로써, PBEC이 코팅된 부직포 혹은 스폰지를 얻었다.The PBEC elastomer was coated on the nonwoven fabric using the same method as Examples 1 to 5 to obtain a nonwoven fabric or sponge coated with PBEC.
실험예 1Experimental Example 1
상기 실시예 1 ∼ 9을 통해 얻어진 유흡수제용 탄성중합체와 이들 탄성중합체로 코팅 처리한 부직포의 유흡수율을 ASTM F726-81 방법에 따라 측정하였다.The water absorption rate of the absorbent elastomers obtained in Examples 1 to 9 and the nonwoven fabric coated with these elastomers was measured according to the ASTM F726-81 method.
원유에 톨루엔을 넣어 원유의 함량이 10 중량%가 되도록 희석하여 희석 원유를 만들었다. 이 희석 원유에 무게를 측정한 실시예 1 ∼ 9의 유흡수제용 탄성중합체 또는 이들 탄성중합체로 코팅 처리한 부직포를 넣어 희석 원유를 흡수하게 한 다음, 팽윤된 탄성중합체 또는 탄성중합체로 코팅된 부직포의 무게를 측정하였다. 다음 수학식 1에 의하여 유흡수율을 계산하여 실시예 1 ∼ 5(PBED)와 실시예 6 ∼ 9(PBEC)의 희석 원유에 대한 기름흡수성 결과를 각각 다음 표 1 과 표 2에 제시하였다. 최대기름흡수시간은 유흡수율이 최대가 되는데 필요한 시간을 말한다.Toluene was added to the crude oil to dilute the crude oil to 10% by weight to make diluted crude oil. The diluted crude oil was weighed with the absorbent elastomer of Examples 1 to 9 or the nonwoven fabric coated with these elastomers to absorb the diluted crude oil, and then the swelled elastomer or the nonwoven fabric coated with the elastomer. The weight was measured. The oil absorption rate was calculated by Equation 1 below, and the oil absorption results of the crude oils of Examples 1 to 5 (PBED) and Examples 6 to 9 (PBEC) were shown in Tables 1 and 2, respectively. The maximum oil absorption time is the time required for the maximum oil absorption rate.
상기 표 1 ∼ 2의 결과에 의하면, 본 발명에 따라 불포화 결합의 함량(8%∼12%)이 적고, 내광성(△E=5∼14)이 우수한 고무와, 탄소수 3 내지 18의 직쇄 또는 측쇄 치환기를 가진 지방족 또는 방향족 비닐 단량체를 사용하여 제조한 실시예 1 ∼ 9의 탄성 그라프트중합체는 유흡수성이 우수하였고 부직포에 코팅하여도 깨지지 않는 성질을 가지고 있었다.According to the results of Tables 1 to 2, the rubber having a low content of unsaturated bonds (8% to 12%) and excellent light resistance (ΔE = 5 to 14) according to the present invention, and a straight or branched chain having 3 to 18 carbon atoms The elastic graft polymers of Examples 1 to 9 prepared using aliphatic or aromatic vinyl monomers having substituents were excellent in absorbency and had properties that were not broken even when coated on a nonwoven fabric.
다음 표 3은 유흡수용 중합체로서 시판되고 있는 α-Gel 제품(일본 α회사, 스티렌-부타디엔-스티렌 블록 공중합체)에 대한 유흡수성을 나타낸 것으로 본 발명에서 제조한 유흡수성보다 적음을 알 수 있다. (단 특성, 물성이 공개되어 있지 않기 때문에 상세한 비교는 할 수 없었음)The following Table 3 shows the water absorption of α-Gel products (Japan α company, styrene-butadiene-styrene block copolymer) that are commercially available as a polymer for absorption. . (However, detailed comparison could not be made because the characteristics and physical properties were not disclosed.)
상기 표 3의 결과에 의하면, 희석 원유를 흡수하는 능력에 있어서 본 발명의 PBED 또는 PBEC 탄성중합체들은 종래의 유흡수용으로 많이 사용되는 일반적인 스티렌-부타디엔-스티렌 흡착제보다 최대 흡유량은 훨씬 우수한 결과를 나타내고 있다. 또한 이들 중합체를 코팅한 부직포의 기름 흡수도 부직포 자체보다도 훨씬 우수한 결과를 나타내고 있다.According to the results of Table 3, in the ability to absorb the diluted crude oil, the PBED or PBEC elastomers of the present invention exhibited much better maximum oil absorption than conventional styrene-butadiene-styrene adsorbents that are widely used for conventional oil absorption. have. Moreover, the oil absorption of the nonwoven fabric coated with these polymers also shows much better results than the nonwoven fabric itself.
지상이나 해양에 유출된 다량의 기름을 흡수 제거하기 위해서는 작은 량의 흡수제를 사용하여 많은 양의 기름을 흡수제거 하는 것이 무엇보다도 경쟁력이 있기 때문에 본 발명에서 발명된 유흡수용 망상 탄성 중합체는 유흡수성이 아주 뛰어나다는 것을 특징으로 하고 있다.In order to absorb and remove a large amount of oil spilled on the ground or the ocean, it is more competitive to absorb and remove a large amount of oil using a small amount of absorbent. It is characterized by very excellent.
실험예 2Experimental Example 2
상기 실시예 1 ∼ 5 및 6 ∼ 9에서 중합한 유흡수용 탄성중합체의 구조는 푸리에 변환 적외선 분광기(FT-IR, Perkin 제조사, Perkin-Elmer 1330 모델명)를 이용하여 확인하였다.The structures of the water-absorbing elastomer polymerized in Examples 1 to 5 and 6 to 9 were confirmed using a Fourier transform infrared spectrometer (FT-IR, Perkin, Perkin-Elmer 1330 model name).
tBS-g-EPDM-g-DVB(PBED) 탄성중합체 :tBS-g-EPDM-g-DVB (PBED) Elastomer:
IR(KBr) υMAX: 3010, 2900, 1465, 1380, 900∼790 cm-1 IR (KBr) υ MAX : 3010, 2900, 1465, 1380, 900 to 790 cm -1
tBS-g-EPDM-g-CEMA(PBEC) 탄성중합체 :tBS-g-EPDM-g-CEMA (PBEC) elastomer:
IR (KBr) υMAX: 3010, 2900, 1730, 1620, 1465, 1380, 900∼790 cm-1 IR (KBr) υ MAX : 3010, 2900, 1730, 1620, 1465, 1380, 900 to 790 cm -1
상술한 바와 같이, 본 발명에 따라 제조한 망상구조를 가진 유흡수용 탄성 그라프트중합체는 종래의 유흡수용 중합체에 비해 유흡착 및 유흡수율이 높아 매우 유용하고, 이러한 본 발명의 탄성 그라프트중합체를 이용한 유흡수 제품은 부직포 그 자체에 비해 유흡수율이 향상되는 효과가 있었다.As described above, the oil-absorbing elastic graft polymer having a network structure prepared according to the present invention has a high oil adsorption and a water absorption rate higher than that of the conventional oil-absorbing polymer, and is very useful. Absorption product using was effective in improving the absorption rate compared to the nonwoven fabric itself.
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US3520806A (en) * | 1967-05-26 | 1970-07-21 | Dow Chemical Co | Separation of liquid organic materials from substrates |
JPH0441583A (en) * | 1990-06-08 | 1992-02-12 | Nippon Shokubai Co Ltd | Oil absorptive material |
JPH05209017A (en) * | 1991-11-14 | 1993-08-20 | Mitsubishi Petrochem Co Ltd | Production of self-swelling oil-absorbent polymer, agent for recovering oily substance, and base material which absorbs oily substance and sustainedly releases the same |
US5239007A (en) * | 1991-10-22 | 1993-08-24 | Arco Chemical Technology, L.P. | Oil-absorbent compositions |
JPH09302045A (en) * | 1996-05-14 | 1997-11-25 | Japan Synthetic Rubber Co Ltd | Oil absorbent and oil absorbing material containing the same |
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US3520806A (en) * | 1967-05-26 | 1970-07-21 | Dow Chemical Co | Separation of liquid organic materials from substrates |
JPH0441583A (en) * | 1990-06-08 | 1992-02-12 | Nippon Shokubai Co Ltd | Oil absorptive material |
US5239007A (en) * | 1991-10-22 | 1993-08-24 | Arco Chemical Technology, L.P. | Oil-absorbent compositions |
JPH05209017A (en) * | 1991-11-14 | 1993-08-20 | Mitsubishi Petrochem Co Ltd | Production of self-swelling oil-absorbent polymer, agent for recovering oily substance, and base material which absorbs oily substance and sustainedly releases the same |
JPH09302045A (en) * | 1996-05-14 | 1997-11-25 | Japan Synthetic Rubber Co Ltd | Oil absorbent and oil absorbing material containing the same |
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