JPH0441584A - Process for producing oil absorptive material - Google Patents
Process for producing oil absorptive materialInfo
- Publication number
- JPH0441584A JPH0441584A JP2148670A JP14867090A JPH0441584A JP H0441584 A JPH0441584 A JP H0441584A JP 2148670 A JP2148670 A JP 2148670A JP 14867090 A JP14867090 A JP 14867090A JP H0441584 A JPH0441584 A JP H0441584A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- monomer
- meth
- acrylate
- absorbing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000000463 material Substances 0.000 title claims abstract description 28
- 238000000034 method Methods 0.000 title claims description 10
- 239000000178 monomer Substances 0.000 claims abstract description 99
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 39
- 230000002209 hydrophobic effect Effects 0.000 claims abstract description 30
- 239000004745 nonwoven fabric Substances 0.000 claims abstract description 26
- 229920006037 cross link polymer Polymers 0.000 claims abstract description 15
- 239000011358 absorbing material Substances 0.000 claims description 44
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 claims description 32
- 239000000758 substrate Substances 0.000 claims description 17
- 238000004519 manufacturing process Methods 0.000 claims description 12
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims description 8
- 239000004677 Nylon Substances 0.000 claims description 6
- 229920001778 nylon Polymers 0.000 claims description 6
- 125000001931 aliphatic group Chemical group 0.000 claims description 5
- 150000001875 compounds Chemical class 0.000 claims description 5
- 229920000728 polyester Polymers 0.000 claims description 4
- 230000000379 polymerizing effect Effects 0.000 claims description 3
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 229920000098 polyolefin Polymers 0.000 claims description 2
- 229920002635 polyurethane Polymers 0.000 claims description 2
- 239000004814 polyurethane Substances 0.000 claims description 2
- 229920002994 synthetic fiber Polymers 0.000 claims description 2
- 239000012209 synthetic fiber Substances 0.000 claims description 2
- 239000002759 woven fabric Substances 0.000 claims description 2
- 239000004711 α-olefin Substances 0.000 claims description 2
- 125000002877 alkyl aryl group Chemical group 0.000 claims 2
- 125000000217 alkyl group Chemical group 0.000 claims 2
- 238000010521 absorption reaction Methods 0.000 abstract description 15
- KUDUQBURMYMBIJ-UHFFFAOYSA-N 2-prop-2-enoyloxyethyl prop-2-enoate Chemical compound C=CC(=O)OCCOC(=O)C=C KUDUQBURMYMBIJ-UHFFFAOYSA-N 0.000 abstract description 14
- 238000007667 floating Methods 0.000 abstract description 8
- 238000011084 recovery Methods 0.000 abstract description 8
- 238000007598 dipping method Methods 0.000 abstract description 4
- 239000010409 thin film Substances 0.000 abstract description 3
- 238000004132 cross linking Methods 0.000 abstract description 2
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 abstract 2
- 239000003921 oil Substances 0.000 description 91
- 235000019198 oils Nutrition 0.000 description 90
- -1 polyethylene Polymers 0.000 description 26
- 238000006116 polymerization reaction Methods 0.000 description 18
- 239000004743 Polypropylene Substances 0.000 description 17
- 229920001155 polypropylene Polymers 0.000 description 17
- 230000000052 comparative effect Effects 0.000 description 14
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 10
- 230000014759 maintenance of location Effects 0.000 description 10
- 239000002250 absorbent Substances 0.000 description 9
- 230000002745 absorbent Effects 0.000 description 9
- 238000011282 treatment Methods 0.000 description 8
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 7
- 239000000295 fuel oil Substances 0.000 description 5
- PBOSTUDLECTMNL-UHFFFAOYSA-N lauryl acrylate Chemical compound CCCCCCCCCCCCOC(=O)C=C PBOSTUDLECTMNL-UHFFFAOYSA-N 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 239000003505 polymerization initiator Substances 0.000 description 4
- 239000004342 Benzoyl peroxide Substances 0.000 description 3
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 3
- SNRUBQQJIBEYMU-UHFFFAOYSA-N Dodecane Natural products CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 description 3
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 3
- 239000002202 Polyethylene glycol Substances 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 235000019400 benzoyl peroxide Nutrition 0.000 description 3
- 230000005587 bubbling Effects 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 235000019476 oil-water mixture Nutrition 0.000 description 3
- 229920001223 polyethylene glycol Polymers 0.000 description 3
- FQKSRGCBHCFRTN-UHFFFAOYSA-N (4-nonylphenyl) prop-2-enoate Chemical compound CCCCCCCCCC1=CC=C(OC(=O)C=C)C=C1 FQKSRGCBHCFRTN-UHFFFAOYSA-N 0.000 description 2
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 2
- CRSBERNSMYQZNG-UHFFFAOYSA-N 1-dodecene Chemical compound CCCCCCCCCCC=C CRSBERNSMYQZNG-UHFFFAOYSA-N 0.000 description 2
- UZKWTJUDCOPSNM-UHFFFAOYSA-N 1-ethenoxybutane Chemical group CCCCOC=C UZKWTJUDCOPSNM-UHFFFAOYSA-N 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N 1-nonene Chemical compound CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 2
- 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 description 2
- DXIJHCSGLOHNES-UHFFFAOYSA-N 3,3-dimethylbut-1-enylbenzene Chemical compound CC(C)(C)C=CC1=CC=CC=C1 DXIJHCSGLOHNES-UHFFFAOYSA-N 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 125000003438 dodecyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920001451 polypropylene glycol Polymers 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 125000004079 stearyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- RMSGQZDGSZOJMU-UHFFFAOYSA-N 1-butyl-2-phenylbenzene Chemical group CCCCC1=CC=CC=C1C1=CC=CC=C1 RMSGQZDGSZOJMU-UHFFFAOYSA-N 0.000 description 1
- LAYAKLSFVAPMEL-UHFFFAOYSA-N 1-ethenoxydodecane Chemical group CCCCCCCCCCCCOC=C LAYAKLSFVAPMEL-UHFFFAOYSA-N 0.000 description 1
- OMIGHNLMNHATMP-UHFFFAOYSA-N 2-hydroxyethyl prop-2-enoate Chemical compound OCCOC(=O)C=C OMIGHNLMNHATMP-UHFFFAOYSA-N 0.000 description 1
- IMCBLSMMFWHLSN-UHFFFAOYSA-N 2-methyl-n-octylprop-2-enamide Chemical compound CCCCCCCCNC(=O)C(C)=C IMCBLSMMFWHLSN-UHFFFAOYSA-N 0.000 description 1
- FRIBMENBGGCKPD-UHFFFAOYSA-N 3-(2,3-dimethoxyphenyl)prop-2-enal Chemical compound COC1=CC=CC(C=CC=O)=C1OC FRIBMENBGGCKPD-UHFFFAOYSA-N 0.000 description 1
- ATVJXMYDOSMEPO-UHFFFAOYSA-N 3-prop-2-enoxyprop-1-ene Chemical compound C=CCOCC=C ATVJXMYDOSMEPO-UHFFFAOYSA-N 0.000 description 1
- DFVOXRAAHOJJBN-UHFFFAOYSA-N 6-methylhept-1-ene Chemical compound CC(C)CCCC=C DFVOXRAAHOJJBN-UHFFFAOYSA-N 0.000 description 1
- FIHBHSQYSYVZQE-UHFFFAOYSA-N 6-prop-2-enoyloxyhexyl prop-2-enoate Chemical compound C=CC(=O)OCCCCCCOC(=O)C=C FIHBHSQYSYVZQE-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- GAWIXWVDTYZWAW-UHFFFAOYSA-N C[CH]O Chemical group C[CH]O GAWIXWVDTYZWAW-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- PVNIQBQSYATKKL-UHFFFAOYSA-N Glycerol trihexadecanoate Natural products CCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCC PVNIQBQSYATKKL-UHFFFAOYSA-N 0.000 description 1
- YIVJZNGAASQVEM-UHFFFAOYSA-N Lauroyl peroxide Chemical compound CCCCCCCCCCCC(=O)OOC(=O)CCCCCCCCCCC YIVJZNGAASQVEM-UHFFFAOYSA-N 0.000 description 1
- 239000011837 N,N-methylenebisacrylamide Substances 0.000 description 1
- RFFFKMOABOFIDF-UHFFFAOYSA-N Pentanenitrile Chemical compound CCCCC#N RFFFKMOABOFIDF-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- ZJCCRDAZUWHFQH-UHFFFAOYSA-N Trimethylolpropane Chemical compound CCC(CO)(CO)CO ZJCCRDAZUWHFQH-UHFFFAOYSA-N 0.000 description 1
- QYKIQEUNHZKYBP-UHFFFAOYSA-N Vinyl ether Chemical class C=COC=C QYKIQEUNHZKYBP-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001252 acrylic acid derivatives Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 125000002947 alkylene group Chemical group 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000001680 brushing effect Effects 0.000 description 1
- 101150014174 calm gene Proteins 0.000 description 1
- 150000001733 carboxylic acid esters Chemical class 0.000 description 1
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- JBSLOWBPDRZSMB-FPLPWBNLSA-N dibutyl (z)-but-2-enedioate Chemical compound CCCCOC(=O)\C=C/C(=O)OCCCC JBSLOWBPDRZSMB-FPLPWBNLSA-N 0.000 description 1
- HEJZJSIRBLOWPD-VHXPQNKSSA-N didodecyl (z)-but-2-enedioate Chemical compound CCCCCCCCCCCCOC(=O)\C=C/C(=O)OCCCCCCCCCCCC HEJZJSIRBLOWPD-VHXPQNKSSA-N 0.000 description 1
- DLBIZQBMDGOEFK-UHFFFAOYSA-N didodecyl 2-methylidenebutanedioate Chemical compound CCCCCCCCCCCCOC(=O)CC(=C)C(=O)OCCCCCCCCCCCC DLBIZQBMDGOEFK-UHFFFAOYSA-N 0.000 description 1
- 229940069096 dodecene Drugs 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- GLVVKKSPKXTQRB-UHFFFAOYSA-N ethenyl dodecanoate Chemical compound CCCCCCCCCCCC(=O)OC=C GLVVKKSPKXTQRB-UHFFFAOYSA-N 0.000 description 1
- LZWYWAIOTBEZFN-UHFFFAOYSA-N ethenyl hexanoate Chemical compound CCCCCC(=O)OC=C LZWYWAIOTBEZFN-UHFFFAOYSA-N 0.000 description 1
- AFSIMBWBBOJPJG-UHFFFAOYSA-N ethenyl octadecanoate Chemical compound CCCCCCCCCCCCCCCCCC(=O)OC=C AFSIMBWBBOJPJG-UHFFFAOYSA-N 0.000 description 1
- LDLDYFCCDKENPD-UHFFFAOYSA-N ethenylcyclohexane Chemical compound C=CC1CCCCC1 LDLDYFCCDKENPD-UHFFFAOYSA-N 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- ZNAOFAIBVOMLPV-UHFFFAOYSA-N hexadecyl 2-methylprop-2-enoate Chemical compound CCCCCCCCCCCCCCCCOC(=O)C(C)=C ZNAOFAIBVOMLPV-UHFFFAOYSA-N 0.000 description 1
- 150000002430 hydrocarbons Chemical group 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 239000010721 machine oil Substances 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- ZIUHHBKFKCYYJD-UHFFFAOYSA-N n,n'-methylenebisacrylamide Chemical compound C=CC(=O)NCNC(=O)C=C ZIUHHBKFKCYYJD-UHFFFAOYSA-N 0.000 description 1
- JRUSUOGPILMFBM-UHFFFAOYSA-N n,n-dioctylprop-2-enamide Chemical compound CCCCCCCCN(C(=O)C=C)CCCCCCCC JRUSUOGPILMFBM-UHFFFAOYSA-N 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 229940059574 pentaerithrityl Drugs 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920005651 polypropylene glycol dimethacrylate Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000010020 roller printing Methods 0.000 description 1
- 238000007650 screen-printing Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 238000007751 thermal spraying Methods 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/204—Keeping clear the surface of open water from oil spills
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Graft Or Block Polymers (AREA)
Abstract
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、吸油材の製造方法に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to a method for manufacturing an oil absorbent material.
更に詳しくは、油水混合系の油や水面に浮上している’
ii膜状膜状対しても選択的かつ効率的に油を吸収し、
しかも吸収した油の保油性能に優れ−旦吸収した油の再
放出(液ダレ等)がないため油の回収効率が良く、かつ
焼却等の後処理が容易な吸油材の製造方法に関する。In more detail, oil in an oil-water mixture system or floating on the water surface.
ii selectively and efficiently absorbs oil even in membranous membranes,
Moreover, the present invention relates to a method for producing an oil absorbing material which has excellent oil retention performance for absorbed oil, has good oil recovery efficiency since there is no re-release of absorbed oil (liquid dripping, etc.), and is easy to perform post-treatment such as incineration.
(従来の技術)
近年、海上への流出油や廃水中の油分の回収が環境保全
上大きな問題となっている。(Prior Art) In recent years, the recovery of oil spilled onto the sea and oil content from wastewater has become a major problem in terms of environmental conservation.
また、家庭や工場で廃棄される小規模の廃油や工場にお
ける機械油などの漏油の簡便な処理方法が強く望まれて
いる。In addition, there is a strong desire for a simple method for disposing of small-scale waste oil disposed of in homes and factories, as well as oil leaks such as machine oil in factories.
これらの流出油や廃水中の油分の回収あるいは廃油や漏
油の処理の有力な手段の一つとして、吸油材で油を吸着
したのち焼却その他の後処理を行う手法が従来より用い
られている。このような吸油材として、例えばボリグロ
ビレン繊維、ポリスチレン繊維、ポリエチレン繊維など
の疎水性繊維やその不織布からなる合成樹脂系吸油材が
使用されていた。One of the effective methods for recovering the oil content in these spilled oils and wastewater, or for treating waste oil and oil leaks, has traditionally been the method of adsorbing the oil with an oil-absorbing material and then incinerating or other post-treatment. . As such oil-absorbing materials, synthetic resin-based oil-absorbing materials made of hydrophobic fibers such as polyglobylene fibers, polystyrene fibers, and polyethylene fibers, and nonwoven fabrics thereof, have been used.
しかし、従来の合成樹脂系吸油材は、吸油作用が吸油材
中に存在する空隙に油を吸着保持することによるため、
次のような欠点を有していた。However, conventional synthetic resin oil-absorbing materials have an oil-absorbing effect that relies on adsorbing and retaining oil in the voids present in the oil-absorbing material.
It had the following drawbacks.
■ 吸油後の保油性能に劣っており、低粘性油に対して
は実質的に保油能がなく、また粘性油に対してもわずか
な外圧により容易に吸収していた油を再放出するため液
ブレを生じ易く、後処理がきわめて煩雑になる。■ Poor oil retention performance after oil absorption; virtually no oil retention ability for low viscosity oil; and even for viscous oil, the absorbed oil is easily re-released by slight external pressure. As a result, liquid bleeds easily occur, and post-processing becomes extremely complicated.
■ 油水混合系の油分や水面に浮上している薄膜状油の
回収に適用した場合、油の回収率が悪く、しかも水分も
多量に吸収するため、吸油材が水中に沈んで回収が困難
であったり回収後の焼却に不都合が生じなりする。■ When applied to the recovery of oil in an oil-water mixture or thin film of oil floating on the water surface, the oil recovery rate is poor, and since it also absorbs a large amount of water, the oil-absorbing material sinks into the water and is difficult to recover. Otherwise, inconveniences may arise in incineration after collection.
(発明が解決しようとする課M)
本発明は、従来の吸油材が有する上記問題点を解決する
ものである。(Problem M to be Solved by the Invention) The present invention solves the above-mentioned problems that conventional oil absorbing materials have.
すなわち、本発明の目的は、油水混合系の油や水面に浮
上している薄膜状油でも選択的かつ効率的に油を吸収し
、しかも吸収した油の保油性能に優れ一旦吸収した油の
再放出(液ダレ等)がないため油の回収効率が良く、か
つ焼却等の後処理が容易な吸油材を工業的に簡便な操作
によって再現性よく製造する方法を提供することにある
。In other words, the object of the present invention is to selectively and efficiently absorb oil even in the case of oil in an oil-water mixture system or thin film oil floating on the water surface, and to have excellent oil retention performance for the absorbed oil and to retain the oil once absorbed. It is an object of the present invention to provide a method for producing an oil absorbing material with good reproducibility by an industrially simple operation, which has good oil recovery efficiency since there is no re-release (liquid dripping, etc.), and which is easy to perform post-treatments such as incineration.
(課題を解決するための手段および作用)本発明者らは
、疎水性多孔質基材に付着せしめた特定の単量体成分を
特定の条件下で重合することにより、重合により生成す
る吸油性架橋重合体を均−且つ強固に疎水性多孔質基材
に担持することができ、この吸油性架橋重合体を疎水性
多孔質基材に担持してなる吸油材が吸油性能および保油
性能にきわめて優れていることを見いだし、本発明を完
成するに至った。(Means and effects for solving the problem) The present inventors have developed an oil-absorbing property produced by polymerization by polymerizing a specific monomer component attached to a hydrophobic porous base material under specific conditions. The cross-linked polymer can be evenly and firmly supported on the hydrophobic porous base material, and the oil-absorbing material made by supporting this oil-absorbing cross-linked polymer on the hydrophobic porous base material has excellent oil absorption and oil retention performance. We have found that this is extremely superior, and have completed the present invention.
すなわち本発明は、溶解度パラメーター(SP値)が9
以下の単量体を主成分としてなる分子中に1個の重合性
不飽和基を有する単量体(A)90〜99.999重量
%および分子中に少なくとも2個の重合性不飽和基を有
する架橋性単量体(B)0.001〜1011量%(た
だし単量体(A)および(B)の合計は100重量%で
ある)からなる単量体成分を疎水性多孔質基材に含浸付
着せしめた後、単量体成分の付着した基材を湯浴中に浸
漬して単量体成分を重合することを特徴とする、吸油性
架橋重合体を疎水性多孔質基材に担持してなる吸油材の
製造方法に関するものである。That is, the present invention has a solubility parameter (SP value) of 9.
90 to 99.999% by weight of monomer (A) having one polymerizable unsaturated group in the molecule consisting of the following monomers as main components and at least two polymerizable unsaturated groups in the molecule. A monomer component consisting of 0.001 to 1011% by weight of crosslinkable monomer (B) (however, the total of monomers (A) and (B) is 100% by weight) is added to a hydrophobic porous base material. The oil-absorbing crosslinked polymer is applied to a hydrophobic porous substrate by impregnating and adhering the oil-absorbing crosslinked polymer to a hydrophobic porous substrate, and then immersing the substrate with the monomer component attached in a hot water bath to polymerize the monomer component. The present invention relates to a method for manufacturing an oil-absorbing material in which the oil-absorbing material is supported.
溶解度パラメーター(SP値)は、化合物の極性を表わ
す尺度として一般に用いられており、本発明ではSma
llの計算式にHoyの凝集エネルギ一定数を代入して
導いた値を適用するものとし、単位(cal1国3 )
!/2で表される。Solubility parameter (SP value) is generally used as a measure to express the polarity of a compound, and in the present invention, Sma
The value derived by substituting Hoy's cohesive energy constant into the formula for ll is applied, and the unit is (cal1 country 3)
! /2.
本発明で用いられる単量体(A)の主成分を構成する単
量体は、溶解度パラメーター(SP値)が9以下で分子
中に1個の重合性不飽和基を有する単量体である。溶解
度パラメーター(SP値)が9を越える単量体を単量体
(A)の主成分に用いると、単量体成分の疎水性多孔質
基材への含浸付着が十分に行えなかったり、得られる吸
油材の吸油性能が著しく低下するため好ましくない。The monomer constituting the main component of the monomer (A) used in the present invention is a monomer having a solubility parameter (SP value) of 9 or less and one polymerizable unsaturated group in the molecule. . If a monomer with a solubility parameter (SP value) exceeding 9 is used as the main component of monomer (A), the monomer component may not be sufficiently impregnated into the hydrophobic porous substrate, or the obtained product may not be obtained. This is not preferable because the oil absorption performance of the oil absorbing material will be significantly reduced.
溶解度パラメーター(SP値)が9以下で分子中に1個
の重合性不飽和基を有する単量体としては、例えばメチ
ル(メタ)アクリレート、エチル(メタ)アクリレート
、ブチル(メタ)アクリレート、t−ブチル(メタ)ア
クリレート、2−エチルヘキシル(メタ)アクリレート
、n−オクチル(メタ)アクリレート、ドデシル(メタ
)アクリレート、ステアリル(メタ)アクリレート、フ
ェニル(メタ)アクリレート、オクチルフェニル(メタ
)アクリレート、ノニルフェニル(メタ)アクリレート
、ジノニルフェニル(メタ)アクリレート、シクロヘキ
シル(メタ)アクリレート、メンチル(メタ)アクリレ
ート、ジブチルマレエート、ジドデシルマレエート、ド
デシルクロトネート、ジドデシルイタコネートなどの不
飽和カルボン酸エステル;(ジ)ブチル(メタ)アクリ
ルアミド、(ジ)ドデシル(メタ)アクリルアミド、(
ジ)ステアリル(メタ)アクリルアミド、(ジ)ブチル
フェニル(メタ)アクリルアミド、(ジ)オクチルフェ
ニル(メタ)アクリルアミドなどの炭化水素基を有する
(メタ)アクリルアミド;1−ヘキセン、1−オクテン
、イソオクテン、1ノネン、1−デセン、1−ドデセン
などのα−オレフィン:ビニルシクロヘキサンなどの脂
環式ビニル化合物;ドテシルアリルエーテルなどの脂肪
族炭化水素基を有するアリルエーテル;カプロン酸ビニ
ル、ラウリル酸ビニル、パルミチン酸ビニル、ステアリ
ン酸ビニルなどの脂肪族炭化水素基を有するビニルエス
テル;ブチルビニルエーテル、ドデシルビニルエーテル
などの脂肪族炭化水素基を有するビニルエーテル;スチ
レン、t−ブチルスチレン、オクチルスチレンなどの芳
香族ビニル化合物などをあげることができ、これらの単
量体を1種または2種以上用いることがきる。これらの
中でも、疎水性多孔質基材に均一に付着し且つ特に優れ
た吸油性能および保油性能を与える単量体としては、少
なくとも1個の炭素数3〜30の脂肪族炭化水素基を有
し、かつアルキル(メタ)アクリレート、アルキルアリ
ール(メタ)アクリレート、アルキル(メタ)アクリル
アミド、アルキルアリール(メタ)アクリルアミド、ア
ルキルスチレンおよびα−オレフィンからなる群より選
ばれる少なくとも1種の不飽和化合物(a)を主成分と
してなる単量体(A)が特に好ましい。Examples of monomers having a solubility parameter (SP value) of 9 or less and one polymerizable unsaturated group in the molecule include methyl (meth)acrylate, ethyl (meth)acrylate, butyl (meth)acrylate, and t- Butyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, n-octyl (meth)acrylate, dodecyl (meth)acrylate, stearyl (meth)acrylate, phenyl (meth)acrylate, octylphenyl (meth)acrylate, nonylphenyl ( Unsaturated carboxylic acid esters such as meth)acrylate, dinonylphenyl(meth)acrylate, cyclohexyl(meth)acrylate, menthyl(meth)acrylate, dibutyl maleate, didodecyl maleate, dodecyl crotonate, didodecyl itaconate; di)butyl (meth)acrylamide, (di)dodecyl (meth)acrylamide, (
(Meth)acrylamide having a hydrocarbon group such as di)stearyl(meth)acrylamide, (di)butylphenyl(meth)acrylamide, (di)octylphenyl(meth)acrylamide; 1-hexene, 1-octene, isooctene, 1 α-olefins such as nonene, 1-decene, 1-dodecene; alicyclic vinyl compounds such as vinylcyclohexane; allyl ethers with aliphatic hydrocarbon groups such as dotesyl allyl ether; vinyl caproate, vinyl laurate, palmitin Vinyl esters with aliphatic hydrocarbon groups such as vinyl acid and vinyl stearate; vinyl ethers with aliphatic hydrocarbon groups such as butyl vinyl ether and dodecyl vinyl ether; aromatic vinyl compounds such as styrene, t-butylstyrene, and octylstyrene, etc. These monomers can be used alone or in combination of two or more. Among these, monomers having at least one aliphatic hydrocarbon group having 3 to 30 carbon atoms are preferred as monomers that uniformly adhere to the hydrophobic porous substrate and provide particularly excellent oil absorption and oil retention performance. and at least one unsaturated compound (a ) is particularly preferred.
このような溶解度パラメーター(SP値)が9以下の単
量体(A)中における使用量は、単量体(A)の全体量
に対して50重量%以上、より好ましくは70重量%以
上となる割合である。溶解度パラメーター(SP値)が
9以下の単量体の単量体(A、 )中の使用量が50重
量%未満では、吸油性能や保油性能に劣った吸油材しが
得られない。The amount used in the monomer (A) having a solubility parameter (SP value) of 9 or less is 50% by weight or more, more preferably 70% by weight or more based on the total amount of the monomer (A). This is the ratio. If the amount of the monomer having a solubility parameter (SP value) of 9 or less in the monomer (A, ) is less than 50% by weight, an oil-absorbing material with poor oil-absorbing performance and oil-retaining performance cannot be obtained.
したがって、本発明では、単量体(A)中に溶解度パラ
メーター(SP値)が9以下の単量体が50重量%以上
含有される必要があるが、単量体(A>中に50!l量
%以下の割合で溶解度パラメーター(SP値)が9を越
える単量体が含有されてもよい、このような単量体とし
ては、例えば(メタ)アクリル酸、アクリロニトリル、
無水マレイン酸、フマル酸、ヒドロキシエチル(メタ)
アクリレート、ポリエチレングリコール(メタ)アクリ
レート、メトキシポリエチレングリコール(メタ)アク
リレートなどをあげることができる。Therefore, in the present invention, it is necessary that the monomer (A) contains 50% by weight or more of a monomer having a solubility parameter (SP value) of 9 or less. A monomer having a solubility parameter (SP value) exceeding 9 may be contained in a proportion of 1% or less. Examples of such monomers include (meth)acrylic acid, acrylonitrile,
Maleic anhydride, fumaric acid, hydroxyethyl (meth)
Examples include acrylate, polyethylene glycol (meth)acrylate, and methoxypolyethylene glycol (meth)acrylate.
本発明で用いられる架橋性単量体(B)の例としては、
エチレングリコールジ(メタ)アクリレート、ジエチレ
ングリコールジ(メタ)アクリレート、ポリエチレング
リコールジ(メタ)アクリレート、ポリエチレングリコ
ールボリプロピレングリコールジ(メタ)アクリレート
、プロピレングリコールジ〈メタ)アクリレート、ボリ
ブロピレングリコールジ(メタ)アクリレート、13−
ブチレングリコールジ(メタ)アクリレート、ネオベン
チルグリコールジ(メタ)アクリレート、1.6−ヘキ
サンシオールジ(メタ)アクリレート、N、N−メチレ
ンビスアクリルアミド、NN−プロピレンビスアクリル
アミド、グリセリントリ(メタ)アクリレート、トリメ
チロールプロパントリ(メタ)アクリレート、テトラメ
チロールメタンテトラ(メタ)アクリレート、多価アル
コール(例えばグリセリン、トリメチロール10パンあ
るいはテトラメチロールメタン)のアルキレンオキシド
付加物と(メタ)アクリル酸とのエステル化によって得
られる多官能(メタ)アクリレートやジ・ビニルベンゼ
ンなどをあげることができ、これらの架橋性単量体を1
種または2種以上用いることができる。Examples of the crosslinkable monomer (B) used in the present invention include:
Ethylene glycol di(meth)acrylate, diethylene glycol di(meth)acrylate, polyethylene glycol di(meth)acrylate, polyethylene glycol polypropylene glycol di(meth)acrylate, propylene glycol di(meth)acrylate, polypropylene glycol di(meth)acrylate Acrylate, 13-
Butylene glycol di(meth)acrylate, neobentyl glycol di(meth)acrylate, 1,6-hexanethiol di(meth)acrylate, N,N-methylenebisacrylamide, NN-propylenebisacrylamide, glycerin tri(meth)acrylate , trimethylolpropane tri(meth)acrylate, tetramethylolmethanetetra(meth)acrylate, esterification of alkylene oxide adducts of polyhydric alcohols (e.g. glycerin, trimethylol 10 pan or tetramethylolmethane) with (meth)acrylic acid. Polyfunctional (meth)acrylates and di-vinylbenzene obtained by
One species or two or more species can be used.
本発明において疎水性多孔質基材への含浸付着に用いら
れる単量体成分中の単量体(A)および架橋性単量体(
B)の比率は、単量体(A)および架橋性単量体(B)
の合計に対して、単量体(A)が90〜99.999重
量%の範囲、架橋性単量体(B)が0.001〜10重
量%の範囲である。In the present invention, monomer (A) and crosslinkable monomer (
The ratio of B) is the monomer (A) and the crosslinkable monomer (B).
The monomer (A) is in the range of 90 to 99.999% by weight, and the crosslinkable monomer (B) is in the range of 0.001 to 10% by weight.
単量体(A)が90重量%未満であったり架橋性単量体
(B)が10重量%を越えると、重合により生成する吸
油性架橋重合体の架橋密度が高くなりすぎて多量の油を
吸収できなくなるため好ましくない、また、単量体(A
)が99.999重量%を越えたり架橋性単量体(B)
が0.001重量%未満では、重合により生成する吸油
性架橋重合体の油に対する可溶性が増大し、吸油後に吸
油性架橋重合体が疎水性多孔質基材から脱離・溶出して
吸油材本来の機能を発揮できなくなるなめ好ましくない
。If the monomer (A) is less than 90% by weight or the crosslinkable monomer (B) is more than 10% by weight, the crosslinking density of the oil-absorbing crosslinked polymer produced by polymerization will be too high, resulting in a large amount of oil. This is undesirable because the monomer (A
) exceeds 99.999% by weight or crosslinkable monomer (B)
If it is less than 0.001% by weight, the solubility of the oil-absorbing cross-linked polymer produced by polymerization in oil increases, and after oil absorption, the oil-absorbing cross-linked polymer desorbs and elutes from the hydrophobic porous base material, causing the oil-absorbing material to become indispensable. It is not desirable because it makes it impossible to perform its functions.
本発明において用いられる単量体成分は、後の重合を容
易に進行させるため一般に重合開始剤と混合して疎水性
多孔質基材への含浸付着工程に供される。このような重
合rwJ始剤としては、例えばベンゾイルパーオキシド
、ラウロイルパーオキシド、クメンハイドロパーオキシ
ドなどの有機過酸化物;2,2′−アゾビスイソブチロ
ニトリル、2.2′−アゾビスジメチルバレロニトリル
などのアゾ化合物などをあげることができる。また、単
量体成分の含浸付着を容易にするため、トルエンやシク
ロヘキサン等の疎水性有機溶削で単量体成分を希釈した
りパラフィンや高分子化合物等で単量体成分を増粘して
おいてもよい。In order to facilitate the subsequent polymerization, the monomer components used in the present invention are generally mixed with a polymerization initiator and subjected to the impregnating and adhering step to a hydrophobic porous substrate. Such polymerization rwJ initiators include, for example, organic peroxides such as benzoyl peroxide, lauroyl peroxide, and cumene hydroperoxide; 2,2'-azobisisobutyronitrile, 2,2'-azobisdimethyl Examples include azo compounds such as valeronitrile. In addition, in order to facilitate the impregnation and adhesion of the monomer components, the monomer components are diluted with hydrophobic organic abrasion such as toluene or cyclohexane, or the monomer components are thickened with paraffin or a polymer compound. You can leave it there.
本発明に用いられる疎水性多孔質基材としては、それ自
体が水に溶解したり膨潤したりしない程度の疎水性を有
し好ましくは油を吸着する高い親油性を有し、かつ単量
体成分の重合により生成する吸油性架橋重合体を有効に
担持できる広い表面積と油を吸収保持する空隙を有する
多孔質の基材であれば特に制限はなく、例えば合成繊維
や親油処理した天然m雑からなる基材を用いることがで
きる。中でも、特に優れた吸油性能を有する吸油材を提
供するものとして、ポリプロピレンやポリエチレンなど
のポリオレフィン、ポリエステル、ナイロンおよびポリ
ウレタンからなる群より選ばれる少なくとも一種の合成
繊維の不織布または織布であることが好ましい。The hydrophobic porous base material used in the present invention has hydrophobicity to the extent that it does not dissolve or swell in water, preferably has high lipophilicity to adsorb oil, and has monomer There is no particular restriction as long as it is a porous base material that has a large surface area that can effectively support the oil-absorbing crosslinked polymer produced by polymerization of the components and voids that absorb and retain oil. A base material consisting of various materials can be used. Among these, preferred is a non-woven fabric or woven fabric made of at least one synthetic fiber selected from the group consisting of polyolefins such as polypropylene and polyethylene, polyester, nylon, and polyurethane, as it provides an oil-absorbing material with particularly excellent oil-absorbing performance. .
本発明において単量体成分を疎水性多孔質基材に含浸付
着させる方法としては特に制限なく、例えばスプレーを
用いての噴霧や吹き付け、刷毛塗りやローラーやスクリ
ーンなどの公知の印刷印捺方法を用いての塗布、あるい
は疎水性多孔質基材を単量体成分に浸漬したのち必要に
応じて所定量に絞り取る方法などをあげることができる
。In the present invention, the method of impregnating and adhering the monomer component to the hydrophobic porous substrate is not particularly limited, and for example, known printing methods such as spraying, spraying, brushing, roller, or screen printing may be used. Examples include applying the monomer component using a hydrophobic porous substrate, or dipping a hydrophobic porous base material in the monomer component and then squeezing it out to a predetermined amount as necessary.
単量体成分の疎水性多孔質基材への付着量としては特に
制限ないが、疎水性多孔質基材100重量部に対して単
量体成分10〜500重量部の範囲の割合となるよう付
着させるのが好ましい、単量体成分の付着量が10重量
部未満であれば、得られる吸油材の吸油性能および保油
性能が不十分となることがあり好ましくない、また、単
量体成分の付着量が500重量%を越えると、重合によ
り生成する吸油性架橋重合体が疎水性多孔質基材の空隙
を埋めてしまう結果、吸油材の吸油性能が低下すること
があり好ましくない。There is no particular restriction on the amount of the monomer component attached to the hydrophobic porous substrate, but the proportion should be in the range of 10 to 500 parts by weight per 100 parts by weight of the hydrophobic porous substrate. If the amount of the monomer component, which is preferably attached, is less than 10 parts by weight, the oil absorption and oil retention performance of the resulting oil absorbing material may be insufficient, which is undesirable. If the adhesion amount exceeds 500% by weight, the oil-absorbing cross-linked polymer produced by polymerization will fill the voids in the hydrophobic porous base material, resulting in a decrease in the oil-absorbing performance of the oil-absorbing material, which is undesirable.
本発明において疎水性多孔質基材に付着せしめた単量体
成分を重合するには、単量体成分の付着した疎水性多孔
質基材を湯浴中に浸漬して重合を行うことが必要である
9重合を湯浴中以外の重合雰囲気たとえば空気中や不活
性カス中で行うと、重合の制御が国数となり部分的に表
面粘着性を生じるなど吸油材として好適な吸油性架橋重
合体が得られない、この結果として、吸油性架橋重合体
を疎水性多孔質基材に担持してなる吸油材を再現性良く
得られなくなり、得られた吸油材に残存する粘着性のな
め保管や使用時の取扱いに問題が生じることになる。In the present invention, in order to polymerize the monomer component attached to the hydrophobic porous substrate, it is necessary to immerse the hydrophobic porous substrate with the monomer component attached in a hot water bath for polymerization. If the polymerization is carried out in a polymerization atmosphere other than a hot water bath, such as in the air or in an inert scum, the polymerization will need to be controlled and the surface will become partially sticky, resulting in an oil-absorbing cross-linked polymer suitable as an oil-absorbing material. As a result, it becomes impossible to obtain an oil-absorbing material in which an oil-absorbing cross-linked polymer is supported on a hydrophobic porous base material with good reproducibility, and the sticky residue remaining in the obtained oil-absorbing material can be easily stored. This will cause problems in handling during use.
湯浴中で重合を行う際の重合温度や重合時間等の重合条
件は、重合開始剤の種類や量あるいは単量体成分の種類
や組成により興なるが、一般に40〜100℃好ましく
は50〜95℃に保った湯浴中に単量体成分の付着した
基材を数分から数時間保持することにより、本発明の吸
油材を得ることができる。Polymerization conditions such as polymerization temperature and polymerization time when polymerizing in a hot water bath vary depending on the type and amount of the polymerization initiator or the type and composition of the monomer components, but generally the temperature is 40-100°C, preferably 50-100°C. The oil-absorbing material of the present invention can be obtained by keeping the base material to which the monomer component is attached in a hot water bath maintained at 95° C. for several minutes to several hours.
また、より好ましくは湯浴中に不活性ガスをバブリング
して湯浴中の溶存酸素を除去することにより、より短時
間で且つより均一な本発明の吸油材を得ることができる
。Moreover, more preferably, by bubbling an inert gas into a hot water bath to remove dissolved oxygen in the hot water bath, a more uniform oil absorbing material of the present invention can be obtained in a shorter time and more uniformly.
なお、本発明で用いられる湯浴としては、温水からなる
浴を用いるのが工業的に好ましいが、単量体成分を疎水
性多孔質基材から溶出させたり該基材を劣化させるなど
の悪影響を与えない範囲で、エチレングリコール等の有
機溶射や各種添加剤を混入した湯浴を用いてもよい。Although it is industrially preferable to use a hot water bath as the hot water bath used in the present invention, it may cause adverse effects such as elution of monomer components from the hydrophobic porous substrate or deterioration of the substrate. Organic thermal spraying such as ethylene glycol or a hot water bath mixed with various additives may be used as long as it does not cause any damage.
また、このようにして得られた本発明の吸油材は、湯浴
から取り出してそのまま使用してもよいが、必要に応じ
て乾燥してから使用してもよい。Further, the oil-absorbing material of the present invention thus obtained may be used as it is after being taken out of the hot water bath, but it may be used after drying if necessary.
乾燥方法としては任意の方法が採用でき、例えば熱風、
マイクロ波、赤外線、紫外線などの手段をあげることが
できる。Any method can be used for drying, such as hot air,
Examples include microwaves, infrared rays, and ultraviolet rays.
(発明の効果)
本発明の製造方法によれば、疎水性多孔質基材に吸油性
架橋重合体を均−且つ強固に固定化させることか工業的
に簡便な操作を行うだけで達成でき、しかも本発明の製
造方法で得られる吸油材は従来の吸油材に比較して優れ
た性能を有するものである。(Effects of the Invention) According to the production method of the present invention, it is possible to uniformly and firmly immobilize an oil-absorbing crosslinked polymer on a hydrophobic porous substrate by simply performing an industrially simple operation. Moreover, the oil-absorbing material obtained by the production method of the present invention has superior performance compared to conventional oil-absorbing materials.
すなわち、本発明の製造方法により得られる吸油材は、
疎水性多孔質基材に吸着した油を更に吸油性架橋重合体
が吸収して膨潤する吸油機構を有するため、従来の吸油
材に比べ以下の■〜■の優れた吸油性能を示す。That is, the oil absorbent obtained by the production method of the present invention is
Since it has an oil-absorbing mechanism in which the oil-absorbing crosslinked polymer further absorbs the oil adsorbed on the hydrophobic porous base material and swells, it exhibits the following excellent oil-absorbing performance compared to conventional oil-absorbing materials.
■ 吸油後の保油性能に優れ、液ダレを生じることがな
く、焼却等の後処理が極めて容易である。■ Excellent oil retention performance after oil absorption, no dripping, and post-treatment such as incineration is extremely easy.
■ 水をほとんど吸収せず、油のみを選択的に吸収する
ため、油水混合系からの油や水面に浮上している薄膜状
油などの回収に高い効果を示す。■ Because it absorbs almost no water and only selectively absorbs oil, it is highly effective in recovering oil from oil-water mixed systems and thin oil films floating on the water surface.
従って本発明は、家庭用廃油処理用、工業用廃油処理用
、漏油処理用の他、廃水処理用、ビット、港湾、湖沼や
海上へ流出した浮上油処理用などに適する吸油材の製造
方法としてきわめて有用である。Therefore, the present invention provides a method for producing an oil-absorbing material that is suitable for household waste oil treatment, industrial waste oil treatment, oil leak treatment, waste water treatment, and treatment of floating oil spilled into bits, ports, lakes, and the sea. It is extremely useful as a
(実施例)
次に、本発明を実施例および比較例をあげて詳細に説明
するが、本発明はこれだけLこ限定されるものではない
、なお、鋼中に特に断わりのない限り部は重量部を表す
ものとする。(Example) Next, the present invention will be explained in detail with reference to Examples and Comparative Examples. However, the present invention is not limited to L. shall represent the division.
実施例1
容量1.9Jのステンレス製バットに、単量体(A)と
してノニルフェニルアクリレート(SP値:8.3>9
9.794部、架橋性単量体(B)として1.6−ヘキ
サンジオールジアクリレート0.206部および重合開
始刑としてベンゾイルパーオキシド0.5部からなる溶
液を仕込んだ。Example 1 In a stainless steel vat with a capacity of 1.9 J, nonyl phenyl acrylate (SP value: 8.3>9
A solution consisting of 9.794 parts of 1,6-hexanediol diacrylate as a crosslinkable monomer (B) and 0.206 parts of benzoyl peroxide as a polymerization initiator was charged.
ついで、この溶液中に20■×15■に裁断したポリプ
ロピレン不織布(目付け200 t / rr? 。Then, in this solution, a polypropylene nonwoven fabric cut into 20cm x 15cm pieces (basis weight 200t/rr?) was added.
嵩密度0.1trl■3)を浸漬したのち引き上げ、簡
易ローラーにて絞った。この時の単量体溶液の付着量は
ポリプロピレン不織布100部に対して100部の割合
であった。After dipping the sample with a bulk density of 0.1 trl (3), it was pulled up and squeezed using a simple roller. The amount of the monomer solution deposited at this time was 100 parts per 100 parts of the polypropylene nonwoven fabric.
その後この単量体溶液の付着したポリプロピレン不織布
を窒素バブリング状態で80℃に保温された湯浴(温水
)中に2時間浸漬し、さらに90℃に昇温し、同温度で
2時開維持して重合を行った。湯浴から引き上げたポリ
プロピレン不織布を熱風乾燥機中、100℃で1時間乾
燥することにより吸油材(1)を得な。Thereafter, the polypropylene nonwoven fabric to which this monomer solution was attached was immersed in a hot water bath (warm water) maintained at 80°C under nitrogen bubbling for 2 hours, and then further heated to 90°C and kept open at the same temperature for 2 hours. Polymerization was carried out. Oil absorbent material (1) was obtained by drying the polypropylene nonwoven fabric taken out of the hot water bath at 100° C. for 1 hour in a hot air dryer.
実施例2
実施例1において、単量体(A>としてヘキサデシルメ
タクリレート(SP値ニア、8)49゜930部および
N−オクチルメタクリルアミド(SP値:8.6>49
.930部、架橋性単量体(B)としてジビニルベンゼ
ン0.140部を代わりに用いた以外は、実施例1と同
様の方法により吸油材(2)を得た。なお、この時の単
量体溶液の付着量はポリプロピレン不織布100部に対
して100部の割合であった。Example 2 In Example 1, 49°930 parts of hexadecyl methacrylate (SP value near, 8) and N-octyl methacrylamide (SP value: 8.6>49) were used as monomers (A>).
.. An oil absorbent material (2) was obtained in the same manner as in Example 1, except that 930 parts of divinylbenzene was used instead of 930 parts of divinylbenzene as the crosslinkable monomer (B). The amount of the monomer solution deposited at this time was 100 parts per 100 parts of the polypropylene nonwoven fabric.
実施例3
実施例1において、単量体(A)としてドデシルアクリ
レート(SP値: 7.9> 55.704部およびN
、N−ジオクチルアクリルアミド(SP値:8.2)3
7.136部、架橋性単量体(B)としてボリプロビレ
ングリコールジメタクリレート(分子量4000)7.
160部を代わりに用いた以外は、実施例1と同様の方
法により吸油材(3)を得た。なお、この時の単量体溶
液の付着量はポリプロピレン不織布100部に対して1
00部の割合であった。Example 3 In Example 1, dodecyl acrylate (SP value: 7.9>55.704 parts and N
, N-dioctyl acrylamide (SP value: 8.2) 3
7.136 parts, polypropylene glycol dimethacrylate (molecular weight 4000) as crosslinkable monomer (B)7.
An oil-absorbing material (3) was obtained in the same manner as in Example 1 except that 160 parts was used instead. The amount of monomer solution deposited at this time is 1 part per 100 parts of polypropylene nonwoven fabric.
The ratio was 0.00 parts.
実施例4
実施例1において、単量体(A)としてドデシルアクリ
レート(SP値ニア、9)99゜823部、架橋性単量
体(B)としてエチレングリコールジアクリレート0.
177部を代わりに用いた以外は、実施例1と同様の方
法により吸油材(4)を得た。なお、この時の単量体溶
液の付着量はポリプロピレン不織布100部に対して1
00部の割合であった。Example 4 In Example 1, 99.823 parts of dodecyl acrylate (SP value near, 9) was used as the monomer (A), and 0.823 parts of ethylene glycol diacrylate was used as the crosslinkable monomer (B).
An oil absorbent material (4) was obtained in the same manner as in Example 1 except that 177 parts was used instead. The amount of monomer solution deposited at this time is 1 part per 100 parts of polypropylene nonwoven fabric.
The ratio was 0.00 parts.
実施例5
実施例1において、単量体(A)としてt−ブチルスチ
レン(SP値=7゜9)54.881部および1−デゼ
ン(SP値ニア、0)44.903部、架橋性単量体(
B)としてジビニルベンゼン0.216部を代わりに用
いた以外は、実施例1と同様の方法により吸油材(5)
を得た。なお、この時の単量体溶液の付着量はポリプロ
ピレン不織布100部に対して100部の割合であった
。Example 5 In Example 1, the monomers (A) were 54.881 parts of t-butylstyrene (SP value = 7°9), 44.903 parts of 1-dezene (SP value near, 0), and a crosslinkable monomer. Quantity (
Oil absorbent material (5) was prepared in the same manner as in Example 1, except that 0.216 parts of divinylbenzene was used instead of B).
I got it. The amount of the monomer solution deposited at this time was 100 parts per 100 parts of the polypropylene nonwoven fabric.
実施例6
実施例1において、単量体(A)としてノニルフェニル
アクリレート(SP値: 8.3>74゜793部およ
びヒドロキシエチルアクリレート(SP値: 10.3
)24.931部、架橋性単量体(B)として1.6−
ヘキサンジオールジアクリレート0.276部を代わり
に用いた以外は、実施例1と同様の方法により吸油材(
6)を得た。Example 6 In Example 1, nonylphenyl acrylate (SP value: 8.3>74°793 parts) and hydroxyethyl acrylate (SP value: 10.3) were used as the monomer (A).
) 24.931 parts, 1.6- as crosslinkable monomer (B)
The oil-absorbing material (
6) was obtained.
なお、この時の単量体溶液の付着量はポリプロピレン不
織布100部に対して100部の割合であった。The amount of the monomer solution deposited at this time was 100 parts per 100 parts of the polypropylene nonwoven fabric.
実施例7
実施例4において、ポリプロピレン不繊布の代わりにポ
リエステル不織布(目付け200t/d。Example 7 In Example 4, polyester nonwoven fabric (basis weight 200 t/d) was used instead of polypropylene nonwoven fabric.
嵩密度0、Ig/■5)を用いた以外は、実施例4と同
様の方法により吸油材(7)を得た。なお、この時の単
量体溶液の付着量はポリエステル不織布100部に対し
て200部の割合であった。An oil-absorbing material (7) was obtained in the same manner as in Example 4, except that a bulk density of 0 and Ig/■5) was used. The amount of the monomer solution deposited at this time was 200 parts per 100 parts of the polyester nonwoven fabric.
実施例8
20■×151に裁断したナイロン不織布(目付け20
0g/イ、嵩密度0.1sr/■3)に単量体(A>と
してドデシルアクリレート(SP値ニア、9)99.8
23部、架橋性単量体(B)としてエチレングリコール
ジアクリレート0.177部および重合開始剤としてベ
ンゾイルパーオキシドからなる溶液をスプレーを用いて
均一に散布した。この時の単量体溶液の付着量はナイロ
ン不織布100部に対して50部の割合であった。Example 8 Nylon nonwoven fabric cut into 20×151 pieces (basis weight 20
0g/I, bulk density 0.1sr/■3) and monomer (A> dodecyl acrylate (SP value near, 9) 99.8
A solution consisting of 23 parts of ethylene glycol diacrylate, 0.177 parts of ethylene glycol diacrylate as a crosslinkable monomer (B), and benzoyl peroxide as a polymerization initiator was uniformly sprayed using a sprayer. The amount of the monomer solution deposited at this time was 50 parts per 100 parts of the nylon nonwoven fabric.
その後この単量体溶液の付着したナイロン不織布を窒素
バブリング状態で80℃に保温された湯浴(温水)中に
2時間浸漬し、さらに90℃に昇温し、同温度で2時間
維持して重合を行った。湯浴から引き上げたナイロン不
織布を熱風乾燥機中、100℃で1時間乾煉することに
より吸油材(8)を得た。Thereafter, the nylon nonwoven fabric to which this monomer solution was attached was immersed in a hot water bath (warm water) kept at 80°C under nitrogen bubbling for 2 hours, then further heated to 90°C, and maintained at the same temperature for 2 hours. Polymerization was performed. The nylon nonwoven fabric taken out of the hot water bath was dried in a hot air dryer at 100°C for 1 hour to obtain an oil absorbent material (8).
比較例1
実施例1において、単量体(A)としてドデシルアクリ
レート(SP値: 7.9)89.820部、架橋性単
量体(B)としてエチレングリコールジアクリレート1
0.180部を代わりに用いた以外は、実施例1と同様
の方法により比較吸油材(1)を得た。なお、この時の
単量体溶液の付着量はポリプロピレン不織布100部に
対して100部の割合であった。Comparative Example 1 In Example 1, 89.820 parts of dodecyl acrylate (SP value: 7.9) was used as the monomer (A), and 1 ethylene glycol diacrylate was used as the crosslinkable monomer (B).
A comparative oil absorbent material (1) was obtained in the same manner as in Example 1 except that 0.180 part was used instead. The amount of the monomer solution deposited at this time was 100 parts per 100 parts of the polypropylene nonwoven fabric.
比較例2
実施例1において、単量体(A>としてドデシルアクリ
レート39.854部およびメタクリル酸(SP値:
10.1)59.780部、架橋性単量体(B)として
エチレングリコールジアクリレート0.366部を代わ
りに用いた以外は、実施例1と同様の方法により比較吸
油材(2)を得た。なお、この時の単量体溶液の付着量
はポリプロピレン不織布100部に対して100部の割
合であった。Comparative Example 2 In Example 1, 39.854 parts of dodecyl acrylate and methacrylic acid (SP value:
10.1) Comparative oil-absorbing material (2) was obtained in the same manner as in Example 1, except that 59.780 parts and 0.366 parts of ethylene glycol diacrylate were used as the crosslinkable monomer (B). Ta. The amount of the monomer solution deposited at this time was 100 parts per 100 parts of the polypropylene nonwoven fabric.
比較例3
実施例4において、架橋性単量体(B)としてのエチレ
ングリコールジアクリレートを用いなかった以外は、実
施例4と同様の方法により比較吸油材(3)を得た。な
お、この時の単量体溶液の付着量はポリプロピレン不織
布100部に対して100部の割合であった。Comparative Example 3 A comparative oil-absorbing material (3) was obtained in the same manner as in Example 4, except that ethylene glycol diacrylate as the crosslinkable monomer (B) was not used. The amount of the monomer solution deposited at this time was 100 parts per 100 parts of the polypropylene nonwoven fabric.
比較例4
実施例1で得たのと同じ単量体溶液の付着したポリプロ
ピレン不織布を窒素雰囲気下に80℃に保温された温風
乾燥機中に入れ、80℃で2時間加熱した後90℃に昇
温し、同温度で2時間維持して重合を行なうことにより
比較吸油材(4)を得た。この比較吸油材(4)を触感
により実施例1で得られた吸油材(1)と比較したとこ
ろ、部分的に粘着性が残り、重合の不均一性が認められ
た。Comparative Example 4 A polypropylene nonwoven fabric coated with the same monomer solution as obtained in Example 1 was placed in a hot air dryer kept at 80°C under a nitrogen atmosphere, heated at 80°C for 2 hours, and then dried at 90°C. Comparative oil absorbent material (4) was obtained by increasing the temperature to 100% and maintaining the same temperature for 2 hours to carry out polymerization. When this comparative oil-absorbing material (4) was compared to the oil-absorbing material (1) obtained in Example 1 by touch, stickiness remained in some parts and non-uniformity of polymerization was observed.
実施例9(吸油性能試験)
実施例1〜8で得られた吸油材(1)〜(8)、比較例
1〜4で得られた比較吸油材(1)〜〈4〉および実施
例1で用いたのと同じポリプロピレン不織布のそれぞれ
を10国×101に裁断し、この裁断された試料のそれ
ぞれを20℃の条件下にゲロシンまたはスピンドル油中
に浸漬した。24時間後に引き上げて試料をクリップで
挾み、釣り下げ状態で30分間空中に放置して試料に保
持されない油を十分に流下せしめた後、試料の重量を測
定し、次式に従って吸油材に保持された油の量(吸油量
)を計算しな。Example 9 (Oil absorption performance test) Oil absorbing materials (1) to (8) obtained in Examples 1 to 8, comparative oil absorbing materials (1) to <4> obtained in Comparative Examples 1 to 4, and Example 1 Each of the same polypropylene nonwoven fabrics used in Example 1 was cut into 10 x 101 pieces, and each of the cut samples was immersed in gelosin or spindle oil at 20°C. After 24 hours, lift the sample, clamp the sample with clips, and leave it hanging in the air for 30 minutes to allow the oil not retained in the sample to flow down sufficiently. Measure the weight of the sample, and hold it on the oil absorbing material according to the following formula. Calculate the amount of oil absorbed (oil absorption amount).
吸油量(g)=吸油後の試料の重量−浸漬前の試料の重
量
結果を第1表に示す。Oil absorption amount (g) = weight of sample after oil absorption - weight of sample before immersion The results are shown in Table 1.
実施例10(i油性能試験)
実施例9で得た吸油後の試料のそれぞれを200メツシ
ユの金網上にのせて、試料に10kg/cdの荷重を1
分間かけ、その時に流出する油量を測定し、次式に従い
加重後の保油率を計算した。Example 10 (i-oil performance test) Each of the oil-absorbed samples obtained in Example 9 was placed on a 200-mesh wire mesh, and a load of 10 kg/cd was applied to the sample.
The amount of oil flowing out at that time was measured, and the oil retention rate after weight was calculated according to the following formula.
保油率(%)=((吸油量−流出油量)/吸油量)×1
00
(なお、吸油量(g)は実施例9における計算式%式%
)
結果を第1表に示す。Oil retention rate (%) = ((oil absorption amount - spilled oil amount) / oil absorption amount) x 1
00 (The oil absorption amount (g) is calculated using the formula % in Example 9.
) The results are shown in Table 1.
第1表
実施例11(浮上油回収試験)
容量361の水槽に水30j (水面の面積=1350
cd)を入れ、さらに水面にA重油15gを添加しな、
この水面上に実施例1〜8で得られた吸油材(1)〜(
8)および比較例1〜4で得られた比較吸油材(1)〜
(4)ならびに実施例1で用いたのと同じポリプロピレ
ン不織布のそれぞれを10cmX10cmに裁断した試
料を4時間浮かべたのち引き上げ、水面上のA重油の残
存の様子から浮上油回収能を次の基準により評価した。Table 1 Example 11 (Floating oil recovery test) 30j of water in a water tank with a capacity of 361 (area of water surface = 1350
cd) and then add 15g of heavy oil A to the water surface.
On this water surface, the oil absorbing materials (1) to (1) obtained in Examples 1 to 8 are
8) and comparative oil absorbing materials (1) obtained in Comparative Examples 1 to 4.
(4) and samples of the same polypropylene nonwoven fabric used in Example 1 cut into 10 cm x 10 cm were floated for 4 hours and then pulled up. Based on the residual A heavy oil on the water surface, the floating oil recovery ability was evaluated according to the following criteria. evaluated.
○:水面上にA重油が全く残存しない。○: No heavy oil A remains on the water surface.
△:水面上にA重油がわずかに点在する。Δ: Heavy oil A is slightly scattered on the water surface.
×:水面上にA重油がかなりの量で残存する。×: A considerable amount of heavy oil A remains on the water surface.
その結果を第2表に示す。The results are shown in Table 2.
Claims (1)
主成分としてなる分子中に1個の重合性不飽和基を有す
る単量体(A)90〜99.999重量%および分子中
に少なくとも2個の重合性不飽和基を有する架橋性単量
体(B)0.001〜10重量%(ただし単量体(A)
および(B)の合計は100重量%である)からなる単
量体成分を疎水性多孔質基材に含浸付着せしめた後、単
量体成分の付着した基材を湯浴中に浸漬して単量体成分
を重合することを特徴とする、吸油性架橋重合体を疎水
性多孔質基材に担持してなる吸油材の製造方法。 2、単量体(A)が少なくとも1個の炭素数3〜30の
脂肪族炭化水素基を有し、且つアルキル(メタ)アクリ
レート、アルキルアリール(メタ)アクリレート、アル
キル(メタ)アクリルアミド、アルキルアリール(メタ
)アクリルアミド、アルキルスチレンおよびα−オレフ
ィンからなる群より選ばれる少なくとも1種の不飽和化
合物(a)を主成分としてなるものである請求項1記載
の吸油材の製造方法。 3、単量体(A)が請求項2記載の不飽和化合物(a)
を単量体(A)中に50重量%以上含有してなるもので
ある請求項1または2記載の吸油材の製造方法。 4、疎水性多孔質基材がポリオレフィン、ポリエステル
、ナイロンおよびポリウレタンからなる群より選ばれる
少なくとも一種の合成繊維の不織布または織布である請
求項1記載の吸油材の製造方法。[Claims] 1. Monomer (A) having one polymerizable unsaturated group in the molecule, which is mainly composed of a monomer with a solubility parameter (SP value) of 9 or less, from 90 to 99.999. Weight% and crosslinkable monomer (B) having at least two polymerizable unsaturated groups in the molecule 0.001 to 10% by weight (however, monomer (A)
and (B) (total of 100% by weight) is impregnated onto a hydrophobic porous substrate, and then the substrate with the monomer component attached is immersed in a hot water bath. A method for producing an oil-absorbing material in which an oil-absorbing crosslinked polymer is supported on a hydrophobic porous base material, the method comprising polymerizing a monomer component. 2. Monomer (A) has at least one aliphatic hydrocarbon group having 3 to 30 carbon atoms, and alkyl (meth)acrylate, alkylaryl (meth)acrylate, alkyl (meth)acrylamide, alkylaryl 2. The method for producing an oil absorbing material according to claim 1, wherein the main component is at least one unsaturated compound (a) selected from the group consisting of (meth)acrylamide, alkylstyrene, and α-olefin. 3. Monomer (A) is the unsaturated compound (a) according to claim 2
3. The method for producing an oil-absorbing material according to claim 1, wherein the monomer (A) contains 50% by weight or more of the following. 4. The method for producing an oil-absorbing material according to claim 1, wherein the hydrophobic porous base material is a nonwoven or woven fabric of at least one synthetic fiber selected from the group consisting of polyolefin, polyester, nylon, and polyurethane.
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2148670A JPH0441584A (en) | 1990-06-08 | 1990-06-08 | Process for producing oil absorptive material |
| AU70039/91A AU651567B2 (en) | 1990-01-29 | 1991-01-19 | Oil-absorbent polymer and use therefor |
| AT9191300645T ATE105209T1 (en) | 1990-01-29 | 1991-01-29 | OIL ABSORBENT POLYMER AND ITS USE. |
| EP91300645A EP0441512B1 (en) | 1990-01-29 | 1991-01-29 | Oil- absorbent polymer and use therefor |
| CA002035216A CA2035216A1 (en) | 1990-01-29 | 1991-01-29 | Oil-absorbent polymer and use therefor |
| DE69101851T DE69101851T2 (en) | 1990-01-29 | 1991-01-29 | Oil absorbing polymer and its use. |
| US08/126,731 US5374600A (en) | 1990-01-29 | 1993-09-27 | Oil-absorbent polymer and use therefor |
| US08/579,888 US5641847A (en) | 1990-01-29 | 1995-12-28 | Oil-absorbent polymer and use therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2148670A JPH0441584A (en) | 1990-06-08 | 1990-06-08 | Process for producing oil absorptive material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0441584A true JPH0441584A (en) | 1992-02-12 |
Family
ID=15457995
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2148670A Pending JPH0441584A (en) | 1990-01-29 | 1990-06-08 | Process for producing oil absorptive material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0441584A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112725906A (en) * | 2020-12-29 | 2021-04-30 | 河北工业大学 | Electrostatic spinning preparation method of porous polylactic acid fiber oil absorption material |
-
1990
- 1990-06-08 JP JP2148670A patent/JPH0441584A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112725906A (en) * | 2020-12-29 | 2021-04-30 | 河北工业大学 | Electrostatic spinning preparation method of porous polylactic acid fiber oil absorption material |
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