JPS62265302A - Production of water-soluble vinyl polymer - Google Patents
Production of water-soluble vinyl polymerInfo
- Publication number
- JPS62265302A JPS62265302A JP10894886A JP10894886A JPS62265302A JP S62265302 A JPS62265302 A JP S62265302A JP 10894886 A JP10894886 A JP 10894886A JP 10894886 A JP10894886 A JP 10894886A JP S62265302 A JPS62265302 A JP S62265302A
- Authority
- JP
- Japan
- Prior art keywords
- water
- solution
- polymerization initiator
- cyclodextrin
- polymerization
- 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
- 229920002554 vinyl polymer Polymers 0.000 title claims abstract description 9
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 239000003505 polymerization initiator Substances 0.000 claims abstract description 27
- 229920000858 Cyclodextrin Polymers 0.000 claims abstract description 17
- HFHDHCJBZVLPGP-UHFFFAOYSA-N schardinger α-dextrin Chemical compound O1C(C(C2O)O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC(C(O)C2O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC2C(O)C(O)C1OC2CO HFHDHCJBZVLPGP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 150000001728 carbonyl compounds Chemical group 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 239000000243 solution Substances 0.000 abstract description 24
- 238000006116 polymerization reaction Methods 0.000 abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 20
- -1 carboxyl compound Chemical class 0.000 abstract description 15
- 239000000178 monomer Substances 0.000 abstract description 14
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 abstract description 12
- 239000007864 aqueous solution Substances 0.000 abstract description 9
- 239000012046 mixed solvent Substances 0.000 abstract description 7
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 abstract description 6
- ISAOCJYIOMOJEB-UHFFFAOYSA-N benzoin Chemical compound C=1C=CC=CC=1C(O)C(=O)C1=CC=CC=C1 ISAOCJYIOMOJEB-UHFFFAOYSA-N 0.000 abstract description 6
- 244000028419 Styrax benzoin Species 0.000 abstract description 3
- 235000000126 Styrax benzoin Nutrition 0.000 abstract description 3
- 235000008411 Sumatra benzointree Nutrition 0.000 abstract description 3
- 229960002130 benzoin Drugs 0.000 abstract description 3
- 235000019382 gum benzoic Nutrition 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 229920000642 polymer Polymers 0.000 abstract description 3
- QSJXEFYPDANLFS-UHFFFAOYSA-N Diacetyl Chemical group CC(=O)C(C)=O QSJXEFYPDANLFS-UHFFFAOYSA-N 0.000 abstract description 2
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical compound C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 abstract description 2
- 239000012965 benzophenone Substances 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 abstract description 2
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 abstract 2
- WURBFLDFSFBTLW-UHFFFAOYSA-N benzil Chemical compound C=1C=CC=CC=1C(=O)C(=O)C1=CC=CC=C1 WURBFLDFSFBTLW-UHFFFAOYSA-N 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 abstract 1
- 239000008240 homogeneous mixture Substances 0.000 abstract 1
- 239000012456 homogeneous solution Substances 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 13
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 12
- 229920003169 water-soluble polymer Polymers 0.000 description 9
- 150000003839 salts Chemical class 0.000 description 8
- MSAHTMIQULFMRG-UHFFFAOYSA-N 1,2-diphenyl-2-propan-2-yloxyethanone Chemical compound C=1C=CC=CC=1C(OC(C)C)C(=O)C1=CC=CC=C1 MSAHTMIQULFMRG-UHFFFAOYSA-N 0.000 description 7
- 239000001116 FEMA 4028 Substances 0.000 description 7
- WHGYBXFWUBPSRW-FOUAGVGXSA-N beta-cyclodextrin Chemical compound OC[C@H]([C@H]([C@@H]([C@H]1O)O)O[C@H]2O[C@@H]([C@@H](O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O3)[C@H](O)[C@H]2O)CO)O[C@@H]1O[C@H]1[C@H](O)[C@@H](O)[C@@H]3O[C@@H]1CO WHGYBXFWUBPSRW-FOUAGVGXSA-N 0.000 description 7
- 235000011175 beta-cyclodextrine Nutrition 0.000 description 7
- 229960004853 betadex Drugs 0.000 description 7
- 239000000126 substance Substances 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- 229910001873 dinitrogen Inorganic materials 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- NEHMKBQYUWJMIP-UHFFFAOYSA-N chloromethane Chemical compound ClC NEHMKBQYUWJMIP-UHFFFAOYSA-N 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 229920006322 acrylamide copolymer Polymers 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 3
- QWQFVUQPHUKAMY-UHFFFAOYSA-N 1,2-diphenyl-2-propoxyethanone Chemical compound C=1C=CC=CC=1C(OCCC)C(=O)C1=CC=CC=C1 QWQFVUQPHUKAMY-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
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 2
- JKNCOURZONDCGV-UHFFFAOYSA-N 2-(dimethylamino)ethyl 2-methylprop-2-enoate Chemical compound CN(C)CCOC(=O)C(C)=C JKNCOURZONDCGV-UHFFFAOYSA-N 0.000 description 2
- JADMAVSCPFDMLP-UHFFFAOYSA-N 2-(dimethylamino)ethyl 2-methylprop-2-enoate;prop-2-enamide Chemical compound NC(=O)C=C.CN(C)CCOC(=O)C(C)=C JADMAVSCPFDMLP-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000007872 degassing Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 239000003999 initiator Substances 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 229940050176 methyl chloride Drugs 0.000 description 2
- 239000004570 mortar (masonry) Substances 0.000 description 2
- 230000000379 polymerizing effect Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Inorganic materials [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- SKMHHHHLLBKNKR-UHFFFAOYSA-M sodium;prop-2-enamide;prop-2-enoate Chemical compound [Na+].NC(=O)C=C.[O-]C(=O)C=C SKMHHHHLLBKNKR-UHFFFAOYSA-M 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- PQUXFUBNSYCQAL-UHFFFAOYSA-N 1-(2,3-difluorophenyl)ethanone Chemical compound CC(=O)C1=CC=CC(F)=C1F PQUXFUBNSYCQAL-UHFFFAOYSA-N 0.000 description 1
- JAHNSTQSQJOJLO-UHFFFAOYSA-N 2-(3-fluorophenyl)-1h-imidazole Chemical compound FC1=CC=CC(C=2NC=CN=2)=C1 JAHNSTQSQJOJLO-UHFFFAOYSA-N 0.000 description 1
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 1
- ZAFNJMIOTHYJRJ-UHFFFAOYSA-N Diisopropyl ether Chemical compound CC(C)OC(C)C ZAFNJMIOTHYJRJ-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 150000008043 acidic salts Chemical class 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000021615 conjugation Effects 0.000 description 1
- 125000000113 cyclohexyl group Chemical class [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical compound CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 description 1
- LVHBHZANLOWSRM-UHFFFAOYSA-N methylenebutanedioic acid Natural products OC(=O)CC(=C)C(O)=O LVHBHZANLOWSRM-UHFFFAOYSA-N 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000006303 photolysis reaction Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 229940047670 sodium acrylate Drugs 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- NLVXSWCKKBEXTG-UHFFFAOYSA-N vinylsulfonic acid Chemical compound OS(=O)(=O)C=C NLVXSWCKKBEXTG-UHFFFAOYSA-N 0.000 description 1
- 229920003176 water-insoluble polymer Polymers 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Polymerisation Methods In General (AREA)
Abstract
Description
【発明の詳細な説明】 本発明は水溶性ビニル系重合体の製法に関する。[Detailed description of the invention] The present invention relates to a method for producing a water-soluble vinyl polymer.
さらに詳しくはシクロデキストリンで抱接された重合開
始剤を用いることを特徴とする光重合法による水溶性ビ
ニル系重合体の製法に関するものである。More specifically, the present invention relates to a method for producing a water-soluble vinyl polymer by a photopolymerization method characterized by using a polymerization initiator encapsulated with cyclodextrin.
水溶性ビニル系モノマーの水溶液を重合させて水溶性重
合体を得る方法の一つとして、従来から知られているよ
うに、紫外線領域の波長を照射させて、いわゆる光重合
法が提案されている。As one method of polymerizing an aqueous solution of a water-soluble vinyl monomer to obtain a water-soluble polymer, a so-called photopolymerization method has been proposed, which involves irradiation with wavelengths in the ultraviolet region. .
この光重合法は、一般的に光照射のみによる、即ち、直
接光重合法による場合は、まれであり、重合開始剤を併
用することが多く、特に工業的には重合開始剤の使用は
必須要件である。This photopolymerization method generally relies only on light irradiation, that is, direct photopolymerization is rare, and a polymerization initiator is often used in combination, and the use of a polymerization initiator is essential, especially in industrial applications. It is a requirement.
重合開始剤の種類は、対象とする水溶性ビニル系モノマ
ーの種類、重合液のモノマー濃度、目的とする重合体の
分子量等を考慮して選定されるのが、普通であるが、そ
の他照射される光線の波長にも特別に留意して選択され
るべきである。その理由として重合開始剤は特有の波長
の光線を吸収、その励起によって、ラジカルに分解後、
重合の開始に働くために、即ち、各種波長の光線を照射
されるとき、そのうちで一定の波長の光線のみを選択的
に吸収することによって、はじめて重合開始剤のラジカ
ル分解が発生して、モノマーの重合がF=(能となりえ
るからである。The type of polymerization initiator is usually selected by considering the type of water-soluble vinyl monomer to be targeted, the monomer concentration of the polymerization solution, the molecular weight of the target polymer, etc. The wavelength of the light beam used should also be selected with special consideration. The reason for this is that the polymerization initiator absorbs light of a specific wavelength, and due to its excitation, it decomposes into radicals, and then
In order to initiate polymerization, in other words, when irradiated with light rays of various wavelengths, by selectively absorbing only the rays of a certain wavelength, radical decomposition of the polymerization initiator occurs for the first time, and monomers are formed. This is because the polymerization of can result in F=(ability).
そのため、一定波長の光線を発する照射装置にて、光重
合を行なう場合、いかなる種類の重合開始剤を選定して
もよいわけでなく、その波長に対応した吸収帯を有する
重合開始剤の種類の選定が極めて重要となってくる。
ところで、従来から知られている水溶性重合体の光重合
には、300nm〜400nm、なかでも360nm近
辺の波長の、一般的には近紫外線と称されるものが多用
されている。それは近紫外線が360nmを中心波長を
有しているので、例えば、300nmより短かい波長を
有する紫外線と比較して、肉眼に対しては安全で、実際
プラントに設こした場合、短時間では、作業者の肉眼に
悪影響を与えることがないという利点と、近紫外線用ラ
ンプがケミカルランプとして、安価に市販されていると
いう二つの理由からきている0例えば、東芝製ケミカル
ランプFL40SBL、Phi 1ips製TLADK
30W105.松下電工製プランクライトブルー jj
j光灯などである。このように安価な市販の近紫外線対
に対して各種の重合開始剤が開発され使用されている。Therefore, when photopolymerization is carried out using an irradiation device that emits light of a certain wavelength, it is not permissible to select any type of polymerization initiator, but only the type of polymerization initiator that has an absorption band corresponding to the wavelength. Selection becomes extremely important.
By the way, in the photopolymerization of conventionally known water-soluble polymers, what is generally called near ultraviolet light, which has a wavelength of 300 nm to 400 nm, particularly around 360 nm, is often used. Because near ultraviolet rays have a center wavelength of 360 nm, they are safer to the naked eye than, for example, ultraviolet rays with wavelengths shorter than 300 nm. This comes from two reasons: the advantage of not having a negative impact on the naked eye of workers, and the fact that near-ultraviolet lamps are commercially available as chemical lamps at low prices.For example, Toshiba's chemical lamp FL40SBL, Phi 1ips' TLADK.
30W105. Matsushita Electric Works Plank Light Blue jj
j Light lamps, etc. Various polymerization initiators have been developed and used for these inexpensive commercially available near-UV pairs.
その中でも、重合の対象が水溶性重合体の場合では、従
来から重合開始剤として。Among them, when the target of polymerization is a water-soluble polymer, it has traditionally been used as a polymerization initiator.
一般的にカルボニル化合物が使用されているのが汀通で
1例えば350nm近傍に、吸収極大を示すペンツフェ
ノン、そして近紫外線照射の下で多用されるアゾビスイ
ソブチロニトリル、またベンゾイン系等、カルボニル化
合物として、良く使用される。Generally, carbonyl compounds are used in Tingtong.1 For example, pentuphenone, which has an absorption maximum near 350 nm, azobisisobutyronitrile, which is often used under near ultraviolet irradiation, and carbonyl compounds such as benzoin, etc. Often used as a compound.
しかし、それらは共通して一般的疎水性を有するので、
水溶媒系への溶解は不良で水を溶媒とするモノマー重合
液中への重合開始剤の溶解が必須要件となる水溶性重合
体の場合には、極めて不都合なものとなっている。これ
を改善するため、従来からメタノールなど各種アルコー
ルなどの溶媒に、あらかじめ開始剤としてのカルボニル
化合物を重合液中に溶解した後、光照射を行なうか、ま
たは界面活性剤の併用によりその親水性を高めて重合液
中に乳化分散することが行なわれてきた。However, since they have general hydrophobicity in common,
This is extremely inconvenient in the case of water-soluble polymers, which have poor solubility in aqueous solvent systems and require dissolution of the polymerization initiator into a monomer polymerization solution using water as a solvent. In order to improve this problem, conventionally, a carbonyl compound as an initiator is dissolved in a polymerization solution in advance in a solvent such as various alcohols such as methanol, and then light irradiation is performed, or the hydrophilicity is increased by using a surfactant in combination. Emulsification and dispersion in a polymerization solution has been carried out at a high concentration.
しかし、このように、重合開始剤を水溶性モノマー中に
溶解させる従来の方法は重合開始剤溶解のための溶媒に
よる連鎖移動および界面活性剖使用による泡立ちと、重
合液の透明性の低下などに起因して水溶性型合本として
の、水溶性の低下をもたらす他、分子量アップを阻害す
るなどの欠点がある。However, the conventional method of dissolving a polymerization initiator in a water-soluble monomer has problems such as chain transfer due to the solvent used to dissolve the polymerization initiator, foaming due to the use of surfactants, and a decrease in the transparency of the polymerization solution. As a result, there are drawbacks such as a decrease in water solubility as a water-soluble type compound, as well as inhibiting an increase in molecular weight.
本発明者らは、これらの問題点を解消するため、鋭意研
究を行なった結果、本発明に到達したものである。即ち
、本発明は、
シクロデキストリンで抱接された重合開始剤を用。In order to solve these problems, the present inventors conducted intensive research and arrived at the present invention. That is, the present invention uses a polymerization initiator encapsulated with cyclodextrin.
いることを特徴とする光重合法による水溶性ビニル系重
合体の製法を提供するものである。The present invention provides a method for producing a water-soluble vinyl polymer by a photopolymerization method, characterized in that:
本発明により、水溶性重合体の重合に際して、特にカル
ボニル化合物系開始剤の親木性を高めて、水への溶解性
を改良する目的で、予め重合開始剤をシクロデキストリ
ンによって、抱接させて、重合開始剤の親水性を充分に
高めて、水溶性となし、重合液中への均一分散を促進し
、これによって、均一な光重合を可能とならしめ、高分
子量かつ、水溶性の極めて優れた水溶性重合体の製法を
確立したものである。According to the present invention, when polymerizing a water-soluble polymer, the polymerization initiator is conjugated with cyclodextrin in advance, especially for the purpose of increasing the affinity of the carbonyl compound-based initiator and improving its solubility in water. , the hydrophilicity of the polymerization initiator is sufficiently increased to make it water-soluble, promoting uniform dispersion in the polymerization solution, thereby enabling uniform photopolymerization, and making it extremely water-soluble with high molecular weight. This method established an excellent method for producing water-soluble polymers.
このように、シクロデキストリンにより抱接された重合
開始剤を用いて光重合を行なう場合、シクロデキストリ
ン自体に紫外線および可視光線領域の両方の波長領域に
おいて、吸収がないことが確認されているので、抱接さ
れて水溶性を有するようになった重合開始剤の光分解が
抱接によって阻害されることはない。In this way, when photopolymerization is carried out using a polymerization initiator encapsulated by cyclodextrin, it has been confirmed that cyclodextrin itself has no absorption in both the ultraviolet and visible light wavelength regions. Photodecomposition of a polymerization initiator that has become water-soluble due to inclusion is not inhibited by inclusion.
なお、本発明に用いる水溶性ビニルモノマーとしては、
例えば、アクリルアミド、メタクリルアミド、アクリル
酸、メタクリル酸、ビニルスルホン酸、アクリルアミド
−メチルプロパンスルホ/酸、イタコン酸等、または、
それらの塩類、(メタ)アクリル酸ジアルキルアミノア
ルキルエステル類、それらの塩、もしくは酸性塩類、ま
たは。In addition, the water-soluble vinyl monomer used in the present invention includes:
For example, acrylamide, methacrylamide, acrylic acid, methacrylic acid, vinyl sulfonic acid, acrylamide-methylpropane sulfo/acid, itaconic acid, etc.
their salts, (meth)acrylic acid dialkylaminoalkyl esters, their salts, or acid salts;
その四級化物、ジアルキルアミノアルキルアクリルアミ
ド類、それらの塩もしくは酸性塩類、または、それらの
四級化物等が挙げられ、これらは単独または2種以上を
混合して用いてもよい。Examples include quaternized products thereof, dialkylaminoalkylacrylamides, salts or acidic salts thereof, and quaternized products thereof, and these may be used alone or in combination of two or more kinds.
本発明において用いられ重合開始剤としては、バイアセ
チル系、ベンゾフェノン系、ベンジル系、ベンゾイン系
、シクロヘキサン系を含むカルボニル化合物が、好まし
く選らばれる。As the polymerization initiator used in the present invention, carbonyl compounds including biacetyl, benzophenone, benzyl, benzoin, and cyclohexane compounds are preferably selected.
本発明に用いれらる紫外線の波長としては約200nm
から400nmに及ぶものか、または300nm〜40
0nmの範囲に限定されるものでもよい。The wavelength of ultraviolet rays used in the present invention is approximately 200 nm.
to 400nm, or 300nm to 40nm
It may be limited to a range of 0 nm.
本発明により、水溶性重合体の製法に際して。According to the present invention, in the production of water-soluble polymers.
近紫外線照射下での、特に、カルボニル化合物よりなる
重合開始剤を有機溶媒に予め溶解し、その後、重合液中
に分散溶解させるという従来の方法に代って、カルボニ
ル化合物よりなる重合開始剤の、そのままでは疎水性の
ものを、重合開始剤の抱接によって、水溶性を向上させ
、親木性となして1重合液中に均一に溶解せしめて、均
一な重合反応を行なうことができ、また1本発明により
、従来技術より、格段に高分子量かつ、極めて優れた水
溶性を有する水溶性重合体の重合を可能としたものであ
る。In particular, in place of the conventional method of dissolving a polymerization initiator made of a carbonyl compound in advance in an organic solvent and then dispersing it in a polymerization solution under near ultraviolet irradiation, the polymerization initiator made of a carbonyl compound is By incorporating a polymerization initiator, a hydrophobic substance can be improved in water solubility and become wood-philic, allowing it to be uniformly dissolved in a single polymerization solution and carrying out a uniform polymerization reaction. Furthermore, the present invention has made it possible to polymerize a water-soluble polymer having a much higher molecular weight and extremely superior water solubility than conventional techniques.
次に1本発明を実施例により具体的に説明する。Next, one embodiment of the present invention will be specifically explained using examples.
実施例1
市販のβ−シクロデキストリン[半井化学薬品株式会社
製]20.0gを、イソプロピルアルコール/木=50
wt、7wt、%(7)U合溶媒1,000gに均一に
溶解後、ベンゾインイソプロピルエーテル4.5gを混
合、攪拌し、均一に溶解させる。約1時間、攪拌後、混
合溶媒を70℃の温水で加熱しつつ真空下で、完全に蒸
発させ、白色の蒸発乾固物を得る。Example 1 20.0 g of commercially available β-cyclodextrin [manufactured by Hanui Chemical Co., Ltd.] was mixed with isopropyl alcohol/wood = 50
wt, 7wt, % (7) After uniformly dissolving in 1,000 g of U mixed solvent, 4.5 g of benzoin isopropyl ether is mixed and stirred to uniformly dissolve. After stirring for about 1 hour, the mixed solvent is completely evaporated under vacuum while heating with hot water at 70° C. to obtain a white evaporated solid.
この粉末は、β−シクロデキストリン/ベンゾインイソ
プロピルエーテルのモル比率が、はぼ1mo1/1mo
1.重量比では、4.5wt、%/1wt、%の抱接物
となっていると推定される。This powder has a molar ratio of β-cyclodextrin/benzoin isopropyl ether of approximately 1 mo 1/1 mo.
1. The weight ratio is estimated to be 4.5wt, %/1wt, % inclusions.
これを乳鉢で細かく、すりつぶして得られた微粉末のベ
ンゾインイソプロピルエーテルの抱接物中には約18%
程度のベンゾインイソプロピルエーテルが含まれている
ものと仮定し、ベンゾインイソプロピルエーテルの抱接
物を0.111g採取する。一方、600gのアクリル
酸ソーダ20m01%含有の組成のアクリルアミド水溶
液を七ツマー濃度33.3%となるよう調製し、pHを
約10.0に合せたモノマー液を窒素ガスで脱気し、酸
素を駆逐後、ベンゾインイソプロピルエーテル抱接物0
.111gを水50gに予め溶解し。The finely powdered benzoin isopropyl ether conjugate obtained by grinding this in a mortar contains about 18%
0.111 g of benzoin isopropyl ether conjugate is collected. On the other hand, 600g of an acrylamide aqueous solution containing 20ml of sodium acrylate was prepared with a composition of 33.3%. After expulsion, benzoin isopropyl ether conjugate 0
.. Dissolve 111 g in 50 g of water in advance.
窒素ガスで脱気後、その溶解液をモノマー液に混入し、
よく攪拌する。このときベンゾインイソプロピルエーテ
ル抱接物0.111g中のベンゾインインプロピルエー
テルは附子ツマー液1100ppの濃度となっている。After degassing with nitrogen gas, the dissolved solution is mixed into the monomer solution,
Stir well. At this time, the concentration of benzoin propyl ether in 0.111 g of the benzoin isopropyl ether conjugate was 1100 pp of Zimmer's solution.
この重合溶液を予め窒素ガスで充満されたガラス蓋付き
の外部を10℃の冷却水を通じた構造のジャケット付き
の重合器に入れ上部より市販の東芝製ケミカルランプF
L40SBLfiによす360nmを中心とする近紫外
線を照射し、30分後、重合溶液はゴム状の弾性体に変
る。これを、取り出し市販の肉挽機で1.0mm〜2.
0mmの細片状に砕き70°Cの熱風で120分間乾燥
し。This polymerization solution was placed in a jacketed polymerization vessel with a glass lid that was previously filled with nitrogen gas, and the outside was heated with cooling water at 10°C, and a commercially available Toshiba Chemical Lamp F
L40SBLfi was irradiated with near-ultraviolet light centered at 360 nm, and after 30 minutes, the polymerization solution turned into a rubber-like elastic body. Take this out and grind it with a commercially available meat grinder to 1.0 mm to 2.
It was crushed into 0 mm pieces and dried with hot air at 70°C for 120 minutes.
水分80%の粉末のアクリル酸ソーダーアクリルアミド
共玉合体を得た。A powdered acrylic acid/acrylamide co-merged powder having a water content of 80% was obtained.
この粉末の固有粘度をA14定したところ[η]=30
.5 (d I/g)[1N−NaC1,30℃]とい
う驚くべき高い値を示し、水不溶分(%)を求めると。The intrinsic viscosity of this powder was determined by A14 [η] = 30
.. It showed a surprisingly high value of 5 (d I/g) [1N-NaCl, 30°C], and when the water-insoluble content (%) was determined.
[粉末サンプル固形分−溶解 水不溶分(%)=□ 粉末サンプル固形分g サンプル固形分]g x 100=0.04(%) と少なく極めて水溶性の良好な結果が得られた。[Powder sample solid content - dissolved Water insoluble content (%) = □ Powder sample solid content g Sample solid content]g x 100=0.04(%) Very good water solubility was obtained.
従来の場合、かかる重合の条件下では、[η]=20.
0〜23 、0 (d l/g) 、水不溶分(%)=
0.11〜0.25(%)程度の値が普通に得られてい
る点からみて実施例1で示された通り本発明は各段に優
れていることが確認される。Conventionally, under such polymerization conditions, [η]=20.
0 to 23, 0 (d l/g), water insoluble content (%) =
In view of the fact that values of about 0.11 to 0.25 (%) are commonly obtained, it is confirmed that the present invention is superior in each level as shown in Example 1.
比較例1
β−シクロデキストリンに抱接を行なわず、ベンジイン
イソプロピルエーテルのみを、0.02gを、2.0g
のメタノールに溶解させ、実施例1の七ツマー液に混合
実施例1の七ツマー液に混合、実施例1と同様の近紫外
線照射を行ない、得られた粉末のアクリル醜ソーダーア
クリルラミド共重合体の固有粘度=21.3 [dl/
g] 、水不溶解方(%)=0.13%であった。実施
例1と比較して固有粘度も低く、また水不溶解方も多く
、水溶性重合体としては、品質的に劣るものであった。Comparative Example 1 0.02g of benzine isopropyl ether alone without conjugation to β-cyclodextrin, 2.0g
The powdered acrylic ugly soda acrylamide copolymer was dissolved in methanol, mixed with the 7-summer solution of Example 1, mixed with the 7-summer solution of Example 1, and irradiated with near ultraviolet rays in the same manner as in Example 1. Intrinsic viscosity = 21.3 [dl/
g], water insoluble (%) = 0.13%. Compared to Example 1, the intrinsic viscosity was lower, and more water-insoluble polymers were present, resulting in inferior quality as a water-soluble polymer.
実施例2
実tA例1において、ベンゾインインプロピルエーテル
を、ベンジルに替えて、抱接化合物となし、他の条件を
同様に保ち、アクリル酸ソーダーアクリルアミド共重合
体の粉末を得た。Example 2 In Practical Example 1, benzoin propyl ether was replaced with benzyl as an inclusion compound, and other conditions were kept the same to obtain a powder of a sodium acrylate acrylamide copolymer.
粉末の固有粘度=29.8 [dl/g]と高く、水不
溶分(%)=0.06%と少なく、いずれも従来のもの
より優れたものであった。The powder had a high intrinsic viscosity of 29.8 [dl/g] and a low water-insoluble content (%) of 0.06%, both of which were superior to conventional powders.
比較例2
実施例1において、ベンゾインイソプロピルエーテルを
ベンゾジルに替えて、抱接させることなく、メタノール
に溶解させて他の条件を同様に保ち、アクリル酸ソーダ
ーアクリルアミド共重合体の粉末を得た。Comparative Example 2 In Example 1, benzoin isopropyl ether was replaced with benzodyl, and the powder was dissolved in methanol without inclusion, keeping the other conditions the same, to obtain a powder of a sodium acrylate acrylamide copolymer.
粉末の固有粘度=20.7 [dt/g] 、水不溶分
(%)=0.17(%)であった。The intrinsic viscosity of the powder was 20.7 [dt/g], and the water-insoluble content (%) was 0.17 (%).
実施例3
市販のβ−シクロデキストリン[半井化学薬品製]12
.0gをイソプロピルアルコール/水=50wt 、5
7wt、%の混合溶媒1.000gに均一に溶解後、ベ
ンジルメチルケタール2.7gを混合攪拌し、均一に溶
解させる。Example 3 Commercially available β-cyclodextrin [manufactured by Hanui Chemicals] 12
.. 0g to isopropyl alcohol/water = 50wt, 5
After uniformly dissolving in 1.000 g of a mixed solvent of 7 wt%, 2.7 g of benzyl methyl ketal is mixed and stirred to uniformly dissolve.
約1時間、攪拌後、混合溶媒を70℃の温水で外部加熱
しつつ真空下で、完全に蒸発させて得られた蒸発乾固物
は白色で、β−シクロデキストリン/ベンジルメチルケ
タールのモル比率が約1m。After stirring for about 1 hour, the mixed solvent was completely evaporated under vacuum while externally heating with hot water at 70°C. The evaporated solid product obtained was white and had a molar ratio of β-cyclodextrin/benzyl methyl ketal. is about 1m.
1/1mo1.重量比では、4.5wt、%/1wt・
%の抱接物となっていると推定される。これを、乳鉢で
細かくすりつぶして得られた微粉末のベンジルメチルケ
タールの抱接物中には約18%程度のベンジルメチルケ
タールが含まれるものと仮定し、ベンジルメチルケター
ルの抱接物を0.067g採取する。一方、285.0
gのジメチルアミノエチルメタアクリレートの塩化メチ
ル四級塩を80モル%とアクリルアミド20モル%の比
率のモノマーを主成分とするモノマー濃度70.0%の
水溶液を:A製し、pH=5.0にyJ整し、窒素ガス
で脱気し、酸素を除きベンジルメチルケタール抱接物0
.067gを水30gに、予め溶解し、窒素ガスで脱気
後、その溶解液をモノマー液に混入し、よく攪拌する。1/1mo1. Weight ratio: 4.5wt, %/1wt・
It is estimated that % of the inclusions are present. Assuming that about 18% benzyl methyl ketal is contained in the finely powdered benzyl methyl ketal conjugate obtained by finely grinding this in a mortar, the benzyl methyl ketal conjugate is 0. Collect 067g. On the other hand, 285.0
An aqueous solution with a monomer concentration of 70.0%, the main component of which is methyl chloride quaternary salt of dimethylaminoethyl methacrylate of 80 mol % and acrylamide 20 mol %, was prepared by A, and the pH was 5.0. yJ, degassed with nitrogen gas, and removed oxygen to remove benzyl methyl ketal conjugate.
.. After dissolving 067 g in 30 g of water in advance and degassing with nitrogen gas, the solution was mixed into the monomer solution and stirred well.
このとき0.067gの抱接物中のベンジルメチルケタ
ールは対モノマー液、約60ppmの濃度となっている
。At this time, the concentration of benzyl methyl ketal in 0.067 g of clathrate was about 60 ppm relative to the monomer solution.
この重合溶液を予め窒素ガスで充満されたガラス蓋付き
の外部を10’0の冷却水を通じた構造のジャケントを
設けた重合容器に入れ上部より市販の東芝製ケミカルラ
ンプFL20SBL型により。This polymerization solution was placed in a polymerization container equipped with a jacket with a glass lid that was previously filled with nitrogen gas and had a structure in which 10'0 of cooling water was passed through the polymerization container, and a commercially available Toshiba chemical lamp FL20SBL type was used from the top.
360nmを中心とする近紫外線を照射し、50分後重
合溶液は固いゴム状の弾性体を得る。これを取り出し、
市販の肉挽機で2.0mm〜3.0mmの細片状に砕さ
、70℃の熱風で120分間乾燥し、水分9.2%の粉
末のアクリルアミド−ジメチルアミノエチルメタクリレ
ートの四級用共重合体を得た。Near ultraviolet light having a wavelength of 360 nm is irradiated, and after 50 minutes, the polymerization solution becomes a hard rubber-like elastic body. Take this out,
Grind into pieces of 2.0 mm to 3.0 mm with a commercially available meat grinder, dry with hot air at 70°C for 120 minutes, and prepare a quaternary powder of acrylamide-dimethylaminoethyl methacrylate with a moisture content of 9.2%. A polymer was obtained.
この粉末の固有粘度[lN−NaC1,30℃Jを41
1定したところ、
[η] =13.5 [dl/g]という高い値であり
。The intrinsic viscosity of this powder [lN-NaCl, 30°C J is 41
When the temperature was set to 1, it was a high value of [η] = 13.5 [dl/g].
不溶分(%)=0.01%と少なく、極めて優れたもの
であった・
従来の場合、かかる条件下では、[η]=7.0〜8.
0[dl/g1.不溶分(%)=0.04%が普通であ
る。The insoluble content (%) was as low as 0.01%, which was extremely excellent. In the conventional case, under such conditions, [η] = 7.0 to 8.
0[dl/g1. Insoluble content (%) = 0.04% is normal.
実施例4
実施例3において、イソプロピルアルコール/水=50
wt 、57wt、%の混合溶媒を使用することなく、
水30gに12.0gのβ−シクロデキストリンとベン
ジルメチルケタール2.7gと混合攪拌し、均一に溶解
させ、約2.5時間攪拌することによって、溶媒を使用
することなく水溶媒中でβ−シクロデキストリンによる
ベンジルメチルケタール抱接物の水溶液0.204gを
採取する。この中にはベンジルメチルケタール0.01
23gを内臓する0、067gの抱接物が含まれている
。この抱接物の水溶液0.204gを実施例3と同様に
ジメチルアミノエチルメタアクリレートの塩化メチル四
級塩の80モル%、アクリルアミド20モル%の比率の
モノマーを主成分とする七ツマー液濃度70.0%での
pH=5.0となる水溶液の285gに加え、同様の光
重合を行ない、粉末のアクリルアミド−ジメチルアミノ
エチルメタアクリレートの四級塩の共重合体を得た。こ
のときベンジルメチルケタール抱接物に含まれるベンジ
ルメチルケタールは対モノマー液6oppmの濃度であ
る。Example 4 In Example 3, isopropyl alcohol/water = 50
wt, 57wt, without using a mixed solvent of %,
By mixing and stirring 12.0 g of β-cyclodextrin and 2.7 g of benzyl methyl ketal in 30 g of water, dissolving them uniformly, and stirring for about 2.5 hours, β- 0.204 g of an aqueous solution of benzyl methyl ketal conjugate with cyclodextrin is collected. This contains 0.01 benzyl methyl ketal.
Contains 0,067 g of inclusions containing 23 g. In the same manner as in Example 3, 0.204 g of an aqueous solution of this conjugate was added to a 70-mer solution containing monomers with a ratio of 80 mol% of methyl chloride quaternary salt of dimethylaminoethyl methacrylate and 20 mol% of acrylamide as main components. In addition to 285 g of an aqueous solution having a pH of 5.0 at 0%, the same photopolymerization was carried out to obtain a powdery copolymer of acrylamide-dimethylaminoethyl methacrylate quaternary salt. At this time, the benzyl methyl ketal contained in the benzyl methyl ketal conjugate has a concentration of 6 oppm relative to the monomer liquid.
この固有粘度をl1111定したところ、[η]=13
、3 [d l/g] と高く、不溶分=0.01%と
少なく、極めて優れたものであり、実施例3と大差がな
かった。When this intrinsic viscosity was determined by l1111, [η]=13
, 3 [d l/g] and a low insoluble content of 0.01%, which was extremely excellent and not much different from Example 3.
比較例3
実施例3において、β−シクロデキストリンを使用せず
、ベンジルメチルケタール0.012gを抱接物とする
ことなく2.0gのメタノールに溶解して、実施例3の
水溶液を調製した後、同様の光重合を行なって得た粉末
のアクリルアミド−ジメチル7ミノエチルメタアクリレ
ートの四級塩の共重合体は、[η]=7.3[dl/g
1.不溶分=0.04%であり、実施例4および実施例
3の両方に劣るものであった。Comparative Example 3 After preparing the aqueous solution of Example 3 without using β-cyclodextrin and dissolving 0.012 g of benzyl methyl ketal in 2.0 g of methanol without using it as an conjugate. The copolymer of powdered acrylamide-dimethyl 7-minoethyl methacrylate quaternary salt obtained by the same photopolymerization had [η] = 7.3 [dl/g
1. The insoluble content was 0.04%, which was inferior to both Example 4 and Example 3.
Claims (3)
いることを特徴とする光重合法による水溶性ビニル系重
合体の製法。(1) A method for producing a water-soluble vinyl polymer by a photopolymerization method, which is characterized by using a polymerization initiator encapsulated with cyclodextrin.
許請求の範囲第1項記載の製法。(2) The production method according to claim 1, wherein the polymerization initiator is a carbonyl compound.
ろの特許請求の範囲第1項または第2項記載の製法。(3) The manufacturing method according to claim 1 or 2, wherein the wavelength of the irradiated light is centered around 360 nm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10894886A JPS62265302A (en) | 1986-05-12 | 1986-05-12 | Production of water-soluble vinyl polymer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10894886A JPS62265302A (en) | 1986-05-12 | 1986-05-12 | Production of water-soluble vinyl polymer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62265302A true JPS62265302A (en) | 1987-11-18 |
Family
ID=14497703
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10894886A Pending JPS62265302A (en) | 1986-05-12 | 1986-05-12 | Production of water-soluble vinyl polymer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62265302A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5521266A (en) * | 1994-10-28 | 1996-05-28 | Rohm And Haas Company | Method for forming polymers |
US6613703B1 (en) | 2000-04-27 | 2003-09-02 | Kimberly-Clark Worldwide, Inc. | Thermoplastic nonwoven web chemically reacted with a cyclodextrin compound |
JP2009114221A (en) * | 2007-11-01 | 2009-05-28 | Tokuyama Dental Corp | Curable composition |
-
1986
- 1986-05-12 JP JP10894886A patent/JPS62265302A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5521266A (en) * | 1994-10-28 | 1996-05-28 | Rohm And Haas Company | Method for forming polymers |
US5710226A (en) * | 1994-10-28 | 1998-01-20 | Rohm And Haas Company | Method for forming polymers |
US6613703B1 (en) | 2000-04-27 | 2003-09-02 | Kimberly-Clark Worldwide, Inc. | Thermoplastic nonwoven web chemically reacted with a cyclodextrin compound |
JP2009114221A (en) * | 2007-11-01 | 2009-05-28 | Tokuyama Dental Corp | Curable composition |
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