JPS6050809B2 - Method for producing acrylamide polymer - Google Patents
Method for producing acrylamide polymerInfo
- Publication number
- JPS6050809B2 JPS6050809B2 JP12309775A JP12309775A JPS6050809B2 JP S6050809 B2 JPS6050809 B2 JP S6050809B2 JP 12309775 A JP12309775 A JP 12309775A JP 12309775 A JP12309775 A JP 12309775A JP S6050809 B2 JPS6050809 B2 JP S6050809B2
- Authority
- JP
- Japan
- Prior art keywords
- acrylamide
- present
- polymer
- aqueous solution
- 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.)
- Expired
Links
- 229920002401 polyacrylamide Polymers 0.000 title claims description 13
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims description 23
- 239000000178 monomer Substances 0.000 claims description 5
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 5
- 239000012736 aqueous medium Substances 0.000 claims description 4
- -1 acrylic ester Chemical class 0.000 description 13
- 239000007864 aqueous solution Substances 0.000 description 12
- 229920000642 polymer Polymers 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- 238000006116 polymerization reaction Methods 0.000 description 7
- 150000003839 salts Chemical class 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000003995 emulsifying agent Substances 0.000 description 5
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical class [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000004220 aggregation Methods 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000008394 flocculating agent Substances 0.000 description 3
- 230000003311 flocculating effect Effects 0.000 description 3
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 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
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical class OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 150000003926 acrylamides Chemical class 0.000 description 2
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium peroxydisulfate Substances [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 2
- VAZSKTXWXKYQJF-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)OOS([O-])=O VAZSKTXWXKYQJF-UHFFFAOYSA-N 0.000 description 2
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000007720 emulsion polymerization reaction Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 150000007529 inorganic bases Chemical class 0.000 description 2
- 239000002609 medium Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 150000007530 organic bases Chemical class 0.000 description 2
- 150000002978 peroxides Chemical class 0.000 description 2
- 229940077386 sodium benzenesulfonate Drugs 0.000 description 2
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 2
- MZSDGDXXBZSFTG-UHFFFAOYSA-M sodium;benzenesulfonate Chemical compound [Na+].[O-]S(=O)(=O)C1=CC=CC=C1 MZSDGDXXBZSFTG-UHFFFAOYSA-M 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 239000004342 Benzoyl peroxide Substances 0.000 description 1
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 150000005215 alkyl ethers Chemical class 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 238000010533 azeotropic distillation Methods 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 235000019400 benzoyl peroxide Nutrition 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000003093 cationic surfactant Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 239000003623 enhancer Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000000887 hydrating effect Effects 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 239000007764 o/w emulsion Substances 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- SGLDQLCVBBVVAJ-UHFFFAOYSA-N prop-2-enamide;sulfuric acid Chemical compound NC(=O)C=C.OS(O)(=O)=O SGLDQLCVBBVVAJ-UHFFFAOYSA-N 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000012966 redox initiator Substances 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 229910001948 sodium oxide Inorganic materials 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- KVCGISUBCHHTDD-UHFFFAOYSA-M sodium;4-methylbenzenesulfonate Chemical compound [Na+].CC1=CC=C(S([O-])(=O)=O)C=C1 KVCGISUBCHHTDD-UHFFFAOYSA-M 0.000 description 1
- KQFAFFYKLIBKDE-UHFFFAOYSA-M sodium;ethanesulfonate Chemical compound [Na+].CCS([O-])(=O)=O KQFAFFYKLIBKDE-UHFFFAOYSA-M 0.000 description 1
- KKVTYAVXTDIPAP-UHFFFAOYSA-M sodium;methanesulfonate Chemical compound [Na+].CS([O-])(=O)=O KKVTYAVXTDIPAP-UHFFFAOYSA-M 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 150000008054 sulfonate salts Chemical class 0.000 description 1
- 150000003460 sulfonic acids Chemical class 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 150000003512 tertiary amines Chemical class 0.000 description 1
- 239000007762 w/o emulsion Substances 0.000 description 1
- 239000003021 water soluble solvent Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Polymerisation Methods In General (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
【発明の詳細な説明】
本発明はアクリルアミド系重合体の製造方法に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing an acrylamide polymer.
詳しくは溶解性および凝集能が共に優れ、特に凝集剤と
して好適なアクリルアミド系重合体の製造方法に関する
ものである。ポリアクリルアミド類は凝集剤、土壌沈降
剤、紙力増強剤等の多くの用途に付されている。なかて
も凝集剤用は種々の廃水に対して優れた効果を奏するの
で脚光を浴びている。いづれの用途に適用するにしろポ
リアクリルアミド類は溶解性及び凝集能が共に優れたも
のが要求され、とくに凝集剤用に対する要求は厳しい。Specifically, the present invention relates to a method for producing an acrylamide polymer that has excellent solubility and flocculating ability and is particularly suitable as a flocculant. Polyacrylamides are used for many purposes such as flocculants, soil settling agents, and paper strength enhancers. Among these, flocculants are in the spotlight because they have excellent effects on various types of wastewater. Regardless of the application, polyacrylamides are required to have excellent solubility and flocculating ability, and the requirements for use as flocculants are particularly severe.
しかしながら、一般に溶解性及び凝集能はいづれか一方
を向上させると他方が低下するという傾向が認められ、
両者の性能を共に向上させることは極めて困難であつた
。しカルて、本発明者らはかかる傾向を有するポリアク
リルアミド類の性能の向上につき鋭意研究したところ特
定の塩の存在下でアクリルアミド類を重合するならば、
ポリアクリルアミド類の安定性を損うことなく溶解性及
び凝集能が共に優れ、商品価値の極めて高いポリアクリ
ルアミド類が得られることを見出し、本発明に到達した
。However, it is generally recognized that when either solubility or aggregation ability is improved, the other decreases.
It has been extremely difficult to improve the performance of both. The present inventors have conducted extensive research into improving the performance of polyacrylamides that have such a tendency, and have found that if acrylamides are polymerized in the presence of a specific salt,
The present invention was achieved by discovering that polyacrylamides with excellent solubility and aggregation ability and extremely high commercial value can be obtained without impairing the stability of polyacrylamides.
すなわち本発明の要旨は、アクリルアミドまたはアクリ
ルアミドおよびこれと共重合し得る単量体とを水性媒体
中で重合する際に、重合性不飽和結合を含まない有機ス
ルホン酸塩を存在させることを特徴とするアクリルアミ
ド系重合体の製造方法に存する。本発明を詳細に説明す
るに、本発明において原料として使用されるアクリルア
ミドとしては、特に制限されるものではなく、アクリル
アミドと水と硫酸とを反応させ、アクリルアミド硫酸塩
とした後アルカリで中和して得られるアクリルアミド・
であつてもよいし、アクリロニトリルを金属含有触媒の
存在下接触的に水和して得られるアクリルアミドであつ
てもよい。That is, the gist of the present invention is characterized in that when acrylamide or acrylamide and a monomer copolymerizable therewith are polymerized in an aqueous medium, an organic sulfonate containing no polymerizable unsaturated bond is present. The present invention relates to a method for producing an acrylamide polymer. To explain the present invention in detail, the acrylamide used as a raw material in the present invention is not particularly limited, and acrylamide is reacted with water and sulfuric acid to form an acrylamide sulfate salt, which is then neutralized with an alkali. Acrylamide obtained by
or acrylamide obtained by catalytically hydrating acrylonitrile in the presence of a metal-containing catalyst.
しカルて、後者の方法により水溶液として得られるアク
リルアミド水溶液に本発明方法を適用すフる場合、特に
優れた効果を奏する。In particular, when the method of the present invention is applied to an aqueous acrylamide solution obtained as an aqueous solution by the latter method, particularly excellent effects can be achieved.
またアクリルアミドと共重合し得る単量体としてはアク
リル酸、アクリル酸ソータ、アクリル酸エステル、酢酸
ビニル等が挙げられる。Examples of monomers that can be copolymerized with acrylamide include acrylic acid, acrylic acid sorter, acrylic ester, and vinyl acetate.
アクリルアミドあるいはアクリルアミドと他の5単量体
とを水性媒体中て重合する方法としては水溶液重合、乳
化重合等アクリルアミド系重合体の製造法として周知の
重合方法が適用される。As a method for polymerizing acrylamide or acrylamide and the other five monomers in an aqueous medium, well-known polymerization methods for producing acrylamide polymers such as aqueous solution polymerization and emulsion polymerization can be applied.
たとえば水溶液重合は70%以下、好ましくは11〜5
0%アクリルアミド水溶液に過硫酸カリ、過儲酸アンモ
ニウム、過酸化水素、過酸化ベンゾイル等の過酸化物、
アゾビスイソブチロニトリル、2,2!−アゾビス(2
−アミジノプロパン)2塩酸塩等のアゾ系遊離基開始剤
をアクリルアミドに対して、0.001〜2重量%添加
し、通常、40〜80℃に加熱することによつて実施さ
れる。勿論、亜硫酸ソーダ等の金属塩あるいは第3級ア
ミンと過酸化物を組合せた所謂レドックス系の開始剤を
使用してもよく、この楊合にはより低温での重合が可能
になる。また、乳化重合は70%以下、好ましくは30
〜60%のアクリルアミド水溶液を四塩化炭素、ジクロ
ルエタン、トリクロルエチレンのような塩素化炭化水素
、ヘキサン、シクロヘキサンのような脂肪族、脂環族の
炭化水素、あるいはベンゼン、キシレンのような芳香族
炭化水素等の有機媒体に乳化させ、水溶液重合の場合と
同様の開始剤の存在下加熱することによつて実施される
。For example, aqueous solution polymerization is 70% or less, preferably 11 to 5
0% acrylamide aqueous solution with peroxides such as potassium persulfate, ammonium peroxide, hydrogen peroxide, benzoyl peroxide, etc.
Azobisisobutyronitrile, 2,2! -Azobis (2
-amidinopropane) dihydrochloride or the like is added in an amount of 0.001 to 2% by weight based on acrylamide, and the reaction is usually carried out by heating the mixture to 40 to 80°C. Of course, a so-called redox initiator, which is a combination of a metal salt such as sodium sulfite or a tertiary amine and a peroxide, may be used, and this polymerization can be carried out at a lower temperature. In addition, emulsion polymerization is 70% or less, preferably 30%
~60% acrylamide aqueous solution with carbon tetrachloride, chlorinated hydrocarbons such as dichloroethane, trichlorethylene, aliphatic or alicyclic hydrocarbons such as hexane or cyclohexane, or aromatic hydrocarbons such as benzene or xylene. The polymerization is carried out by emulsifying the polymer in an organic medium such as and heating in the presence of the same initiator as in the case of aqueous solution polymerization.
上記有機媒体のアクリルアミド水溶液に対する重量比は
、通常1〜3である。The weight ratio of the organic medium to the acrylamide aqueous solution is usually 1 to 3.
乳化剤としては、ポリオキシエチレンアルキルエーテル
型、ポリオキシエチレンアルキルフェノ,ールエーテル
型、ポリオキシエチレンアルキルエステル型、ソルビタ
ンアルキルエステル型、ポリオキシエチレンアルキルア
マイド型のような非イオン界面活性剤、あるいは慣用の
カチオン、アニオン界面活性剤が採用される。As the emulsifier, nonionic surfactants such as polyoxyethylene alkyl ether type, polyoxyethylene alkylphenol ether type, polyoxyethylene alkyl ester type, sorbitan alkyl ester type, polyoxyethylene alkyl amide type, or conventional surfactants can be used. Cationic and anionic surfactants are employed.
j乳化剤の種類により例えはFLB3
.5〜6の油溶性乳化剤を使用した場合には油中水型エ
マルジョンを形成し、FII,B8〜18の水溶性乳化
剤を使用した場合には水中油型エマルジョンを形成する
。乳化剤濃度は通常0.0】〜5%である。
3これらの方法はアクリルアミドと他の単量体を共重
合させる場合にも適用される。しかして、本発明はかか
るアクリルアミドの水性媒体中での重合を重合性の不飽
和結合を含まない有機スルホン酸塩の存在下で行なうも
のであ4イる。jDepending on the type of emulsifier, for example, FLB3
.. When oil-soluble emulsifiers 5 to 6 are used, a water-in-oil emulsion is formed, and when water-soluble emulsifiers FII, B8 to 18 are used, an oil-in-water emulsion is formed. The emulsifier concentration is usually between 0.0 and 5%.
3 These methods are also applied when copolymerizing acrylamide with other monomers. Therefore, in the present invention, the polymerization of acrylamide in an aqueous medium is carried out in the presence of an organic sulfonate containing no polymerizable unsaturated bonds.
重合性の不飽和結合を含まない有機スルホン酸塩として
は、一価あるいは多価の飽和脂肪族スルホン酸、脂環族
スルホン酸、芳香族スルホン酸、複素環式スルホン酸等
の酸と、水酸化ナトリウム、水酸化ウリウム、水酸化リ
チウム、水酸化カルシウム、水酸化マグネシウム、水酸
化アンモニウム等の無機塩基あるいはトリメチルアミン
、ジダメチルアミン等の有機塩基との塩が挙げられる。Examples of organic sulfonic acid salts that do not contain polymerizable unsaturated bonds include acids such as monovalent or polyvalent saturated aliphatic sulfonic acids, alicyclic sulfonic acids, aromatic sulfonic acids, and heterocyclic sulfonic acids; Examples include salts with inorganic bases such as sodium oxide, urium hydroxide, lithium hydroxide, calcium hydroxide, magnesium hydroxide, ammonium hydroxide, and organic bases such as trimethylamine and didamethylamine.
より具体的にはベンゼンスルホン酸ソーダ、トルエンス
ルホン酸ソーダ、メタンスルホン酸ソーダ、エタンスル
ホン酸ソーダ、あるいはこれらに対する他の塩基との塩
等が挙げられる。O 工業的には入手及び取扱いの容易
さ、あるいは環境汚染の観点から上記スルホン酸と水酸
化ナトリウムの塩がよく採用される。More specific examples include sodium benzenesulfonate, sodium toluenesulfonate, sodium methanesulfonate, sodium ethanesulfonate, and salts thereof with other bases. O Industrially, the above-mentioned salts of sulfonic acid and sodium hydroxide are often employed from the viewpoint of ease of acquisition and handling, or from the viewpoint of environmental pollution.
本発明方法では有機スルホン酸塩は、通常アクリルアミ
ドに対して0.05〜5師量%、好ましくは70.1〜
1鍾量%使用される。In the method of the present invention, the amount of organic sulfonate is usually 0.05 to 5%, preferably 70.1 to 5% based on acrylamide.
1% by weight is used.
有機スルホン酸塩の添加時期はとくに制限されず、重合
直前でも重合途中でもよい。The timing of addition of the organic sulfonate is not particularly limited, and may be added immediately before or during polymerization.
また、予めアクリルアミド水溶液に塩を添加しておいて
もよい。更に、予じめアクリルアミド水溶液を前記した
ような有機、無機の塩基で処理しておき、重合の際に有
機スルホン酸で中和して得られる塩の存在によつてを本
発明は達成される。Alternatively, a salt may be added to the acrylamide aqueous solution in advance. Furthermore, the present invention is achieved by the presence of a salt obtained by treating an aqueous acrylamide solution in advance with an organic or inorganic base as described above and neutralizing it with an organic sulfonic acid during polymerization. .
かくして得られる重合体は、通常メタノール、アセトン
等の水溶性溶媒中で沈澱脱水するか、あるいは共沸蒸留
により脱水した後種々の用途に付される。The polymer thus obtained is usually dehydrated by precipitation in a water-soluble solvent such as methanol or acetone, or dehydrated by azeotropic distillation, and then subjected to various uses.
本発明方法で得られるアクリルアミド系重合体は溶解性
および凝集能が共に優れており、凝集剤、特にバルブ廃
水の処理に優れた効果を示すものである。The acrylamide polymer obtained by the method of the present invention has excellent solubility and flocculating ability, and exhibits excellent effects as a flocculant, particularly in treating valve wastewater.
次に実施例により本発明を更に詳細に説明するが、本発
明はその要旨を超えない限り以下の実施例により制約さ
れるものではない。Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to the following Examples unless the gist thereof is exceeded.
実施例1
銅含有触媒の存在下、アクリロニトリルを接触水和して
得られたアクリルアミド水溶液(アクリルアミド濃度5
呼量%)を125y採取し、ベンゼンスルホン酸ソーダ
を0.32y添加后脱塩水を迫加し、500y水溶液と
する。Example 1 Acrylamide aqueous solution obtained by catalytic hydration of acrylonitrile in the presence of a copper-containing catalyst (acrylamide concentration 5
%) was collected for 125y, and after adding 0.32y of sodium benzenesulfonate, demineralized water was added to make a 500y aqueous solution.
このアクリルアミド水容液を700mLの内容積を持つ
セパラブルフラスコこ移し、25℃水浴中で30分間N
2ガスを吹き込み、過硫酸アンモニウムの1重量%水溶
液3.1mtを加える。過硫酸アンモニウムを添加後、
水浴の温度を1分間に1゜Cの速度で50℃迄昇温する
。This acrylamide aqueous solution was transferred to a separable flask with an internal volume of 700 mL, and N
2 gas was blown into the flask, and 3.1 mt of a 1% by weight aqueous solution of ammonium persulfate was added. After adding ammonium persulfate,
The temperature of the water bath is raised to 50°C at a rate of 1°C per minute.
昇温途中で重合が開始される。浴温50℃で1時間保持
し、次いで浴温を60℃に前記と同一の昇温速度で昇温
し、60゜Cに2時間保.持した後、フラスコを浴槽か
ら取りだし水冷する。Polymerization starts during the temperature rise. The bath temperature was maintained at 50°C for 1 hour, then the bath temperature was raised to 60°C at the same rate of increase as above, and maintained at 60°C for 2 hours. After holding the flask, remove it from the bathtub and cool it with water.
かくして得られたポリマーの一部を取りだしメタノール
に懸濁せしめて水分を除く。A portion of the polymer thus obtained is taken out and suspended in methanol to remove water.
白色の粉状になつたポリマーを減圧乾燥したのノちそれ
らを更に粉砕した。The white powdered polymers were dried under reduced pressure and then ground further.
かくして得られたポリマーの性能を次の項目について比
較した。The performance of the polymer thus obtained was compared with respect to the following items.
溶解性: ビーカーに乾燥したポリマー0.2qを
とり、これに200T111の水を加え、4時間 攪
拌した後の溶解性を比較する。Solubility: Add 0.2q of dry polymer to a beaker.
200T111 water was added to this, and the solubility after stirring for 4 hours was compared.
0: ゲル状ポリマーの小塊が残在浮遊して いる。0: Small lumps of gel-like polymer remain floating.
×: ゲル状ポリマーの塊が多量に残つた。凝集能:
クラフトバルブ廃水に硫酸バンド 400ppmを加え
、PH6てポリアクリルア ミド1ppm相当を添加
して、ジヤーテス ターで常法により凝集させ、この
とき生 成するフロックの大きさにより判定し た
。×: A large amount of gel-like polymer lumps remained. Aggregation ability:
400 ppm of sulfuric acid was added to Kraft valve wastewater, and the equivalent of 1 ppm of polyacrylamide at pH 6 was added, and flocculation was performed using a jar tester using a conventional method. Judgments were made based on the size of the flocs produced.
O印:直径 3〜4?
Δ印:直径 1〜3TFrIn
×印:直径 17m未満
種々の有機スルホン酸塩を用いて同様に重合、得られた
ポリマーの性能を試験した。O mark: Diameter 3-4? Δ mark: Diameter 1 to 3 TFrIn × mark: Diameter less than 17 m Various organic sulfonate salts were similarly polymerized and the performance of the obtained polymers was tested.
Claims (1)
共重合し得る単量体を水性媒体中で重合する際に、重合
性不飽和結合を含まない有機スルホン酸塩を存在させる
ことを特徴とする水溶性アクリルアミド系重合体の製造
方法。1. A water-soluble acrylamide polymer characterized by the presence of an organic sulfonate containing no polymerizable unsaturated bonds when acrylamide or acrylamide and a monomer capable of copolymerizing it are polymerized in an aqueous medium. manufacturing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12309775A JPS6050809B2 (en) | 1975-10-13 | 1975-10-13 | Method for producing acrylamide polymer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12309775A JPS6050809B2 (en) | 1975-10-13 | 1975-10-13 | Method for producing acrylamide polymer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5247085A JPS5247085A (en) | 1977-04-14 |
| JPS6050809B2 true JPS6050809B2 (en) | 1985-11-11 |
Family
ID=14852119
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12309775A Expired JPS6050809B2 (en) | 1975-10-13 | 1975-10-13 | Method for producing acrylamide polymer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6050809B2 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS53125492A (en) * | 1977-04-11 | 1978-11-01 | Toagosei Chem Ind Co Ltd | Preparation of acrylamide polymer |
| JPS6036891A (en) * | 1983-08-05 | 1985-02-26 | Tlv Co Ltd | Exhaust device for steam heater |
| US5178774A (en) * | 1990-06-29 | 1993-01-12 | Allied Colloids Limited | Purification of aqueous liquor |
| US5698109A (en) * | 1990-06-29 | 1997-12-16 | Allied Colloids Limited | Purification of aqueous liquor |
| US5112500A (en) * | 1990-06-29 | 1992-05-12 | Allied Colloids Limited | Purification of aqueous liquor |
-
1975
- 1975-10-13 JP JP12309775A patent/JPS6050809B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5247085A (en) | 1977-04-14 |
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