![]() Method of producing cation polymeric adsorbent
专利摘要:
METHOD FOR CATIONIC POLYMER ADSORBENT by reacting the condensation product of formaldehyde with urea or melamine with a compound containing an amide group at 60-90 C, characterized in that, to obtain an adsorbent with a high adsorption capacity, as a condensation product of formaldehyde with urea or melamine is used amino group-free amino precondensate selected from the group consisting of N-methylol urea, N, N-dimethylol urea, dimethyl ester Y, N-dimethylol urea, N, N-dim tilolthiourea, N, N-dimethylol-5-oxypropylene urea dimethyl ester and hexamethylolmelamine, and as the compound containing amide groups, the amino compound of the formula CH3 — SH-1-H-C — X, OT-4II-I, CH4 –4-CH 4CH, CH4 -CH, OT-4II-I-4 R 1 NQ-lH-C-lSI-X Cl R: I it IV 0 Y where R is methyl, ethyl or the group CO -CH2 -NH-CO-NII-CH, j, OH; Rj is methyl or ethyl, or R and RJ together with the nitrogen atom that joins them is a pyrrolidino, piperidino, morpholino, or N-methyl piperazino group; 00 V is methyl; Q is ethylene or propylene, X and Y alone, independently of the other, hydrogen or, SP, and the reaction is carried out in an aqueous medium in the presence of sulfamic acid at pH 4.5-7 and the molar ratio of the amino pre-condensate layer and the amino compound or quaternary ammonium salt 公开号:SU1181552A3 申请号:SU813394405 申请日:1981-10-27 公开日:1985-09-23 发明作者:Хаазе Ярослав;Пальмберг Рогер 申请人:Циба-Гейги Аг (Фирма); IPC主号:
专利说明:
I This invention relates to the field of polymer adsorbents,; used to remove anionic from aqueous solutions, especially from wastewater, for example, filtrates, residual baths from bleaching processes, or dyeing from drains after rinsing and washing. The purpose of the invention is to obtain an adsorbent with a high adsorption capacity. Example 1.51.7 g of a 40% solution of the compound of the formula SI. 3 N-CH2-CH2-CH -NH-CO-NH-CH20H CH pH = 4.6, adjusted using concentrated HCt, mixed with 26.4 g of N, N-dimethylolurea and heated to. The molar ratio of the starting materials was 1: 1.8. To this mixture was added 10 ml of 15% sulfamic acid, and the reaction mixture solidified. Then the mixture is heated for 1.5 hours under reflux, the reaction mixture is drunk on a drying sheet and further condensed in a vacuum oven at 8590 0. After 15 hours, 41.5 g of a light yellow vitreous product is obtained, which is crushed and absorbed 2000 ml. water. After 30 minutes of stirring at room temperature, filtration is performed through a filter cloth and the product is dried in a vacuum oven for 16 hours. 20.0 g of a slightly yellow powder with a nitrogen content of 25.3% is obtained, Examples 2-6. Proceed as described in Example 1, but instead of the indicated reaction components are used, respectively, listed in the second and third columns of the table. 1 raw materials in the specified amount x at pH 7. Nitrogen content with 500 mg made according to examples 1-18 anion exchange resin in the form 15522 The reaction products and the molar ratio of the starting components are listed in the fourth and fifth columns, respectively. 5Example 7. 27.5g of compound formulas . (CHp. N- (CH2) 3-NH-CO-N (CH20H) s, / Cl dissolved in 30 ml of water and adjusted to pH 4.5 with concentrated hydrochloric acid. 26.4 g of N, N-dimethylolurea are added to it and heated to 60 ° C. To this mixture, 10 ml of 15% sulfamic acid is added, and a fine suspension is formed, transparent as a glass. The molar ratio of the starting materials is 1: 2. Then it is heated for 1.5 hours to 80-85 ° C, the reaction mixture is poured onto the drying sheet and further condensed in a vacuum drying cabinet at 85-90 ° C. After 15 hours, 1500 ml of water is obtained and absorbed. After 30 minutes of stirring at room temperature, filtration is performed through a filter cloth and the product is dried in a vacuum oven for 15 hours at 85-90 ° C. Get 23.0 g of a white powder with a nitrogen content of 22.9%. Example 8. Proceed as described in Example 7, but used. instead of the indicated reaction components, respectively, the starting materials listed in the second and third columns of Table 2 are in the indicated amounts at pH 7. The nitrogen content in the reaction products and the molar ratio of the starting components are given in the fourth and fifth columns, respectively. Examples 9-36. In a three-necked flask with a magnetic stirrer, a cooler and a thermometer, the mixture is mixed at 50 ° C 500 MJi to a pH of 7 with a 0.1% aqueous solution of the dye of the formula N OzKa powder. At each experiment, after the duration of the adsorption, the x min suspension of the penzy is filtered through a storage filter and determined in Table 1 11815524 tab. 3 percent security. Filtrate. 19.8 Monomethylol-51.7 (CH), N- (CHj), urea-W-CO-W-CH-W Hexametshhol-51,7 Same melamine H, n-dimethylol-75.0 (CHj) j H- (CHA.urea-NH-CO-N (CH, CW), Ionometkol-75,0 The same urea Hexamethylol 75.0 Same Mepamin Table 3 1181552 8 Continuation of table 3
权利要求:
Claims (1) [1] METHOD FOR CATIONIC POLYMER ADSORBENT by reacting the condensation product of formaldehyde with urea or melamine with a compound containing an amide group at 60-90 C e, characterized in that, in order to obtain an adsorbent with a high adsorption capacity, as a condensation product of formaldehyde with urea or melamine an amino group-free precondensate of an aminoplast selected from the group consisting of N-methylolurea, Ν, Ν'-dimethylolurea, dimethyl ether Ν, Ν * -dimethylolurea, Ν, Ν'-dimetre is used loltiomochevinu, dimethyl ether, Ν, Ν-1 -dimetilol 5 oksapropilenmocheviny and hexamethylol melamine, and as a compound comprising a first amide group, an amine compound of formula CH 3 & Ύ or a quaternary ammonium salt of the general formula where R A is methyl, ethyl or a group -CH ^ -NH-CO-NH-CH ^ OH; R 2 is methyl or ethyl, or R 3 and R 2 together with the nitrogen atom connecting them are pyrrolidino, piperidino, morpholino or N-methylpiperazino; V is methyl; Q is ethylene or propylene, X and Y independently of one another - hydrogen or -CH z OH, wherein the reaction is carried out in an aqueous medium in the presence of sulfamic acid at pH 4,5-7 and 1 molar ratio of SG aminoplast precondensate and amine compound or a quaternary ammonium salt (1,5- 3.5): 1; SU <„> 1181552
类似技术:
公开号 | 公开日 | 专利标题 US4178438A|1979-12-11|Cationically modified, cellulose-containing materials US4439203A|1984-03-27|Process for improving the wetfastness of dyeings, printings and optical brightenings on cellulosic substrates and compositions useful therefor SU1181552A3|1985-09-23|Method of producing cation polymeric adsorbent US5659011A|1997-08-19|Agents having high nitrogen content and high cationic charge based on dicyanimide dicyandiamide or guanidine and inorganic ammonium salts CA1169204A|1984-06-19|Color salt US3979285A|1976-09-07|Process for the purification of industrial effluents US4439208A|1984-03-27|Method for improving the fastness of dyeings with basic dyes on cellulosic substrates US4511707A|1985-04-16|Water-soluble precondensates useful for improving the fastness of dyes and optical brighteners on hydroxy group-containing substrates GB2115422A|1983-09-07|A polymeric polydonor complexon and the method for preparation thereof US4407976A|1983-10-04|Anionic adsorbent FI67087B|1984-09-28|KATJONISKT ADSORPTIONSMEDEL FOERFARANDE FOER DESS FRAMSTAELLNING OCH DESS ANVAENDNING FOER ATT AVLAEGSNA ANJONISKA AEMNEN FRAON VATTENHALTIGA LOESNINGAR US4306080A|1981-12-15|Process for the purification of industrial effluents CA1125931A|1982-06-15|Process for removing cationic substances fromaqueous solutions US4484927A|1984-11-27|Polymers useful for improving the fastness of dyes and optical brighteners on hydroxy group-containing substrates EP0038299B1|1984-11-14|Cationic compounds CA1091866A|1980-12-23|Process for dyeing textile material US4297296A|1981-10-27|Quaternized polyamines US4758671A|1988-07-19|Water-soluble cation-active polyelectrolytes EP0145656B1|1989-12-13|Cationic compounds JP3860220B2|2006-12-20|New condensation products and their uses JP2006518776A|2006-08-17|Polymer ether amines, their production and use RU1768599C|1992-10-15|Method of flocculant preparation for clarification of high-hydrophilic hard precipitated clay hydrosuspensions SU1692946A1|1991-11-23|Method of neutralization of dye plant sewage CH612201A5|1979-07-13|Process for the preparation of cationically modified cellulose materials
同族专利:
公开号 | 公开日 FI70676B|1986-06-26| DE3170329D1|1985-06-05| ES506596A0|1983-02-01| DK473381A|1982-04-29| CA1191992A|1985-08-13| BR8106927A|1982-07-13| JPH0248295B2|1990-10-24| AT13063T|1985-05-15| FI813350L|1982-04-29| EP0051044A3|1982-08-04| US4478724A|1984-10-23| US4424284A|1984-01-03| DE3142153A1|1982-05-27| IL64112A|1984-09-30| EP0051044B1|1985-05-02| ZA817428B|1982-09-29| IL64112D0|1982-01-31| ES8302741A1|1983-02-01| EP0051044A2|1982-05-05| FI70676C|1986-10-06| JPS57102231A|1982-06-25|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 DE4110736A1|1991-04-03|1992-10-08|Rotta Innovations Gmbh Dr|Heat degradable polymer particles used in water treatment - comprising amino resin matrix with immobilised functional polymer|GB497042A|1937-06-11|1938-12-12|Henry Alfred Piggott|New urea derivatives| GB497043A|1937-06-11|1938-12-12|Henry Alfred Piggott|New quaternary ammonium compounds| GB497485A|1937-06-17|1938-12-19|Reginald John William Reynolds|Manufacture of substituted acid amides| GB497368A|1937-06-18|1938-12-19|Henry Alfred Piggott|New nitrogen-containing organic compounds| US2203492A|1937-06-30|1940-06-04|Ici Ltd|Dyed cellulosic material| US2203493A|1937-06-30|1940-06-04|Ici Ltd|Treatment of cellulosic material| US2367455A|1941-04-09|1945-01-16|Rohm & Haas|Aminocyanoacetamide resins| US2698787A|1951-12-17|1955-01-04|American Cyanamid Co|Urea-formaldehyde resins for wet strength paper and their use| US2901391A|1954-06-15|1959-08-25|American Cyanamid Co|Modified urea-formaldehyde resins and paper containing the same| US3189646A|1962-04-26|1965-06-15|Coastal Interchemical Company|Process for the preparation of n-methylol amide derivatives| US3252898A|1962-09-27|1966-05-24|Johns Manville|Removal of soluble anionic materials from water| GB1360648A|1970-12-23|1974-07-17|Nippon Soda Co|Method of adsorbing heavy metals and compounds of heavy metals| US4104160A|1972-05-10|1978-08-01|Ciba-Geigy Corporation|Process for the purification of industrial effluents| US4207184A|1975-06-17|1980-06-10|Ciba-Geigy Ag|Process for the purification of industrial effluents| US4178438A|1975-11-14|1979-12-11|Ciba-Geigy Aktiengesellschaft|Cationically modified, cellulose-containing materials| DE2650967A1|1975-11-21|1977-06-02|Ciba Geigy Ag|METHOD OF COLORING TEXTILE MATERIAL| US4316005A|1979-06-28|1982-02-16|Ciba-Geigy Corporation|Cationic adsorption agent| US4424284A|1980-10-28|1984-01-03|Ciga-Geigy Corporation|Cationic adsorption agent|US4424284A|1980-10-28|1984-01-03|Ciga-Geigy Corporation|Cationic adsorption agent| ES2021090B3|1986-07-31|1991-10-16|Ciba-Geigy Ag|CATIONIC DECOMPOSITION PRODUCTS OF BASIC CARBAMIDES AND EPIHALOGENHYDRINES.| RU2034788C1|1990-12-28|1995-05-10|Совместное советско-западногерманское предприятие "Аква Ремонт"|Method of water treatment from organic compounds| US5169878A|1991-04-08|1992-12-08|The Dow Chemical Company|Composition and method of preparation of viscosity-stabilized polyisocyanates comprising triazine groups| JPH0723593U|1993-10-06|1995-05-02|武盛 豊永|Felt-tip pen with pencil| DE19638594A1|1996-09-20|1998-03-26|Basf Ag|Process for the purification of wastewater and circulating water in papermaking, deinking and pulp bleaching|
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申请号 | 申请日 | 专利标题 CH801680|1980-10-28| 相关专利
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