• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Die Erfindung betrifft neue Anionenaustauscher auf Basis vernetzter N-alkylierter Polyacryl- oder Polymethacrylamide; diese neuen Anionenaustauscher enthalten sowohl schwach basische als auch quartäre Ammoniumgruppen. Die Erfindung betrifft ferner ein Verfahren zur Herstellung dieser neuen Anionenaustauscher und deren Verwendung zur Adsorption schwacher Säuren.
    公开号:SU1055335A3
    申请号:SU813229053
    申请日:1981-01-16
    公开日:1983-11-15
    发明作者:Геллер Гарольд；Ланге Петер-Михаель；Мартинола Фридрих
    申请人:Байер Аг (Фирма)；
    IPC主号:
    专利说明:

    ate
    co: s;: l 11 The invention relates to anion exchangers, in particular, to the process of populating anion exchangers containing amide groups. Known ways & 1 Iopucheni anionitov by processing of copopimers of acripate and au-vinipbenzopa (DVB) diamines l. The closest to the proposed technical solution is the method of obtaining anion exchangers of the interaction path of a crosslinked ester of papy (meth-) acrylic acid with a polyamine containing at least one primary amino group, followed by 94, .4% of the amino groups of the resulting N-amino-apylated poly ( meth) acrylamide into groups of quaternary ammonium bases by alkylation 2. A disadvantage of the known method is that the anion exchangers obtained are characterized by a low exchange capacity and their regeneration A large amount of alkali regenerating agent is banging. The purpose of the invention is to increase the exchange capacity of the anion exchanger and lower than tme pa of the regenerating agent. This goal is achieved by heme according to the method of producing anionwat 5 by reacting an apkyl (meth) acrylate copolymer, in which the alkyl has a composition, and a crosslinking agent with a polyalkylenepolyamine and subsequent alkylation of the copolymer amino groups with an apkyl chloride composition. Cj-C or xrtophethiol, alkylation is subjected to O8O mol% of amino groups and a poly amine selected from the group consisting of N, N-methigropylenediamine -1,3, H, N-diethylpropylene diamine-1,3, diethylenetriamine, N, is used as polyapkylene polyamine. N-diethylethylenediamine and tetraethylenepentamine. Examples 1-5. YuOO ml of weakly basic anionwave (content of tert-amino groups is 1.69 mp / l) are placed in 1 l of completely demineralized water. After adding an equimoprine amount of caustic soda (in terms of the methylchloride used) to the samples of the ionig, the methyl chloride is introduced into the suspension at room temperature. The reaction mixture is then acidified to pH ' 2 by addition of hydrochloric acid. Thus, the anion exchangers are completely converted into salt. After separation from the reaction solution, the anion exchanger is washed with 5 p of completely desalted water in a filter tube. Table
    Continued table. 1 310 In tab. 1 pripedig used cp otdelnyh initial mixtures the number of metihporida, the time of getting metihporida amount of caustic soda, the output of atgonite, full exchange capacity (OU) in mmop / mp ionite, the content of synovnOOBHbix groups in mmop / mp and in% of ion exchanger; equal to the degree of transfer of the amino groups to the quaternary ammonium base groups), as well as the change in volume in percent during regeneration by 5% sodium hydroxide loaded with ionic acid. Spasobactile anion exchange resin is obtained in the following manner. In a mixture of 4O07 g methyl acrylate, 358 g of technical DVB {pure DVB content 62.8 wt.% ,. residual ethylstyrop) and 138. g of 1.7 octadiene dissolve 225 g of isodocecan and 30 g of 75% benzoyl peroxide. Then it is stirred, the mixture is fed into an aqueous solution of 6.75 g of methylidellose and 0.225 g of sodium nitrite in 45OO g of water and is first first subjected to polymerization at 65 ° C for 5 hours, and then at 9 ° C for 2 hours. 4297 g of dry is obtained granulated polymer with a grain diameter OD g, 1.0 mm. 250 g of the obtained polymer and 1200 N, N-Dimethylpropylene diamine-1.3 are heated to 195-2OO ° C for 5 hours. The C5 formed macroporous, weakly basic anion exchange resin is then expelled from the amine and washed with a neutral reaction with completely salted water in a filter tube . Yield: 1250 ml of anion exchanger, the contents of spabo-basins; 1.69 mmop / p. Example 6.1l of a gelatinous, weakly basic anion exchanger (the content of tertiary amino groups is 1.88 mol / l) obtained by aminolysis of 120O g of N. N-aimethylpropylene diamine-1, 3, 25O g of ethyl acetate polymer, 5% DVB and 3% 1,2,4 -trivinyl dichexane, is reacted with 38 g of methyl chloride in the manner described. Output: 1.22 liters of anion exchange resin; the content of strongly basic groups is 0.54 mmol / ml of 33% OEK; content of weakly basic, groups 1,09 mmol / ml; no change in volume during regeneration with sodium liquor. Example 7. 1 l of macroporous, spabic-base anion exchanger (content of tertiary amino groups 1.35 mol / l), obtained by aminolysis 1500 g diethyl 35 propnyl trans-shsm-1,3, 250 g half a night before methyl acrylate, obtained from 20O1 g methypacrylate, 181.5 g technical DVB (DVB content 62.1%) and 67.5 g of (1.5) -hexadiene- (1.5) in the presence of 450 g of isododecane are reacted with 36.6 g of ethyl chloride in the manner described. Output: 1.3 l of anion exchange resin, the content of strongly basic groups is 0.39 mmol / ml 35% OEK; the content of weakly basic groups is 0.72 mmop / ml, the increase in volume during regeneration with caustic soda 2%. Example 8. 1 l of macroporous, weakly basic anion exchanger (content of tertiary amino groups 1.85 mol / l) obtained by aminolysis 12OO g N, N -dimethylpropylene diamine-1,3, 25 O g of methyl acrylate polymer obtained from 3890 g methyl acrylate and 610 g technical DVB (DVB content 59%) in the presence of 45O g of lacquer gasoline, suspended in 1 liter of completely demineralized water and after adding 30 g of NQOH (as a 45% aqueous solution) react with 37.5 g of anag methyl chloride. OK for examples 1-5. Output: 1.22 O l of anion exchange resin; the content of strongly basic groups is 0.5 mmol / ml of 33% OU; the content of weakly basic groups is 1.0 mmol / ml; increase in volume during regeneration with caustic soda 1%. Example 9. 21O ml of macroporous, spabic-base anion exchanger (content of tertiary amino groups 1.76 mp / l) obtained by aminolysis of 415 g of N, N-dimethylpropipenediamine-1, 3 with 86 g of polymer obtained from 889.5 g for 10 hours of methipmethacrylate, 8O, 5 g of technical DVB (DVB content 62%) and 30 g of octadiene-1.7 in the presence of 10O g of isododecane, are suspended in 2OO ml of fully non-absorbed water and reacted with 2O g of methyl chloride for 2 oh. Recycling wire t analop Cho examples 1-5. Output: 315 ml of anion exchange resin; content of basal groups, 0.32 m top / ml ZO% OU; the content of weakly basic groups is 0.74 mmol / ml; an increase in volume during regeneration with caustic soda 2%. Example 1O. 74O ml of macroporous, weakly basic anion exchanger (companion of tertiary amino groups 1.56 mol / l) obtained by aminolysis 250 g of polymer obtained from 713 g of butyl acrylate, 62.7 g of technical DVB (DVB content 63.3%) w 24 g of octaiea -1 , 7 in pumaissia 40 g of isodeicane, with 120O g of N, N-dimethylpropylene diamine-1, 3 according to examples 1-5, are suspended in 7OO MP Hobessopen water and after the addition of 46 g of water | Interaction with 58 g of megiphlord for 16 h at 40 s. Recycled anapogic examples 1 Exit: 1080 MP anion exchange resin, the content of the cinemate groups 0.8 mmop / MP 8O% OU; content of saabo-base grztl 0.2 mmop / mp; increase in the volume of regeneration by caustic soda 1O%. Example 11, 10O ml of macroporotic, weakly basic anion exchanger (containing tertiary amino groups, 2 mp / polueneyo by an amino acid 25Og described in macroporous schralers 1–5, 1g of mepacrylate with samples of 1314 g diethylphenol according to examples 1–5, d, 1% of the polymethacrylate with samples of 1314 g of diethylpolymer of 5–5 macroporous, 1-byg of mepacrylate with samples of 1314 g of diethylphenol containing 1–5 of diethylphenol containing 1–5 of diethylphenol containing 1–5 of diethylphenol, 1-by-5 pp, 1 byp of metipacrypate, 15 pg of diethylpolymer, 5–10 pp, and 4–1 pp of 1–5 mpp of 1pc of the polymethylphenol containing 314 g of pyloric acid, 25%. After the addition of 35 g of NdOII (as a 45% aqueous solution), it is reacted with 140 g of propylporide for 2 hours at 40 ° C. Anapogic is processed 1fimvram 1-5. Output: 122 MP anioniga; the content of sipyyosiovny groups about, 6 mmop / mp "25% of OEK; content of weakly basic groups is 1.8 mmop / ml; Increasing the volume during regeneration with caustic soda 1%. Example 12 1OO ml of macroporous, weakly basic anioite (content of tertiary amino groups 4.1 mol / l obtained by aminopoly 2OO g, similar to npiiMepaM 1-5 of macroporous polimer methyl acrylate ether of acrylic kilo with 189O g of tetraethylene pentamine, It is suspended in 150 ml of completely desalted water after adding 200 g of No OH (as a 45% aqueous solution) and subjected to reaction with 20 g of methyl chloride over 16 hours. Recycled as in Examples 1-5. High pressure: 115 ml of ion-exchange resin ; the content of strong-base groups of 1.3 mm ü / mp "38% of OU; content of weakly pears: 2.1 mmop / mp; an increase in the volume of 2% with regenerated sodium hydroxide. Example 13. 1OO ml of macroporos of spabic anioiite (2.7 mol / l contain tertiary amino groups), about 250 g of macroporous popime {methyacacrylate with 1450 g of N, N die1 {shetiamine in paragraphs 1-5 of macroporous {pimeter {a metiacacrylate) according to examples 1-5 are suspended in 150 ml of fully water and reacted with 5.3 g of 2-chloro ethanol for 10 hours at 5 ° C. At the same time, the pH value of the suspension is slowly increased from 6 to 10 by adding dilute caustic soda solution. It is processed as in Examples 1-5. Output: 138 ML; the content of cuHbHoocHOBHbix groups of 0.27 mmol / mp of OU; the content of weakly labeled groups of 1.2 mmol / ml; volume reduction during regeneration with caustic soda 3%. 1 l of anion exchangers of examples 1-13 of anion exchanger according to the method of the prototype is loaded into a filter tube (inner diameter 55 mm), through which 2O p / h of leached and degassed water is passed through to flashing silicon button (0.1 ml / l 5402 at the filter discharge) and then subjected to countercurrent regeneration of 40 g of No OH in the form of a 4% aqueous solution at 20 ° C under a load of 2 l / h. Composition of water Strong acids (total), mmol / l 7 Weak acids (total), i mmol / l 0.5 Cream per acid (as S (02), mg / l 7 Table 2 shows the dynamic o (f The capacity of the anion exchangers and the amount of the means for regeneration in mol.% DOE. These data are the average of three data: experiments. Table 2, Table 2, 2, Table 2 shows that DOE anion exchangers According to the invention, the consumption of anion exchangers according to the invention is lower, and the consumption of anion exchangers according to the prototype method is lower.
    iso7, 0
    93 7.9
    69
    Oh oh
    proto 2% sodium hydroxide solution is used, as silicic acid drops out.
    B-tab. 3 shows the data for DOEC as it is from table. 3, DOE
    anion exchangers and consumption of the regeneration agent, the annonig according to the invention, in which they represent the mean values of all cases are greater than the number of three experiments of the anion exchanger. 5 10.
    7 0.95
    105 31 0,8 125 137 100 O, 73 It is investigated its repeated regeneration of the obtained anion exchangers. Dp this in the above-described time x 1 n of the anion exchange resin of example 3 and the known anion exchange resin is repeatedly loaded and regenerated countercurrently. In this case, water of the following quality is used: spilled and degassed water containing 7 mop.%, In terms of the total content of strong and strong acids, acid ions 1 + silicic acid (test 1); leached water containing 31 mol.% in terms of the total content of weak and strong acids, carbonic acid and silicic acid (experiment 2); demineralized water containing 1.OO mol% weak acids (experiment 3). .Table
    权利要求:
    Claims (1)
    [1]
    METHOD FOR PRODUCING ANIONITE by reacting an apkip / meth / acrylate copolymer in which the apkip has a C ^ -Cd composition and a crosslinking agent with popiapipenpopiamine and subsequent alkylation of the amino groups of the copolymer with an apkipporide of a C ^ -C ^ ippore ethanopolymer, characterized in that with the dynamic exchange capacity of the anion exchange resin and reducing the consumption of the regenerating agent, 1,080 mole% of amino groups are subjected to alkylation and a polyamine selected from the group consisting of NN-dimethylpropylene diamine-1 is used as popiapipenepopiamine, 3, N, N cetippropiene diamine-1,3, diethipentriamine, N. N-dietepetipendiamine and tetraethyl npentamine.
    SP
    类似技术:
    公开号 | 公开日 | 专利标题
    KR910008292B1|1991-10-12|Gel type chelate resin and method of removing polyhydric alkali earth or heavy metal cation from solution
    EP1734033B1|2014-11-12|Method of purifying amino acid
    US6646083B2|2003-11-11|Crosslinked polymers containing tertiary amine and/or quaternary ammonium salt structures, processes for making and uses thereof
    US7265159B2|2007-09-04|Monodisperse anion exchangers
    SU1055335A3|1983-11-15|Process for preparing anionite
    DE4004953C2|1992-10-15|
    CA1048692A|1979-02-13|Method for preparation of ion exchangers by alkylation and hydroxyalkylation of polymeric hydrophylic anion exchangers
    EP0532894B1|1994-10-05|Weakly basic anion exchange resins, process for their preparation by aminolysis and use for removing sulfates ions from acqueous solutions
    US4177140A|1979-12-04|Method for removing a weak acid from an aqueous solution
    JPH08503015A|1996-04-02|Slightly swellable insoluble polymer with amino groups, process for its production and its use
    GB2207140A|1989-01-25|Process for production of highly water-absorbent resin
    DE3324835A1|1985-01-17|CROSSLINKED COPOLYMER, PROCESS FOR PRODUCING IT AND ITS USE AS SORPENT
    US3808158A|1974-04-30|Amphoteric thermally regenerable ion exchange resins
    EP0213719B1|1991-01-09|Low-rinse, high-capacity, weakly basic acrylic ion exchange resins process for preparing them, and their use in removing anions from a liquid
    US4115297A|1978-09-19|Thermally regenerable amphoteric ion exchangers prepared by sequential treatment of polymeric beads with two reagents of opposing acid base character
    EP0722361B1|1998-05-06|Epoxy derivatives of polyacrylic amides
    WO1989005828A1|1989-06-29|Compounds
    JP3505735B2|2004-03-15|Decolorization method
    SU622820A1|1978-09-05|Method of obtaining ionites
    GB2059952A|1981-04-29|Purifying aqueous acrylamide solutions
    WO2010041274A2|2010-04-15|Process for the preparation of carbonate salts of cross-linked amine polymers
    JPH10277404A|1998-10-20|Production of strong basic anionic exchanger using ethylene oxide
    JPH0662699B2|1994-08-17|Method for producing chelating multidentate ligand resin
    JP2000007727A|2000-01-11|Purification of ionic polymer compound
    JPH06122728A|1994-05-06|Basic anion-exchange resin and its production
    同族专利:
    公开号 | 公开日
    DD156978A5|1982-10-06|
    AU6630281A|1981-07-30|
    EP0032671A2|1981-07-29|
    EP0032671B1|1982-12-22|
    BR8100236A|1981-08-04|
    IL61921D0|1981-02-27|
    ES8200909A1|1981-11-16|
    DE3160015D1|1983-01-27|
    EP0032671A3|1981-10-14|
    ZA81286B|1982-02-24|
    DE3001856A1|1981-07-23|
    ES498587A0|1981-11-16|
    JPS56105758A|1981-08-22|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    NL81827C|1952-04-14|
    NL207888A|1952-06-06|
    US2862894A|1956-11-28|1958-12-02|Rohm & Haas|Preparation of anion-exchange resins containing weakly basic and strongly basic functional groups|
    US3051651A|1959-02-12|1962-08-28|Bayer Ag|Method of removing oxygen dissolved in water by means of anion exchange resins|
    NL7110766A|1970-08-08|1972-02-10|
    US3791866A|1972-08-07|1974-02-12|Rohm & Haas|Recovery of waste brine regenerant|
    US4082564A|1975-09-09|1978-04-04|Rohm And Haas Company|Sugar decolorizing quaternary ammonium acrylamide resins|
    NL7700763A|1977-01-26|1978-07-28|Akzo Nv|PROCEDURE FOR REMOVING SILICA FROM AN Aqueous Solution.|US4731419A|1986-02-24|1988-03-15|Nalco Chemical Company|Alkoxylated/cationically modified amide-containing polymers|
    DE3824266A1|1988-07-16|1990-01-18|Bayer Ag|METHOD FOR THE PRODUCTION OF BIFUNCTIONAL ANION EXCHANGE RESINS, NEW BIFUNCTIONAL ANION EXCHANGE RESINS AND THEIR USE|
    US5236701A|1989-07-19|1993-08-17|Lowchol Scientific Inc.|Ingestible hydrophilic polymeric amines useful for lowering blood cholesterol|
    AT392776B|1989-10-16|1991-06-10|Chemiefaser Lenzing Ag|METHOD FOR PURIFYING AQUEOUS SOLUTIONS OF N-METHYLMORPHOLIN-N-OXIDE|
    CN107922218B|2015-09-15|2021-07-20|陶氏环球技术有限责任公司|Method for regenerating acrylic resin|
    RU2730337C2|2015-09-15|2020-08-21|Дау Глоубл Текнолоджиз, Ллк|Method of regenerating acrylic resin|
    RU2734858C2|2015-09-15|2020-10-23|Дау Глоубл Текнолоджиз, Ллк|Water treatment method|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE19803001856|DE3001856A1|1980-01-19|1980-01-19|ANION EXCHANGER, METHOD FOR THEIR PRODUCTION AND THEIR USE|
    [返回顶部]