• 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:
    This invention relates to removal of cerium, used as a free-radical initiator, from aqueous polymeric dispersions, particularly starch graft copolymer dispersions, by adsorbing cerium (III) onto a strong cation exchange resin, to separation of the adsorbed cerium (III) from the resin using a solution such as sodium sulfate or sodium oxalate to form a cerium (III) precipitate, and to oxidation of the separated cerium (III) to cerium (IV).
    公开号:SU1228778A3
    申请号:SU813280850
    申请日:1981-05-07
    公开日:1986-04-30
    发明作者:Лоренс Спикмэн Эдвин
    申请人:Стандарт Брендз Инкорпорейтед (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to a chemical technology for the preparation of polymer compositions, specifically to the regeneration of catalysts to initiate polymerization reactions of unsaturated organic compounds, and can be used in the isolation of spent cerium from the reaction products of free radical polymerization of vinyl monomers.
    During such reactions, the cerium (IV) used to initiate the polymerization processes is reduced to the trivalent state and remains in the reaction products (polymer dispersions).
    The polymer dispersions obtained by free radical initiation have various uses, for example, adhesives, adhesives for textile fibers, coatings and thickeners for textile inks in a paste. A significant and useful part of this dispersion is a polymer. Residual Ce (III) does not play a positive role in dispersion, and in some cases, for example, when used in food industry.
    l x, cerium is an undesirable component of the dispersion. Moreover, cerium is an expensive material and its desirable to be regenerated as Ce (IV) compounds, which are used as initiators of polymerization processes.
    The aim of the invention is to provide the possibility of converting cerium into its active form.
    Example 1. 1200 ml of Amberlite IR-252 sulphonated cation exchanger with theoretical capacity of 79.8 mg cerium (III) per 1 ml of resin are preconditioned in 1 M sodium sulfate solution at pH 2.5, then washed until no sulfate ions are present. . The cathionite is placed on a column and 12.336 g of synthetic polymer starch emulsion starch emulsion (about 37% solids) containing 19.166 g of cerium is passed through the resin forming the packed layer at a rate of about 30 ml / min to remove the cerium. Analysis of ion exchange polymer emulsion does not show the presence of cerium.
    Then copfi - fH .1 is absent from the absence of irojinMT pHoi i e-gutp-.si11, mega 10 mesher
    Q
    15
    25
    2287782
    2550 ml of 1 M sodium sulfate solution for 45 minutes and sieved to separate the resulting cerium suspension from the resin. A suspension of sulphate 2 salt of cerium, similar to milk, is left to precipitate and the sedimented solution is decanted. After this, the sodium sulfate solution is returned to the resin and stirred for 45 minutes. The process is repeated until there is no cerium removed from the resin in the total amount after 3 extractions (contacts). After treatment with sodium sulfate, the resin contains 3.577 g of cerium. This value represents only about 3.7% of the theoretical capacity of the resin. Thus, the resin that is reconstituted by removing the cerium is ready for re-extraction of cerium from the polymer emulsion. The resin can be used to effectively remove cerium from a polymer emulsion up to about 70% of theoretical capacity without the occurrence of cerium leakage into the contacting emulsion (which means essentially 100% removal). However, for practical purposes, the resin is used to remove cerium to achieve only about 50% of the theoretical capacity (which is 39.9 mg of Ce per 1 ml of resin). Then, cerium is desorbed and the contaminated resin is regenerated.
    The extracted salt — cerium sulfate — is suspended in 1200 ml of water while adjusting to pH 9.5 with a 58% solution of ammonium hydroxide. This solution was vigorously stirred while oxygen was bubbled through the suspension for 1 hour. Add an additional amount of ammonium hydroxide solution to maintain pH 9.5. Then the pH of the suspension was adjusted to 4.0 with sulfuric acid and 19 g of a 58% ammonium hydroxide solution was added to bring the pH back to 9.5. Under these conditions, the most complete conversion of cerium to the active form of cerium occurs (1X0, which was established experimentally. Then oxygen is bubbled through the intensively stirred suspension for 1 h, and the pH is maintained at 9.5 by adding 58% hydrate solution ammonium oxide.
    Next, the resulting regenerated product in the form from the middle of the cerium (IV)
    thirty
    35
    40
    45
    50
    55
    3
    filtered off. The result is a wet mass, pressed on the filter, in the amount of 55.25 g. The analysis shows the presence in 1 g of the filtered mass of 0.2510 g of the total amount of cerium. Additionally, it was found that 1 g of the mass pressed on the filter contains 0.2295 g of active cerium (IV). Yield 91%.
    To 55.00 g of re-activated cerium, calculated on the basis of 12.625 g of cerium (PG), 1.70 ml of 6N is added. sulfuric acid solution. The mixture is heated to 60 ° C and held at this temperature for 24 hours with vigorous stirring. The resulting regenerated initiator containing cerium (IV) has good solubility. The total amount of converted cerium (IV) is 14 g or 74% of its initial content in the emulsion.
    Example 2. 52 ml of cerium-free strong cation-exchange resin Brand Duolite C-26 is treated four times with 52 ml of 1N. hydrochloric acid by suspending and stirring the resin in acid to obtain the hydrogen form of the resin. The treated resin is transferred to a column through which another 52 ml of 1 N is passed. sulfuric acid to complete. full conversion of the resin to the hydrogen form. The resin is then washed with deionized water until the stream is free of sulphate ion.
    200 ml of the starch graft copolymer dispersion (solid content 39%) is adjusted to pH 5.0 with sulfuric acid. It is sieved through a 100 mesh sieve and drained into the top column. The sample is held for 15 minutes to reach the column temperature. A stream is passed through the column at a rate of 0.025 bed volumes per minute. Collect portions of 15 ml and measure the pH of each portion. Portions are collected to obtain two approximately identical samples, which are the initial and the last part of the experiment. Samples analyzed for pH cerium content: 99.65 and 100% cerium, initially present, removed the pH of the samples 1.38 and 1.30.
    PRI me R -3. Effect of cation exchanger on cerium removal.
    287784
    A resin free of cerium (50 ml), as in example 2, in sodium form, is placed in a column with a jacket. Three layer volume (WU), equal to 14.2%
    5 A solution of sodium sulfate pripH5.0 is passed through a column for complete conversion to the sodium form. The resin is washed from sulphate, 150 g of the sample is a dispersion of graft copolymer graft
    10 are sieved and the pH is adjusted to 5.1, placed in the tank of the column and adjusted to the temperature of the column. The sample is passed through the column at 0.025 WU per minute and 25 ml are collected.
    15 flow. Flow analysis shows that 91.0% cerium has been removed and the average pH is 5.0. The higher the pH of the stream compared to the pH of the stream in example 2 (1.38-1.30
    - v. 5.0) is obviously associated with a lower degree of removal of cerium (99.65-100% versus 91.0%) obtained according to this example.
    Example 4. Removal of cerium from
    25 dispersions using resin in the combined hydrogen and sodium form.
    The resin (61 ml), as described in Example 2, is suspended in sodium form in 122 ml of sodium sulfate solution (14.2 g per 100 ml of solution), the pH of the suspension is adjusted to 3.0 using sulfuric acid for 15 minutes before until the pH is stable. The resin is placed in the bottom.
     part of the column and washed from the sulfate ion. 100 ml of the sifted dispersion of starch graft copolymer pH 2.2 is placed in the upper column, brought to the temperature of the column and passed
     through the resin at a speed of 0.20 WU per minute. Samples were prepared as described in Example 2 and analyzed. Results show 99.31 and 100% removal of cerium from the dispersion, pH
    5 2.49 - 2.55.
    Example 5. The selection of CE (111) adsorbed on a strong cation-exchange resin.
    A sample (9.4 ml) of a strongly cationic resin in hydrogen form is loaded with cerium (7.9 mg per 1 ml of resin) by stirring the resin in a solution of cerium nitrate. The resin is removed from the solution, washed thoroughly and suspended in 15 ml of deionized water. Thereafter, 7 g of anhydrous sodium sulfate is stirred into suspension. Almost immediately
    thirty
    S
    a milky white precipitate appears. The precipitate is separated by decanting. Tests show that the white precipitate contains cerium.
    The method of loading the resin and separating the cerium is repeated several times with the same resin to obtain the same results. The results show that cerium is precipitated from smog ne before sedimentation, cerium sulfate precipitate is formed outside the resin and does not clog the pores of the resin.
    The extraction of cerium from the resin can be carried out with sodium sulfate solution using 1 M sodium sulfate.
    The precipitate is easily separated from the resin by settling and decanting or by washing the precipitate through a sieve having openings small enough to hold the resin.
    Example 6. Oxidation of Ce (ITI) to Ce (IV) - reactivation of cerium after removal of cerium from an ion exchange resin
    A suspension of sediment Ce (III) in an acidic solution of sodium sulfate, removed from the resin, as described in example 5, is alkalinized (pH 8) with ammonium hydroxide. The fine precipitate is converted into a heavy, flocculent white precipitate of cerium hydroxide. Qualitative ana-LIZ precipitate shows the absence of Ce (IV). The experiment consists in placing a small amount of sediment in 2-3 ml of strong sulfuric acid, and the presence of Ce (IV) should be determined by the appearance of a yellow color.
    The alkaline suspension (pH 8) is sprayed with air with moderate agitation. The color change is noticeable after 30 minutes. A weak positive quality test for Ce (IV) was obtained after 3 hours. Spraying was continued overnight with a sufficient amount of ammonium hydroxide added to maintain pH 8. At the same time, the precipitate became light cream in color and a strong positive test was observed for Ce (IV) . The precipitate was isolated by centrifugation, washed several times with water, and the suspension was added to 100 ml of 1.22 n. sulfuric acid. The mixture is heated to 70 ° C and 5 ml of concentrated sulfuric acid is added carefully to dissolve the soluble portion of the precipitate. The acidified suspension (180 ml) was evaporated in a water bath to a 24 or almost clear solution.
    287786
    The solution is diluted to 50 ml. Analysis of the solution shows the presence of 0.218 mol of Ce (IV), 0.050 mol of Ce (III) and 4.85 mol of hydrogen ion per 5 liter. Thus, Ce (III), removed from the dispersion of the starch graft copolymer and then separated from the ion exchange resin as a precipitate, is oxidized to Ce (IV) by contact. About solid sediment in alkaline medium with air ,.
    The same results are obtained by spraying oxygen through the same alkaline suspension. 5 Example 7. Isolation and reactivation of cerium isolated from the dispersion, followed by the repeated use of reactivated cerium in the graft polymerization of vinyl monomers.
    The pH of the aqueous suspension of the strong cation-exchange resin of Example 2 in the sodium form is adjusted to 2.5 with sulfuric acid. After that, the resin is placed in a column and washed with water.
    until the absence of sulfate ions. The resin is then used to separate the cerium from the dispersion of the starch graft copolymer. Cerium is recovered from the washed
    0 SMOL by treating with a 0.36 M sodium sulfate solution as described in Example 1. The precipitate is sieved from the resin and washed to remove salts. The precipitate Ce (III) is then oxidized by
    Air J spraying and dissolving in acid, in accordance with Example 6. The polymerization of vinyl monomers is then carried out by the addition of a reactive cerium solution to the reaction mixture.
    The final product obtained contains 40.1% solids from a dry base, has a pH of 8.3 and a Brookfi.pud viscosity of 196 cP / 25 s.
    2 Dispersion films, molded on glass, smooth, continuous, have good adhesion strength and are similar to those obtained from dispersions of starch graft copolymers, where
    . polymerization initiated by cerium ammonium nitrate.
    Example 8, Isolation of cerium adsorbed on a strong cation resin, by forming a precipitate using sodium oxalate.
    Cerium (III) is removed from the dispersions of the starch graft copolymer by contacting the dispersions with a strong 712287788
    thion-exchange resin according to example 4 in the mouth of the wet resin obtained con
    the combined sodium-sodium concentration of sodium oxalate was in the form. The resin is separated from a dispersion of approximately 0.20 M, the final value is thoroughly washed with water. The pH of the solution is 4.6.
    50 ml of precipitated wet resin vno-5
    with t per cylinder (100 ml). After this, 50 ml of 0.27 Cera (III) oxalate oxalate hydrochloride is added to the cylinder, a solution of sodium oxalate with pH 5 is added. So-rj is then reactivated according to example 1, held by the cypond. Then the same results are obtained and mixed with using several 0.2 M solutions of its rotation. For medium volume sodium oxalate.
    权利要求:
    Claims (5)
    [1]
    1. METHOD FOR ISOLATING CERIUM FROM AQUEOUS DISPERSION OF POLYMERS, comprising contacting it with a cation exchange resin to separate cerium (III) from a dispersion, characterized in that, in order to enable the conversion of cerium into its active form, after separation of cerium (III) from the dispersion, solid-phase regeneration of the resin by treating it with a salt that forms an insoluble compound with cerium (III), followed by separating the resulting suspension of cerium (III) salt from the resin and oxidizing cerium (III) in the form of a suspension to cerium (IV) with air or oxygen in an alkaline environment.
    [2]
    2. The method of pop. ^ characterized in that the solid-phase regeneration of the resin is carried out by treating it with anhydrous sodium sulfate or sodium oxalate or their aqueous solutions.
    [3]
    3. The method according to PP. 1 and 2, characterized in that the concentration of sodium sulfate or sodium oxalate solutions is 0.36-1.0 and 0.2 - 0.27 mol / L, respectively.
    [4]
    4. The way popp. 1 and 2, characterized in that the oxidation of cerium (III) to cerium (IV) is carried out at a pH of 8.0-9.5 in two stages with a duration of 1 ~ 1.2 hours each with an intermediate adjustment of the pH of the suspension to 3.8 - 4.0 acid solution.
    [5]
    5. The method of pop. 3, characterized in that the adjustment of the pH of the suspension in the region of 8.0 - 9.5 is carried out with a 50-58% solution of ammonia, and in the region of 3.8 - 4.0 with a solution of sulfuric acid.
    1228778 A5
    I 1
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    同族专利:
    公开号 | 公开日
    CA1174856A|1984-09-25|
    FR2482110A1|1981-11-13|
    FI811419L|1981-11-09|
    BG41131A3|1987-04-15|
    JPH0148282B2|1989-10-18|
    PT72930A|1981-05-01|
    BE888713A|1981-11-09|
    GB2075479B|1983-06-02|
    PT72930B|1982-04-12|
    YU117381A|1983-06-30|
    DE3116794A1|1982-02-11|
    NL8102275A|1981-12-01|
    IT8121569D0|1981-05-07|
    SE8102841L|1981-11-09|
    BR8102672A|1982-01-26|
    ES8203395A1|1982-04-01|
    SE459260B|1989-06-19|
    AU6988981A|1981-11-12|
    HU183425B|1984-05-28|
    IT1142017B|1986-10-08|
    YU42399B|1988-08-31|
    MX158450A|1989-02-02|
    US4279791A|1981-07-21|
    AU545165B2|1985-07-04|
    ES502299A0|1982-04-01|
    FI69855B|1985-12-31|
    FR2482110B1|1986-03-21|
    JPS573801A|1982-01-09|
    GB2075479A|1981-11-18|
    FI69855C|1986-05-26|
    NZ196944A|1983-11-18|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2694681A|1952-03-07|1954-11-16|Univ Idaho Res Foundation Inc|Recycling the complexing agent in the separation of ions by ion exchange|
    US2897050A|1954-04-28|1959-07-28|Air Reduction|Separation of rare earth values by means of a cation exchange resin|
    US2922768A|1956-04-12|1960-01-26|Mino Guido|Process for polymerization of a vinylidene monomer in the presence of a ceric salt and an organic reducing agent|
    FR1522387A|1966-05-20|1968-04-26|Inst Textile De France|Process for grafting polymers containing hydroxyl groups|
    US3509084A|1966-10-26|1970-04-28|Gulf Research Development Co|Ion exchange process|
    JPS5133931B2|1974-09-28|1976-09-22|US4751061A|1987-04-30|1988-06-14|Gte Products Corporation|Process for recovering scandium from waste material|
    DE19837020C1|1998-08-14|1999-09-23|Merck Patent Gmbh|Process for the removal of cerium initiator salts from graft polymers for biotechnology and pharmaceutical applications|
    JP3897059B2|2004-06-22|2007-03-22|旭硝子株式会社|Liquid composition, process for producing the same, and process for producing membrane electrode assembly for polymer electrolyte fuel cell|
    CN103038303A|2010-06-16|2013-04-10|卡吉尔公司|Starch-based compositions for latex replacement|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US06/147,775|US4279791A|1980-05-08|1980-05-08|Recovery of cerium from polymer dispersions|
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