• 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:
    Cationic polyurethanes are prepared by reacting a monomeric, aliphatic dihydroxyl compound containing a maximum of 7 atoms between the two hydroxyl groups and containing an aliphatic radical having at least 10 carbon atoms on one of said atoms with a polyisocyanate to give a preadduct containing NCO end groups, chain-extending the resultant preadduct by means of an aliphatic monomeric diol containing tertiary nitrogen, and converting the chain-extended product into an ammonium compound. These polyurethanes are particularly suitable as the active component in paper sizes. The sizes can be employed both in bulk sizing and in the surface sizing of paper and give sized papers having a high degree of sizing and a low Cobb value. Sizing in a relatively broad pH range is possible, and the polyurethanes can be processed very well together with products usually used for sizing.
    公开号:SU944507A3
    申请号:SU752095620
    申请日:1975-01-03
    公开日:1982-07-15
    发明作者:Шюрманн Хорст；Бунг Джозеф；А.А.Ван Аальтен Хендрикус
    申请人:Акцо Н.В. (Фирма)；
    IPC主号:
    专利说明:

    a phatic radical containing 1022 carbon atoms, and a monomeric aliphatic diol containing a tertiary nitrogen atom and an obtained polymer are treated with hydrogen chloride as the chain extender, or N-methyldiethanolamine hydrochloride 1, 2-propanediol-3 Dimethylamine is used as a chain extender As ammonium compounds, compounds containing positively charged nitrogen are used. Monomeric aliphatic dihydroxy compounds that have an aliphatic substituent from 10 to 22 atm are particularly suitable. ohms carbon. By the proposed monomeric aliphatic dihydroxy compound is meant non-polymeric glycols (ali, phatic, i.e. organic compounds that have two hydroxyl groups in 1,2- or 1,3-or in one of the other positions, for example, d, .L) -position. Monomeric aliphatic dihydroxyl compounds are predominantly used, in which both hydroxyl groups are connected to each other in chains through a maximum of 7 atoms, the aliphatic substituent that must have an aliphatic dihydroxyl compound can be found on the carbon atom that carries one of the two hydroxyl groups , but it can find c at the carbon atom that lies “between the carbon atoms that have both hydroxyl functions. It contains mainly 10-22 carbon atoms. The aliphatic glycol chain, through which both hydroxyl groups are bonded, contains only carbon atoms, the carbon atom can also be replaced by a heteroatom; oxygen or nitrogen. If the heteroatom that exists in the aliphatic chain is nitrogen, then an aliphatic substituent with a minimum of 10 predominantly 16, carbon atoms may also be bonded to the heteroatom. If the geurooatom is in the aliphatic chain, then according to the proposed method, when the dihydroxy compound with polyisocyanates is rotated, there is no residue at the heteroatom that can react with isocyanate groups. Above all, if for example nitrogen is in a chain, then a third is the valence to be replaced by a residue without active carbon atoms. An aliphatic substituent in a dihydroxy compound must have a minimum of 10, preferably a minimum of 16 carbon atoms. It is not necessary that the substituent is only the corresponding hydrocarbon residue. The group RCOO- also acts as an aliphatic substituent, and R is an aliphatic residue with at least 9, mostly at least 15, carbon atoms. Glycerol monoesters, for example glycerol monostearate or glycerolbeneic acid monoester, are particularly suitable. 8 As compounds in which the carbon atom in the aliphatic chain is replaced by a heteroatom, N-substituted dialkanolamines, especially N-stearyl diethanolamine, can be named. . 1,2-dihydroxyoctadecane and 1, -dihydroxyoctadecane are other dihydroxy compounds which have a substituent with an appropriate number of carbons. The conversion of a substituted monomeric aliphatic dihydroxy compound with a polyisocyanate is carried out best in an anhydrous solvent, preferably in acetone. Other solvents that are inert with respect to the isocyanate groups are suitable as the reaction mixture, respectively, and in comparison with the reaction components have only a slight reactivity. In this connection, tetrahydrofuran, dimethylformamide, chloroform, perchlorethylene, methyl ethyl ketone methylene chloride, ethyl acetate, dimethyl sulfoxide can be named. However, the transformation of an aliphatic substituted dihydroxy compound with a polyisocyanate can also be carried out without a solvent in the melt. Catalysts may be used to convert the dihydroxy compound to the polyisocyanate. A particularly suitable diacetoxydibutyltin appears as a catalyst. Other catalysts are di laurate. butyltin., cobalt naphthenate, zinc octoate, and also tertiary α-amines, for example, triethylamine or 1,4-diaza- (2,2,2) -bicycloooctane. Tertiary nitrogen diols used in chain elongation can also be used as catalysts.
    Polyisocyanates, which are used for the synthesis of polyurethane, can be both aliphatic and aromatic. Mixed aliphatic aromatic compounds are also suitable. Diisocyanates are preferably used. Toluene diisocyanate, diphenylmethane-, diisocyanate and hexamethylene diisocyanate are particularly suitable. Shelled diisocyanates can also be used, for example, the reaction of the |; young product diphenylmethane-4, -diisocyanate with 2 moles of phenol.
    Adducts from glycerol and 3 mol of toluene diisocyanate, as well as tri- (4-isocyanatophenyl) monothiophosphate, are suitable as triisocyanates. When using polyisocyanates that have more than two isocyanate groups in a molecule, the higher part of the diisocyanates is preferentially associated, since uncontrolled structuring is very easy if only the high part of the polyisocyanates that have three or more isocyanates are used;
    According to the proposed process, aromatic diisocyanates are preferred.
    The ratio of the reaction partners, namely the molar ratio of the dihydroxy compound to the polyisocyanate, can vary in a relatively wide range. It is possible, for example, to work with a molar ratio of dihydroxy compound to diisocyanate 1: 1.1 - 1: 3. The 1: 1.5 1: 2.5 molar ratio is particularly suitable, with a ratio of exactly 1: 2 being preferred. j Then, the resulting pre-product is allowed to react with an approximate equivalent amount of aliphatic diol containing tertiary nitrogen. Equivalent amounts mean that an equal number of hydroxyl groups of the diol are used for the existing isocyanate groups. In 1 quality. aliphatic diols, which contain tertiary nitrogen, are particularly suitable N-methyldiethanolamine and 1,2-propanediol-3-dimethylamine.
    Other compounds that have tertiary nitrogen are also used, for example, Nn-butyldiethanolamine, N-tertbutyldiethanolamine, N-methyldipropanolamine, N, H-bis-2-hydroxyethyl-p-toluidine and 1, -bis bis-hydroxyethylpiperazine. The diol contains predominantly only 1 or 2 tertiary nitrogen atoms, the molecular weight is less than 300, preferably less than 200. The reaction with the preproxy diol is referred to as chain elongation. The conversion of the pre-product with a chain extender takes place predominantly in an anhydrous solvent, with acetone
    5 is particularly suitable. Best of all, chain elongation is carried out at boiling point. The progress of the reaction can be observed using an appropriate isocyanate determination method. Before the end of the reaction, the MSO content should be less than 1. Then the product with an extended chain is converted to an ammonium compound. In this case, a free electron pair of tertiary nitrogen is bound, so that nitrogen receives a positive charge. In this process, a suitable acid hydrogen or alkyl group may be bound to a tertiary nitrogen. This chain lengthening process can be circumvented if the corresponding glycol, which already exists as an ammonium compound, is used to extend the chain, for example, a salt that is obtained by converting an acid and a glycol with a tertiary nitrogen, for example, N-methyldiethanolamine hydrochloride.
    Translation of the received product from
    0 An extended chain in the ammonium compound is predominantly made with hydrogen chloride. This may be done with aqueous HC1, however HC1 may also be skipped.
    5 through a solution in the form of a gas. The use of a solution of HC in acetone is also very suitable. The conversion to the ammonium compound can also be undertaken using conventional
    0 alkylating agents.
    It is particularly advantageous if the product with an extended chain is intermediately dried before being converted into an ammonium compound. As an intermediate drying, such treatment is obtained by which the solvent used in this case or residues of other liquids can be removed. At. This especially takes into account spray drying of the product or treatment in a rotary evaporator. The intermediate dried product is then suspended from, for example, in water and converted into an ammonium compound by the addition of hydrochloric acid. When using acids, such as hydrochloric acid, it is advisable not to preserve them 3ai, but slowly dispense them to a product with an extended chain. Example. The apparatus used is a three-neck round flask containing 500 ml, which is equipped with a stirrer, a reflux condenser with a drying tube, and a droplet drip funnel. The flask was charged with t3.5 g (0 mol) of commercial grade glyceryl ostearate. 15 mg of dibutyltin diacetate, 2k ml of anhydrous acetone and 16.0 ml (-19.5 g) of a mixture of (2,) and (2.6) isocyanate- (2) and (2.6) (80.20 (0.1–12 mol)) are successively added. The reaction vessel is heated for 30 minutes to a slight reflux of the solvent with stirring. At this time, the reaction temperature (Approximately. Then a solution of 6.5 g of N-methi-diethanolamine (0, mol) in 20 ml of anhydrous acetone is added dropwise over 10 minutes and then heat again so that moderate reflux is retained. After 60 minutes of reaction time, the NCO content falls below 1.5% and a medium It has a viscosity, water-clear polyurethane solution, which is diluted by adding 1 B of technical acetone to ml. For salification, 27.3 ml of 2N hydrochloric acid is now added for about 5 minutes. After this salt is partially colloidal. partially in the form of a white precipitate, which is transferred into the solution by adding 140 ml of water over 15 minutes while maintaining the temperature of the contents of the flask at about 50 ° C. The resulting clear solution is freed from acetone by vacuum distillation. The result is a 201st, slightly opalescent, light yellow-colored polyurethane anionomer solution. By further distillation, the water concentration is increased. At 32 wt D, the polymer solution is still fluid. EXAMPLE 2 The process is carried out as in Example 1, however, 6, O, instead of 6.5 g of N-methyldiethanolamine, and 25.1 ml of 2 N are used for salt formation. hydrochloric acid. The polyurethane solution is no longer diluted with acetone before adding hydrochloric acid. The addition of water according to Example 1. A bluish, shimmering emulsion with an average particle size of 0.5 mm occurs. Example 3 The process is carried out as in Example 2. An elongated chain product is dried intermediate by spray-drying. The intermediate dried product has a melting point of about 93 ° C. To convert the ammonium compound, the intermediate dried product is suspended in water, then hydrochloric acid is added slowly. Example. The process is carried out as in example 1, however, the conversion between glycerol monostearate and toluene diisocyanate is catalyzed by the total amount of L-methyldiethanolamine, which are removed during chain elongation. A product similar to example I occurs. Pru and m 5. The process is carried out as in example 1, but immediately after dissolving glycerol monostearate and toluene diisocyanate without pre-catalyzed reaction of these components with the addition of organotin compounds, tertiary amines or similar active substances, with a solution of N-methyldiethanolamine in acetone is dripped. The reaction time is 2 hours. The ionomer dispersion is slightly turbid. p I M r 6. Eagru; Glycerol monostearate is heated and heated to melt. 16 ml of toluene diisocyanate are added dropwise so that the temperature does not exceed 75 ° C. At the end of the exothermic reaction, the mixture is stirred for another 20 minutes at 75 ° Cf, then the melt is transferred to the solution by adding 50 ml of anhydrous acetone. Further reaction with N-methyldiethanolamine, salt formation and dispersion according to Example 1. Example. The process is carried out as in example 1, however, together 6.5 g
    N-methyldiethanolamine 8.0 g of N-butyldiethanolamine are used. It is highly dispersed, opalescent dispersion.
    EXAMPLE 8 The process is carried out as in example 1, instead of 19.5 g of toluylene diisocyanate, 29, g of 6is- (-isocyanate cyclohexyl) methane are used. A slightly opalescent solution is obtained.
    Example 9. The process is carried out according to the example} j; however, neutralization of tertiary nitrogen follows only to 80SS by decreasing the amount of hydrochloric acid to 21, E ml. There is a stigne and highly dispersed emulsion-Y;, -:. :. . fTp and ip 10. The process is carried out with nfoinptmeipy I, however, glycerol monostearite is replaced by 19.5 g of M, H-di-oL .- g of droxylethyl-sterylamine.
    O P: and W er I. The process is carried out as in Example 1, however, glycereinstearate is replaced with 15.6 g of I, 2-dihydroxy octadecane. Occurs slightly opalescent, slightly yellowish dysggers.
    At measure 12, the process of example 1 is carried out before the inclusive reaction with M-methyldi; ethanolamine. By the addition of 0.86 g of dimethyl sulfate and a further {30% of reaction time for 30 / min), the tertiary nitrogen is converted to quaternary by up to 25% molar.
    After breaking down with 160 ml of technical acetone, 20, i m is attached.
    2 n. hydrochloric acid and then dispersed according to example 1.
    As a final product, a stable, highly dispersed emulsion with strongly cationic centers appears.
    权利要求:
    Claims (2)
    [1]
    1. Patent FRGL880 85, cl. 39 s, 6, pubic. .
    [2]
    2. German Patent No. 8917ii2,
    cl. 39 s, 6, pub. TE + I (prototype).
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    同族专利:
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    JPS55107599A|1980-08-18|
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    HU170930B|1977-10-28|
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    FR2256937A1|1975-08-01|
    NO141167B|1979-10-15|
    BR7410962D0|1975-08-26|
    AT339607B|1977-10-25|
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    NL177218C|1985-08-16|
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DD5379A|
    DD5381A|
    DE953012C|1952-07-04|1956-11-22|Bayer Ag|Process for the production of soluble, preferably higher molecular weight, polyisocyanates capable of further conversion|
    US2966472A|1957-06-26|1960-12-27|Allied Chem|Non-cellular polyurethane coating resistant to discoloration|
    GB953357A|1960-11-08|1964-03-25|Textron Inc|A process for the preparation of urethane modified vegetable oils|
    DE1570602A1|1965-09-03|1969-08-14|Bayer Ag|Process for the production of aqueous polyurethane dispersions|
    DE1595602A1|1966-03-12|1969-09-18|Bayer Ag|Process for the production of polyurethane plastics|
    DE2019324C3|1970-04-22|1979-02-22|Bayer Ag, 5090 Leverkusen|Process for the production of lightfast polyurethane ionomers|DE2537653B2|1975-08-23|1977-10-27|Bayer Ag, 5090 Leverkusen|PAPER SIZING AGENTS AND PROCESS FOR PAPER SIZING|
    DE3102038A1|1980-01-28|1981-12-10|W.R. Grace & Co., 02140 Cambridge, Mass.|POLYURETHANE POLYMER AMINE SALT AS A PAPER ADDITIVE|
    DE3017599C2|1980-05-08|1985-01-10|Akzo Gmbh, 5600 Wuppertal|Fuel briquettes|
    DD158914A5|1980-05-08|1983-02-09|Akzo Nv|FUEL BRIQUETTES|
    SE8200472L|1981-02-23|1982-08-24|Grace W R & Co|PROCEDURE FOR IMPROVING THE WATERPROOF POSITION OF PAPER|
    FR2565267B1|1984-06-05|1987-10-23|Atochem|POLYURETHANE LATEX AS A GLUING AGENT IN THE PAPER INDUSTRY, ITS MANUFACTURING METHOD|
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    DE3523856A1|1985-07-04|1987-01-08|Bayer Ag|AQUEOUS SOLUTIONS OR DISPERSIONS OF POLYISOCYANATE ADDITION PRODUCTS, A METHOD FOR THE PRODUCTION THEREOF, AND THEIR USE AS A COATING OR SIZING AGENT FOR PAPER|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE2400490A|DE2400490C2|1974-01-05|1974-01-05|Cationic polyurethanes and processes for their manufacture|
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