• 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:
    Hydrolysis-resistant copolyether-esteramides according to this invention are terminated, at one chain end, by a hydrocarbon radical and at the other chain end by a hydroxyl group. The sequential linear aliphatic copolyether-esteramides according to the invention are obtained by a polycondensation reaction of linear aliphatic dicarboxylic polyamide oligomers having a molecular weight comprised between 300 and 15,000, with omega - omega '-dihydroxyl polyoxyalkylene sequences having a molecular weight comprised between 100 and 6000 in the presence of a linear aliphatic monocarboxylic polyamide oligomer having a carboxyl group at one end of the macromolecular chain and a hydrocarbon radical at the other end thereof.
    公开号:SU1079179A3
    申请号:SU782567997
    申请日:1978-01-24
    公开日:1984-03-07
    发明作者:Делеан Жерар；Герен Бернар；Пулэн Клод
    申请人:Анто Шими (Фирма)；
    IPC主号:
    专利说明:


    The invention relates to a process for the preparation of linear aliphatic, thermoplastic, block copolyesters with good hydrolysis resistance. The closest to the present invention is a method for producing simple complex block copolyether IDs by reacting aliphatic polyamides containing two carboxyl groups with a molecular weight of 1300-2090 and a polyoxyalkylene glycol with a molecular weight of 650-1000 in the presence of a catalyst when stirred and heated in a vacuum 13. Known simple-complex block copolyamides possess good mechanical properties for the production of molding materials for films, coatings or textile fibers. However, most of the copolyester amide are ice-deficiently resistant to hydrolysis due to the presence of terminal free carboxyl groups which are capable of catalyzing the reaction of ester functional groups contained in the macromolecule, thus causing chemical degradation of the macromolecular chain. The purpose of the invention is to increase the cost to hydrolysis when heated. This goal is achieved by the fact that in the preparation of simple-complex block copolyether-amides by the reaction of aliphatic polyamides containing two carboxy groups with a molecular weight of 1300-2090 and a polyoxoxyalkylene glycol with a molecular weight of 650-1000 in the presence of a catalyst with stirring and heating in vacuum, the reaction is carried out in the presence of an aliphatic polyamide with a molecular weight of 1300-2100, obtained by the reaction of a monomer selected from the group containing 11-aminoundecanoic acid, caprolactam, dodecactam in the presence of mon ocarboxylic acid, this polyamide is used in an amount of 2-10 wt.% of the block copolymer. The predlozhenny method is that block copolyesteramides are obtained by polycondensation of aliphatic linear, containing two | the arboxyl groups of oligomeric polyamides with a molecular weight of 1300-2090, and the WJ w -dihydroxylated polyalkylene units of a molecular weight of 6.50-1000 in the presence of an aliphatic linear, containing one carboxyl group of a polyamide, which has a macromolecular chain at one end and a carboxyl group on one end. the end. The hydrocarbon radical. This polyamide containing a carboxyl group at one end of a macromolecular chain and a hydrocarbon radical at the other end is obtained in a known manner by polymerizing or polycondensing polyamide aliphatic monomers: caprolactam, dodecolactam, 11-aminoundecanoic acid in the presence of a monobasic carboxylic acid, which simultaneously plays the role of a limiting agent macromolecular chain. This polyamide is used in an amount of 2-10% by weight of block copolymer. Organic monobasic acids that can be used to produce polyamides with one carboxyl group in the macromolecular chain are saturated aliphatic acids with Cjj-Cg carbon atoms, for example, caproic, decane, lauric, stearic, myristic, palmitic. The polyamides used with one carboxyl group have a molecular weight of 1300-2100. Polyamides with two carboxyl groups are obtained by known methods, namely, that polycondensation of a linear aliphatic polyamide of type 6,6,6, 6.10,11 or 12 is carried out in the presence of a saturated dibasic aliphatic acid, such as amber, adipic, cork, azelaic , sebacicin, dodecandioic acid. Since this diacid plays the role of a chain stopper in the polymerization of lactam or in polycondensation reactions, the initial amount introduced must be calculated depending on the average molecular weight that you want to receive. Polyamide can be obtained from lactams or amino acids, the hydrocarbon chain of which has 4-14 carbon atoms, such as, for example, caprolactam, enantholactam, dodex-shaktam, undecanolactam, dodecanolactam, 11-aminoundecanoic acid, 12-aminoundecanoic acid. Polyamide can also be a condensation product of a dicarboxylic acid with a diamine, such as nylon 6.6, 6.9, 6.10, 6.12, 9.6, the condensation products of hexamethylenediamine with adipic acid, azelaic acid, sebacic acid, 1,12-dodecandioic acid and nonanmethylenediamine with adipic acid. The monomers used to make polyamide units with one carboxyl group and polyamide units with two w, w-carboxyl groups are preferably of the same nature.
    Polyethers. Containing terminal gidroksilirovanyye groups are Coll linear or branched polyoxyalkylene glycols, such as polioksietileiglikrl, polioksipropilongli1 ol, polioksitet rametylenglikol or mixtures thereof or copolyethers derived from a previous compounds, and average molecules which constitute molecular weight was 650 -1000.
    The weight fraction of polyoxyalkylene glycol in relation to the total weight of the constituents can vary from 1 to preferably from 3 to 50%.
    The polycondensation reaction for the preparation of copolyester aliphols is carried out in the presence of a catalyst with stirring and under vacuum in the order of 0.05–15 mm Hg, at temperatures that are higher than the melting points of the constituents and which are necessary to maintain the reaction mass in a liquid states, these temperatures being 100 grams, and preferably 200-300 C.
    The reaction time may vary from 10 minutes to 10 hours, preferably it is 1-7 hours. This reaction time depends on the nature of the polyoxyalkylene glycol and must be sufficient to achieve the final viscosity needed to obtain a product with good properties for pressing or extruded plastics. .
    Additives, such as antioxidants, stabilizers, imparting resistance to light and heat, substances that impart flame retardancy, dyes, can be added to the resulting polycondensate prior to processing operations or, if possible, during the operation of polycondensation, to improve the properties of the product or its modifications characteristics depending on the requirements for a specific use.
    It should be noted that, at the beginning of the reaction, an antioxidant, 4,4-bis-dimethylbenzyl, -diphenylamine, which, when imparting a weakening effect against aging, has the property of giving the reaction a more regular flow rate without altering the final result, should be followed.
    Control measurements and identification of the products obtained: the intrinsic viscosity is determined in m-cresol at 25 ° C using the Ubellode viscometer; deformation characteristics are measured by the norm ASTND 638.
    The following examples are given as illustrative, but not limited to the scope of the invention.
    Example 1. In a 1 liter reactor, 224 g of polyamide-11 with two carboxyl groups of average molecular weight previously obtained by polycondensation of 11-aminoundeconic acid in the presence of adipic acid and 36 g of polyamide-11 with one carboxylic acid group of an average molecular mass Mp - 2000, previously obtained by polycondensation of 11-aminoundecanoic acid in the presence of stearic acid. Then 125 g of polyoxytetramethyl glycol of average molecular weight Mp 1000 and 1.5 g of tetrabutyl orthotitanate and 4 g of 4, 4-bis-dimethylbenzyl jf-diphenylamine are added.
    An inert atmosphere is created over the reaction mixture and heated until the temperature reaches 260 ° C, then a vacuum is created inside the reactor while maintaining vigorous stirring, starting from the moment when the components melt. The reaction thus lasts for 3 hours at 260 ° C. under a vacuum of 0.1 mm Hg. and the stirring rate gradually decreases with increasing viscosity of the reaction medium.
    This resulting product has an intrinsic viscosity of ft 1.5. According to thermal differential analysis, it has 173 ° C ..
    Quantitative determinations of the end groups of this product give the following results:
    HH traces of COOH 0.01 meq / g. The dried product is then extruded using an Extrusion extruder at 210 s and at a speed of 80 rpm, then injected into an ARBurG press.
    Dynamometric tests give the following results: Stress at the point of fluidity (with a yield point, kg / cm2 -95
    Elongation at the yield point,% 16
    Rupture stress, kg / cm232.
    Elongation at break,% 480 Samples are immersed in permuted water and samples are taken in time, obtaining the following results
    Example 2. A standard simple copolyester amide, i.e. without the use of polyamide with one carboxyl group.
    one
    314 g of polyamide-11 with two carboxyl groups of average molecular weight Mp 2090, previously obtained by polycondensation of 11-tamino -undecanoic acid in the presence of adipic acid, are introduced into a 1-liter reactor; 150 g of polyoxymethylglycol
    average molecular weight, 1.5 g tetrabutyl orthotitanate and 5 g 4,4-bis- (α-dimethibenzyl) diphenylamine
    The reaction is carried out under the same conditions as in example 1,
    The following characteristics are obtained:
    1111.5
    NH 2 tracks
    COOH0.07 meq / g
    mp 173 ° C
    Technological results give the following results.
    It should be noted that under the same operating conditions, the polycondensate obtained without the polyamide with one carboxyl group is maintained for only 7 days instead of 14.
    Example H. In a 6 liter stainless steel reactor equipped with a variable speed agitator, 910 g of fractionalamide-6 powder with two carboxyl groups of average molecular weight Mp 1300, previously obtained by polymerization of caprolactam in the presence of adipic acid, are introduced. as a chain limiter, 130 g of polyamide-b powder with one carboxyl group of average molecular weight Mp 1300, previously obtained by polymerization, g-caprolactam in the presence of enanthic acid as o restrictor circuit, 520 g of polyoxytetramethylene glycol of average molecular weight Mn of 6.50, 1.6 g of
    tetraisopropyl orthotitanate and 14 g of 4,4-bis-° C, o-dimethylbenzyl-diphenylamine.
    Y
    Inside the reactor, create a vacuum of them (0.5 torr), mix with insignificant skurumost, and heat. When the temperature reaches, the reaction mass completely disperses and the stirring speed is increased sufficiently to obtain a thorough mixture of two immiscible phases — a polyether — and a polyamide. Continue to heat until the current temperature of the reaction mass reaches.
    Example 4. As a comparison, standard cros- is synthesized; com plex esopamide without the use of polyamide with one carg box group.
    Into a 2 liter reactor, 350 l of polyamide b are introduced with two carboxyl-vychmyk groups of average weight, 5g) previously prepared by polycondensation of caprolactam in the presence of adipic acid, 175 g of poly- 40, ix tetramethylene glycol of average modular mass Mp 650; 1 g of tetP. Compared to Example 3, it can be seen that the polycondensate obtained without the polyamide with one carboxyl group of 60 remains only 2 days instead of 7 days.
    Example 5. 243 g of polyamide-11 with two carboxyl groups were introduced into a 2-liter reactor.
    The reaction is continued for a time sufficient to produce a product with an appropriate viscosity, which has the following characteristics: Gg3.5
    Cn traces
    COOH1,1 mEq / g
    m.p.
    Samples are hydrolyzed in permuted water at 100 ° C.
    ““ I
    rabutilortotitanat and 10.5 g of 4,4-bis- (dfd-dimethylbazyl diphenylamine.
    The reaction is carried out under the same conditions as in Example 3.
    The resulting product has the following characteristics:
    M.1.45
    NH2 traces
    COOH0.075 meq / g
    192 ° C
    T.I.
    Samples are hydrolyzed in permuted water at 100 ° C.
    i average molecular weight previously obtained by polycondensation of 11-aminoundecanoic acid in the presence of adipic acid, 17.5 g of polyamide-11 with one carboxyl group of average molecular weight Mn 2000, previously obtained polycondens-.
    using 11-aminoundecanoic acid in the presence of stearic acid, then 131 g of polyoxyethylamine glycol of an average molecular weight of Mp 1000, 1.5 - g of tetrabutyl orthotitanate and 5 g of 4,4 -6HC (oC, ot-dimethylbenzyl) -diphenylamine are added.
    The reaction is carried out in the same conditions as in example 1. The resulting measures b. They work according to the method described in example 1, but they use 8 g of polyamide 11-monocarbonate, a boronic acid with an average p-: molecular weight of Mp 1950, previously. obtained by polycondensation of 11-amino-C5 undecanoic acid in the presence of caproic acid.i
    The product obtained has a viscosity of 1.5 and a melting point of 173 ° 6.
    - Example 7: According to the method described in example 1, but 32 g of 11-monocarboxylic polyamide with average molecular weight Mp 2060, previously obtained by polycondensation of 11-aminoundecanoic acid in the presence of decanoic acid, are used. 65
    has the following harak1, 5
    traces
    0.01 meq / g
    173С
    : The image is hydrolyzed in permuted water at
    A quantitative analysis of the “1 group” performed on this product gives the following results:
    Knu Traces, ICOOH 0.012 meq / g I The dried product is then extruded using an extruder and subjected to hydrolysis with replaceable water at, as indicated in Example 1. The following results are obtained.
    The resulting product characteristics
    Characteristic
    viscosity
    Point-to-melting, C
    NHf trailer
    SOOS are terminal,
    mEq / g
    After drying, the product is then extruded using an extruder and
    Mp 1350 weight, previously obtained by polymerization of ε-caprolactam in the presence of caproic acid.
    The resulting product has the following characteristics;
    They are tested for thermohydrolysis, as indicated in Example 1.
    COO koitsevye, mEq / g0.01
    The product is dried, then extruded using an extruder and subjected to hydrolysis test as described in Example 1,
    polyamide 12-monocarboxylic acid with an average molecular weight of Mn 200-0 f previously obtained by polycondensation of lactam 12 in the presence of caproic acid.
    The resulting product has the characteristics.
    Characteristic of x1,52
    12-monocarboxylic acid amide with an average molecular weight of Mn 2100, α-lactam 12, previously obtained by polycondensation in the presence of stearic acid.
    The resulting product has the following characteristics.
    Characteristic
    viscosity 1,55
    20 COOH terminal,
    0.010 meq / g
    After drying in an oven, the product is extruded using an extruder .. 25 and subjected to hydrolysis with replaceable water at 100 ° C, as described in Example 1.
    Get the following results.
    COO trailer,
    0.011 meq / g
    After drying in an oven, the product is extruded using an extruder and subjected to hydrolysis with replaceable water at 100 ° C, as indicated in Example 1.
    Get the following results.
    M,
    11 15 1
    25 25
    Example 12. It is melted as described in Example 1, but using 30 g of a 12-monocarboxylic acid polyamide with an average molecular weight of Mn 2100, pred2.2C but obtained by polycondensation of lactam 12 in the presence of lauric acid.
    The resulting product has the following characteristics.
    Characteristic
    viscosity 1.50
    500
    290 495 275 365 170
    Melting point, C 173 HH terminal Traces of COOH terminal, mEq / g 0.011
    After drying in an oven, the product is extruded using an extruder and subjected to hydrolysis with replaceable water at 100 ° C, as indicated in Example 1.
    Get the following results.
    权利要求:
    Claims (1)
    [1]
    METHOD FOR PRODUCING SIMPLE BLOCK BLOCKS-POLYEFIRAMIDES by reaction of aliphatic polyamides containing two terminal carboxyl groups with a molecular weight of 13002090 and a polyoxyalkylene glycol with a molecular weight of 650-1000 in the presence of a catalyst with stirring and improving the temperature so that the polymer is heated in order to improve the temperature, to hydrolysis by heating, the reaction is carried out in the presence of an aliphatic polyamide, with a molecular weight of 1300-2100, obtained by the reaction of a monomer selected from the group consisting of 11-aminoundecane hydrochloric acid, caprolactam, dodecalactam, in the presence of monocarboxylic acid C ^ -C 18 , and this polyamide is used in an amount of 2 to 10 wt.% of the block * copolymer.
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    同族专利:
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    ES466246A1|1978-10-16|
    IT7819512D0|1978-01-23|
    FR2378058A1|1978-08-18|
    FR2378058B1|1979-05-11|
    NL175629C|1984-12-03|
    CA1104733A|1981-07-07|
    PL111803B1|1980-09-30|
    引用文献:
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7701886A|FR2378058B1|1977-01-24|1977-01-24|
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