• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
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    • 专利摘要:
    1509635 Polyamide adhesive powder KUFNER TEXTILWERKE KG 28 July 1976 [28 July 1975] 31421/76 Heading C3R Polyamide hot melt adhesive powders are mixed with at least one melting point and/or melt viscosity depressing agent in powder form, e.g. toluene sulphonamide or caprolactam, and tempered until the agent is completely uniformly distributed and diffused into the polyamide granules. The product is suitable for spray application and permits a higher loading of agent with less reduction in bond strength than single powder mixtures.
    公开号:SU826962A3
    申请号:SU752303211
    申请日:1975-12-24
    公开日:1981-04-30
    发明作者:Хефеле Иозеф
    申请人:Куфнер Текстильверке (Фирма)；
    IPC主号:
    专利说明:

    This invention relates to a process for the preparation of a powdered glue based on copolyamide. It is known to produce modified hot melt powder powders by adding a melt temperature and melt viscosity agent to polyamide powder. Products of this type are used for coating pasting. They consist of a grain mixture of the copolyamide powder obtained by mole with a grain size below 200 (U and of a finely ground powder of an additive — an amide o, p-toluenesulphonic acid (usually trading mixture of amide and p-toluenesulphonic acid) with the size of α-toluenesulfonic acid below 20ju. These commercially available mixtures are obtained by separately grinding both products and mixing them. Thanks to the addition of softener, hot bonding can also be carried out under mild fixing conditions. The disadvantage of these mixtures is that they can be used only for the application of pores to the last, since in the scattering method the grains of polyamide and softener are placed on the carrier without contact, therefore the presence of the additive does not affect the melting point and the viscosity of the melt. Use is possible if the length of the solvent does not exceed 10% by weight. When using large amounts of solvent it is impossible to avoid the gradual formation of voids in the corrugated valgks. However, when making fixed patches that are used to strengthen fur and leather, it is necessary to use higher amounts of softener, since this requires extremely mild conditions of compaction, otherwise the fur and the skin may be damaged. Hot melting adhesives are also known, where the softener is added directly during polyamide polymerization, and then the containing softener is ground into granules 2J. However, a product is of this type, with a higher content of solvent, only with difficulty or not at all. In addition, the use of known powdered polyamide hot melt adhesives does not provide
    Strength of fastening in time. As a rule, the adhesion strength of a heat-welded compound made of coatings, according to the impregnation method with a powder, under pressure of a fabric underlay with a coating, falls within the first 48 hours to about 3/4 of the initial adhesion strength, and then during cleaning - up to 50% of the initial value.
    The purpose of the invention is to simplify the technology and improve the quality of the product.
    This goal is achieved by the fact that powdered copolyamide with an initial melting point of 80-145 ° C and a powdered additive that lowers the melting point and viscosity of the melt with an initial melting point of 50-110 ° C, is maintained at a temperature from 55 ° C to above the beginning of the final product until uniform distribution of the additive in the copolyamide powder. The mixture, which is subjected to heat treatment and has a different grain composition, consists of 40-97 wt.% Copolyamidium powder and 3-60 wt.% Of a poro1-like additive.
    During the tempering process, under these conditions, the initially powdered additive diffuses into the copolyamide grain, and after the tempering process, which takes from several hours to several days, is completed, a homogeneous final product can be obtained in powder or very easily converted into powder. homogeneous properties and each originally existing copolyamide grain is permeated with an additive.
    In comparison with the initial mixture, when dispersing, different fractions of the grain are almost not established or only too small differences are established between the individual fractions. Copolyamide free grains are absent or barely present. At a processing temperature of about 70 ° C, this state is reached in 70-120 hours and at a temperature of about 10-18 hours, if polyamide grains of 50-200 / U are used.
    While the grain size of the applied additive is usually small and on average lies below the grain diameter of the soptelyamide powder lies in the region of an average of 120,350 tons. To the modified powder obtained by the proposed method, an adhesive that is suitable for coating the elastic substrate by a powder method or method spraying, as well as for coating other objects by the vortex spraying method, in some cases other additives may also be added.
    for example hardener, fillers, pigments or optical brighteners.
    Suitable for reducing the melting point and melt viscosity in powder form for heat treatment with copolyamides are, for example, amide o, p-toluenesulfonic acid, cyclohexylamide o, p-toluenesulfonic acids, caprolactam, etc.
    Known emollients may contain up to 60% by weight of the mixture. f Other substances can be contained in the mixture only within certain limits of the molecularly homogeneous absorption into the polyamide, which also lower the melting point and viscosity of the melt, for example, phthalic acid dicyclohexyl ester and fatty acids (palmitic and stearin), as well as their mixtures, stearin or wax acids, oxidized polyethylene or oxidized ozocerite in an amount of 5-10 wt.%. Stearin, a sparingly absorbed agent, prevents the adhesion from falling well. Additives may be contained in the mixture either alone or in mixture with each other. It is advantageous to use several additives.
    The tempering of both powdered components (polyamide and melting point lowering and melt viscosity of the agent) is carried out appropriately under the influence of temperature in a stationary or only weakly mobile state, since there is little danger of sintering. With weak motion with minimal shear forces, it is possible to temper a slowly rotating tube, into the upper end of which the initial mixture is introduced, and from the lower end the finished tempered end product is withdrawn
    The copolyamides used are obtained by known methods by copolymerization and co-condensation of diamines, dicarboxylic acids, amino acids and lactams. These polymers contain, part of the residual monomers, mainly CaproLacts1M in an amount of about 5 wt.%. When grinding and sowing, the usual in the trade of copolyamides, as a rule, are added excipients based on fatty acid salts of alkaline earth metals in an amount of 0.01-0.05 weight. which are necessary when tempering. At the end of the process, these salts are additionally added. Up to 1% in those cases if the obtained polyamide powder has a low melting point and is intended for raster-like powder application under pressure.
    In order to carry out the process, the complete distribution of the additive in polyamide powder is necessary, since its super-high concentration prevents the formation of lumps. At the end of the process, it receives an easily disintegrating or weakly adhering powder mixture, which can easily be separated by applying weak mechanical forces to the primary grains. The remaining (less than 3% heavily crumpled sintering part can be separated by suction. During the sieve analysis, it is established that the copolymer grains grow during the tempering process and the grain spectrum is shifted to a higher grain diameter. The grain growth corresponds to an increase in volume based on quantities of the substance added. Although one would expect the melt powder to be present in the presence of lower melting point of the softener taken in large quantities as a result of the tempering process around the melt point It will bake to form lumps that are not transferred to a powdery state, however, with an increase in the proportion of softener, there is no difficulty in applying coatings. Moreover, using the proposed method, a slowdown in the adhesion is achieved. Slowing occurs not only after storing the fixed composition , but also when cleaning parts of clothing. The most acceptable are gaskets with a very low melting point of the coating for fixing natural and artificial fur. Example 1. A well-dispersed mixture of 850 h (85%) of 6/6,6 / 12-copolyamide powder 50 h (5%) of dicyclohexyl- is obtained. phthalic acid ester and 100 h (10%) of an amide o powder, p-toluenesulfonic acid. Both finely ground additives from phthalic acid dicyclhexyl ester and amide o, p-toluenesulfonic acid have an average grain size below 20 | U. Unmixed copolyamide powder has a monomeric ratio,%: laurinectam about 30, caprolactam about 40, and hexamethylenediamonium adipate about 30. Grain-size composition,%: Higher ISOiU0,4 180-250 p117.0 125-180 (U34.0 90-125 (U43, 0 Below 60fu0.6 Melting point approx. Melt viscosity, P: 120 ° C200000 ISO C120000 UQ C70000 The mixture is kept in a plastic bag for 15 hours and then left to cool. After 2-3 days, the tempered mixture crystallizes and breaks down at slightly rubbing motion into powder. The tempered product is sieved through a 300-brush sieve. About 2% of the residual residue remains. The particle size analysis of the sifted powder gives the following particle size,%: Higher than 250012,5 180-250 fU27.0 125-180 (U32.0 90-125 (U34.0 60 -90, 0 below 60 (I0.5 Melting point about 108 ° C. Total melt viscosity, П; at 110 ° С200000 at 120 ° С90000 with IBO C32000 at 140 ° С17500 Melt viscosity of a part of grains, P: Above 180 ( U at 130 ° С at 140 ° С Below 90 (u at 130 ° С at 140 ° С Powder is intensively mixed with 0.05% of magnesium stearate. The resulting easily flowing mixed 11-mesh triturated product in the form of dots was sprayed onto a staple cotton cloth pad with a weight of about 110 g / m. The weight of the powder was about 21 g / m. In parallel, an amount of a coating of pure copolyamide powder without an additive is applied to the same pad. The table shows the values of adhesion and its loss during installation, the press and the outer wool material at the temperature of the top plate, bottom plate, 15 seconds of fixation and a pressure of 300 g / cm
    There is no difficulty in coating with sintering powder. Example 2. A well dispersed mixture of 300 hours, (49.2%) of 6/6,6 / 12-copolyamide powder, 30 hours, (4.9%) of caprolactam powder is obtained. and 280 h (45.9%) of amide o, p-toluenesulfonic acid powder. Both finely ground additives from caprolactam and amide o, p-toluenesulfonic acid have an average grain size below 20 | U.
    Copolyamide powder. Has the following properties.
    Monomeric ratio,%: loarinlactam, about 30, caprolactam, about 40, and hexamethylenediamonium adipate, about 30.
    Granulometric composition,%: Over 250 (U0.50
    180-250 (U9.0
    125-180 (U29.0
    90-125 (U38.5
    60-90 (1114.0
    Below 6Ord9.0
    Melting point about 116 C. Melt viscosity, P; at 120 ° С140000
    at 130 ° C. 42000 at i4Q ° C. 18000 The mixture is held in a plastic bag for about 80 hours at and then left to cool. After about 3 days, the tempered mixture crystallizes and breaks into a powder with a slight rubbing between the palms. Tempered product Sifted through a 300-brush screen. About 1% of the sieve residue remains on the sieve.
    The granulometric analysis of the powder gives the following granulometric composition,%:
    Above 0
    180-250 (1134.5
    125-180 (4 33.0
    90-125fU22,0
    60-90 (U5.0
    Below 60 (110.5
    Melting point is about 66 ° C. Melt viscosity is total, P: at 70 ° С35000
    at 80 ° С9000
    at 90 ° С4000
    at 100 ° С2000
    Melt viscosity of a part of grains, P: Higher than 180 (at 180 ° С 10000 Below 90 fu at 180 ° С 6000
    The powder is intensively mixed with 0.2% magnesium stearate and crushed in 11 mesh, and applied to a cotton staple fabric pad with a weight of about 80 g / m. The weight of the powder is about 25 g / m.
    The coated gasket is used for hot welding of fur and leather at 85 ° C. Gluing resistant to cleaning
    in perchlorethylene and resistant to washing at 30 ° C.
    Example 3. A well-distributed mixture consisting of 100 parts by weight is made up. (67.5%) quadrupole powder copolyamide, 40 weight.h. (27.0%) current milled o, p-amide of toluenesulfonic acid and 8 weight.h. (5.5% finely ground phthalic acid dicyclohexyl ester.
    A standard powder of quadruple copolyamide 0-200 grit is obtained from monomeric luarinlactam, caprolactam, hexamethylene diammonium adipate and hexamethylene diammonium sebacate with a melting point of 80-85 C.
    The mixture is subjected to heat treatment in a fixed bed for 72 hours at 55 ° C, and then cooled. After 2-3 days, the calcined mixture crystallizes and falls into the pistons with a slight rubbing between the palms. When sifting mechanically loosened calcined material on the brush sieve does not remain sediment. Melting point of progressed material. The obtained powder, unlike the non-calcined powder, can be applied without problems in the form of a point coating.
    The homogeneous mixture at a temperature above the melting point of the copolyamide powder is melted into a uniform melted mass, extruded into strands and cut into granules.
    It is not possible to obtain a nominal required amount of powder even when cooled with liquid nitrogen.
    Example 4. A well dispersed mixture of 96 h (96%) of 6/6, 6/12 copolyamide powder and 4 h (4%) of stearic powder (technical mixture of fatty acids with a high content of stearic acid) is prepared.
    Copolyamide powder has the following properties.
    The ratio of monomers,%: laurinelactam is about 50, caprolactam is about 30, and hexamethylenediamonium adipate is about 20.
    Grading,%:
    Over 250nj0,8
    180-250 (U3.2
    125-180 (U31: 4
    90-125 (U27.4
    80-90 (119.0
    . 60-80 j4,0
    Less than 60 (li14,2
    Melting point is about 134 C.
    Melt viscosity at 4500 P.
    The mixture in the plastic bag is heat treated for about 18 hours at and then cooled. After cooling, the powder disintegrates, sieving is not required.
    Sieve analysis of the powder gives the following particle size distribution,
    Above 250 | Ц1,0
    180-250 (U24.6
    125-180 (U32.0
    90-125 (U24,4
    80-90 (U16,0
    60-80 (U1.6
    Below 60fU 0,2
    Melting point is about 133 C.
    Melt viscosity at 160 ° C, 2500 P.
    As can be seen, the melting point did not change, the melt viscosity undergoes a strong decrease already with an insignificant addition of stearin (4%).
    The powder can be used directly for the application of layers for outerwear. In contrast to the interlayers that are applied using the raw copolyamide powder, the interlayers with the proposed powder are more easily fixed.
    Example 5. A well prepared day mixture of 95 h (95%) of 6/6/12 copolyamide powder and 5 parts (5%) of phthalic acid dicyclohexyl ester is prepared well. The finely ground additive has an average grain diameter of less than 20 ° and the copolyamide powder is qualitatively different from the powder obtained in Example 3.
    The mixture is processed in the same way as in Example 3. Sifting of the heat treated powder is also not required.
    Sieve analysis of the powder gives the following granulometric composition,%:
    Over 250 (110.4
    180-250 (1128.4
    125-i80 (U28,8
    96-125 U 25.4
    80-90fu14,6
    60-80 (U2,4
    Less than 60 "0.2
    Melting point of about 133 ° C,
    Melt viscosity at 2600 P,
    The resulting powder has about the same melting point as the original copolyaglide. Thanks to the treatment also comes very
    a strong decrease in viscosity, to about half the original value. Use powder as in example 3.
    The resulting modified adhesive powders can be applied to coatings on elastic surfaces by pressure and spraying,
    Using the melt glue produced by the proposed method, for example, duplicated fabric and knit pads, lining materials, scrims, foams for producing composite material with outer material of clothing parts, with caps and for collar shirts of outer material, with natural and artificial leather and furs, as well as footwear, for upholstery pads, flooring, curtains, wallpaper, etc. The most promising are fabric, knitwear and linen compounds.
    权利要求:
    Claims (1)
    [1]
    1.Eduard de Jong. Polyamidsehme 1 zk 1 ed s tof f e fi Jr textile Verkledungen - Adhasion, 1975, No. 11, (prototype-).
    2, K, H, Sfukendrock, Chemische grundlagen Textilveredlung, 1971, 6, No. 7.
    类似技术:
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    同族专利:
    公开号 | 公开日
    ATA529476A|1979-11-15|
    AT357250B|1980-06-25|
    FR2321532B1|1979-07-20|
    CH617808B|1900-01-01|
    US4080347A|1978-03-21|
    FR2321532A1|1977-03-18|
    DE2533729A1|1977-02-17|
    MX147774A|1983-01-12|
    BR7604879A|1977-08-09|
    ES450829A1|1977-08-16|
    JPS5217521A|1977-02-09|
    PL109925B1|1980-06-30|
    HU182968B|1984-03-28|
    GB1509635A|1978-05-04|
    DE2533729B2|1979-12-13|
    JPS5837349B2|1983-08-16|
    IT1069520B|1985-03-25|
    CH617808A|1980-06-30|
    引用文献:
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    CA697168A|1964-11-03|D. Brossman Philip|Non-dusting, pigment-coated nylon molding compositions|
    NL87319C|1938-04-11|
    US2992456A|1954-05-10|1961-07-18|British Celanese|Method of compounding finely-divided thermoplastic material with a plasticizer|
    NL95995C|1956-11-14|
    US3156665A|1961-03-06|1964-11-10|Du Pont|Non-dusting pigment with nu-alkyl and cycloalkyl toluene sulfonamide-coated nylon molding compositions|
    DE1569990C3|1963-11-03|1980-09-11|Fa. Carl Freudenberg, 6940 Weinheim|Process for the manufacture of thermoplastic adhesive powders for ironable stiffeners|
    GB1247665A|1968-06-14|1971-09-29|Bondina Ltd|Iron-on interlinings|
    US3591409A|1969-07-28|1971-07-06|Monsanto Co|Process for coating resin granules by high intensity mechanical blending and product obtained thereby|
    BE792495A|1971-12-10|1973-06-08|Stamicarbon|PROCESS FOR THE STABILIZATION OF POLYMERS|
    JPS4883145A|1972-02-09|1973-11-06|
    JPS491653A|1972-04-19|1974-01-09|
    US3948844A|1973-05-12|1976-04-06|Plate Bonn Gesellschaft Mit Beschrankter Haftung|Copolyamides containing caprolactam, lauriclactam and 11-aminoundecanoic acid|
    US3950297A|1973-05-12|1976-04-13|Plate Bonn Gesellschaft Mit Beschrankter Haftung|Copolyamides containing caprolactam, lauriclactam and hexamethylene diamine adipate|US4399246A|1982-08-06|1983-08-16|E. I. Du Pont De Nemours & Co.|Filled polyamide compositions with silanes and sulfonamides|
    US5853864A|1988-06-30|1998-12-29|H. B. Fuller Licensing & Financing Inc.|Composite article resistant to moisture-induced debonding|
    US5026756A|1988-08-03|1991-06-25|Velsicol Chemical Corporation|Hot melt adhesive composition|
    AU8627491A|1990-06-18|1992-01-23|Robert L. Harder|Improved fusible bonding tape and method of manufacture thereof|
    US5141780A|1991-01-02|1992-08-25|Allied-Signal Inc.|Multifilament yarn with adhesive polymer component|
    US5627229A|1992-07-25|1997-05-06|H.B. Fuller Licensing & Financing, Inc.|Hot melt adhesive having controlled property change|
    US20040265504A1|2003-06-27|2004-12-30|Christophe Magnin|Non-metalic substrate having an electostatically applied activatable powder adhesive|
    CN102925098A|2012-11-29|2013-02-13|昆山天洋热熔胶有限公司|Fast-melting polyamide powder hot melt adhesive and preparation method thereof|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE2533729A|DE2533729B2|1975-07-28|1975-07-28|Hot melt adhesive powder and process for their manufacture|
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