• 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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  • 优先权
    • 专利摘要:
    Improved melt blending process for preparing block copolymer of poly(4,7-dioxadecamethylene adipamide)-polycaprolactam, which is also known as N-30203-6//6, involves continuing the melt blending until the polymer is characterized in that the maximum amount of the block copolymer recovered from an aqueous formic acid solution containing the dissolved block copolymer exceeds about 90%. Fiber prepared from such a characterized block copolymer does not fuse when scoured in boiling water.
    公开号:SU741800A3
    申请号:SU772545399
    申请日:1977-11-24
    公开日:1980-06-15
    发明作者:М.Томпсэн Роберт；Никэл Стифэн
    申请人:Сантех Инк (Фирма)；
    IPC主号:
    专利说明:

    3741800
    The above reaction 1 is often called cyanoethylation; the interaction takes place between acrylonitrile I and ethnlene glycol II, 1,2-bis (/ 3-cyanoethoxyethane) 111 is formed by tfich. Reaction (2) - hydrogenates compound III with 5 obtaining diamine, i.e. 4,7-dioxadecamethylenediamine IV. Diamine IV is reacted with adicic acid V and salt VI is obtained by reaction (3). Then the salt VI is heated and the water is removed, and polymer VII.y is obtained by NH- (eng) 3 - (g) .7 o- (eng) s-kn-C- (HNg) c- (i where y is 4-200 , z - 200, and the molecular weight of the polymer from 5,000 to 100,000. The resulting block copolymer may contain an antioxidant such as 1,3,5-drimethyl-2,6-tris- (3,5-di-tert- butyl-4-hydroxybenzyl) benzene. Small amounts of antioxidant, such as 0.5 wt.%, give satisfactory results, but you can work and use 0.01-2.0 wt.%. Other antioxidants can also be used. Antioxidants like typically mixed with two polymers before melt blending. Other additives useful for polyamides, such as matting agents and / or light stabilizers, can also be used Example: Preparation of 1,2-bis (| 3-cyanoethoxyethane) NC- (CH2) 20- (CH2) 2-O- (CH2 ) In a double-walled glass reactor with double walls (for cooling with water), a bottom opening for condensation and a stopcock, load 930 g (15 moles) of ethylene glycol and 45.6 g of a 40% KOH solution. Then add dropwise 1620 g (30.6 mol) of acrylonitrile (No.C-CHCHCH2) and stirred at such a rate that the temperature did not rise above 35 ° C. At the end of the addition process, the mixture is stirred for another 1 h, then allowed to stand overnight. After that, the mixture is neutralized to pH 7 by the addition of 6 M potassium chloride. After washing three times with a saturated solution of sodium chloride, the product is separated from the aqueous layer, dried over calcium chloride, and passed through a layer of A jfOs to ensure that all the base material is removed. Yield 90%. Example 2. Preparation of 4,7-dioxadecamethylenediamine NH2- (CH2) 3-0- (CH2) 2-0- (CH2) 3-NH2 150 g of 1,2-bis- (D-daanotoxyethane) are charged to a hydrogenation reactor with a capacity of 800 ml. ), 230 ml of dioxane and about 50 g of cobalt Rene. Then the flask is filled with hydrogen and hydrogen pressure is created by heating to 110 ° C. By hydrogen absorption, another precursor product is N-6 or poly (-caprolactam. This is a commercial product, methods for its production are well known and described in a whole number of publications.
    After melt mixing, thoroughly dried N-30203-6 and N-6 (the best block copolymer N-30203-6 / / 6) corresponds to the structural formula Y (CH2) 5-6 hydrogen is added until constant pressure is reached. After cooling, the pressure is released, the catalyst is filtered. Dioxane is distilled off. The mixture obtained is distilled using a stapled tape distillation unit. The diamine is distilled at 123-124 ° C (3.75 mm Hg. About 98 g of a product of 99.95% purity is obtained. The product is 303203-diamine. Example 3. Production and polymerization of poly (4.7 -dioxadecamethylene adipamide) 30203-6. To a solution of 41.50 g of adicic acid dissolved in a mixture of 250 ml of isopropanol and 50 ml of ethanol with stirring, 50 g of 30203-diamine dissolved in 200 ml of isopropanol are added. An exothermic reaction occurs. polymeric salt. It is filtered on a Buchner funnel and immediately recrystallized 400 ml of ethanol and 300 ml of a yopropanol solution are obtained from a mixture.The product is dried in vacuo overnight at 60 ° C; mp 12JfC, pH of 1% solution is 6.9; 85 g of salt are obtained (92% of theoretical) Approximately 40 g of the polymer salt is loaded into a thick-walled glass tube. After that, the neck of the tube is compressed for sealing purposes, air is removed (filled 5 times with nitrogen). Finally, the tube is heated for 2 hours at 200 ° C in an aluminum block. After cooling, the tip of the tube is broken off, the remaining part is bent at an angle of 45 °, connected to a branched pipeline and dehydrated using nitrogen-vacuo cycles. The tubes are heated at 222 ° C for 6 hours in a nitrogen atmosphere at atmospheric pressure using baths that work with methyl salicylate vapors. Upon cooling, the tubes break, the polymer plug-tube breaks into pieces. Example 4. Smelter polymers in the melt. 5 Two different methods are used to blend the polyamides. 4 test pieces, i.e. Nos. 1-4, are made by feeding dried polymers, i.e. N-30203-6 and N-6, to an extruder. In it, the polymers melt and are fed to a static mixer, where a block copolymer is obtained by mixing and heating at elevated temperature. The table shows the residence time in the mixer and the temperature. The other two samples, i.e., 5 and 6, are made by loading appropriate quantities of dried polymers 30203-6 and nylon-6 into a container with two openings in a rubber test tube. These holes are designed for spiral stirrer and nitrogen inlet. Air is removed from the container. After that, the nitrogen-filled reactor is heated in a liquid-steam bath. The mixture of both polymers is stirred with a spiral stirrer, driven by an air motor for the time required. Before cooling the molten polymer, the broom is removed to drain the polymer. In both methods, the polymers are molded and cured after curing, and then processed to dry the process. Example 5. Polymer stretching and stretching. After melt blending, the polymers N-30203-6 and N-6 pull the threads using a plunger extruder. The test samples are passed through a die with 7 holes w with a diameter of about 0.304 mm and a length of 0.608 mm. Dried samples weighing about 50 g are placed in an extruder, where they are allowed to melt for 25 minutes and reach an equilibrium temperature of 230 ° C. Then, the samples are passed through 40-mesh and 250-mesh stainless steel lattice filters and through the die plate by means of a plunger working from the engine. Samples N-30203-6 and N-6 are spun in the melt at an appropriate feed rate. The threads pass through the die through the guides; they are then collected by winding on paper tubes.
    Fiber adhesion, depending on the solubility of the copolymer in formic acid 006 With the passage of volokia through the device for applying a layer of sorbent, it is coated with a finishing spinning layer commercially available and dissolved in heptane. The device includes nylon felt impregnated with a finishing agent; it is attached to the fiber guides below the die. During the spinning process, the extruder temperature is 225 ° C. Example 6. The adhesion test fibers. The fibers obtained, that is, samples 1-6, are put into tubes and placed in boiling water. They are then removed from the boiling water and diluted to determine the relative degree of sticking together. These results are shown in the table. Even with a small degree of sticking together, the fiber is not suitable for sale. Example 7. Characterization of the block copolymer. The test samples 1-6 are tested for their fractionated precipitation in formic acid. In total, the method is as follows: 1 g of dry copolymer, that is, N-30203-6 // 6 is weighed with an accuracy of 0.1 mg. The one gram sample is dissolved in standard formic acid (90%). The resulting solution is diluted with distilled water, for example, to a 55% concentration relative to formic acid of the indicated percentage. The solution is allowed to stand at room temperature for 3 hours, then filtered. The combined precipitate is washed with water, dried and weighed to determine the content of substance in %% at a given concentration of formic acid. Then, a graph is plotted, plotting on the bdna the axis of coordinates, the amount of the sample in %% allocated at different concentrations of formic acid. Each sample has a different solubility in formic acid. With the help of the graph, the concentration of formic acid is obtained with the) isolation of the dissolved polymer. These values are also listed in the table. Table
    260
    ten
    260
    Big
    54,8
    80.4
    Large
    78,8
    54.6 The table shows the results of tests of various samples. As follows from the data presented in the table, with a decrease in the concentration of formic acid with a 50% separation of the copolymer, for example, within 54.8-54-3%, it decreases with the number of adherent fibers. When the formic acid concentration is reduced to 50.7%, the slipiness is not observed at all. Thus, it can be concluded that if the concentration of formic acid at 50% recovery of the copolymer below 50.7% sticking together does not cause fiber to flow. Similarly, as soon as the maximum amount of copolymer recovered exceeds 90.6%, no more slipping of the fiber occurs. When more than 90.6% of the copolymer is isolated from the formic acid solution, fiber sticking also does not occur.
    权利要求:
    Claims (1)
    [1]
    Continuation of the Table Similar results are obtained when preparing N-30203-6 // 6 block copolymers from N-30203-6 and N-6j taken in a different ratio. DETAILED DESCRIPTION A method for producing a polyamide block copolymer by melt blending poly (4,7-dioxadecamethylene adipamide) and polycaprolactam, wherein in order to obtain a block copolymer having improved spin properties, mixing is continued until the maximum amount of block copolymer the copolymer released from its solution in concentrated formic acid when diluted with water is no less than 90.6, weight%. Sources of information taken into account during the examination 1. Belgium patent No. 822104, cl. C 08 d, pub. 1974 (prototype).
    类似技术:
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    同族专利:
    公开号 | 公开日
    FR2372186B1|1984-06-08|
    GB1597244A|1981-09-03|
    DE2752683A1|1978-06-01|
    SE7713312L|1978-05-27|
    NL7712225A|1978-05-30|
    DK153557B|1988-07-25|
    MX145741A|1982-03-26|
    DK524477A|1978-05-27|
    CA1106994A|1981-08-11|
    JPS647090B2|1989-02-07|
    BE861139A|1978-05-24|
    SE436363B|1984-12-03|
    DK153557C|1988-12-27|
    DE2752683C2|1991-01-24|
    IT1088556B|1985-06-10|
    US4045512A|1977-08-30|
    JPS53114897A|1978-10-06|
    FR2372186A1|1978-06-23|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2577621A|1948-08-03|1951-12-04|May Geoffrey Bilson|Production of polyamides of high molecular weight utilizing 1:4-bis--cyclohexane|
    DE1520933B2|1964-05-23|1974-05-09|Schering Ag|Process for the production of copolyamides and their use as hot-melt adhesives|
    US3392253A|1965-05-24|1968-07-09|Robertshaw Controls Co|Thermosetting switch support with thermoplastic bearing|
    US3397107A|1965-07-22|1968-08-13|Kanegafuchi Spinning Co Ltd|Composite polyamide filaments with improved potential crimpability and method of making the same|
    GB1180403A|1966-02-11|1970-02-04|Toyo Rayon Co Ltd|Polyamide Resin Composition|
    DE1720217A1|1966-06-22|1970-06-04|Asahi Chemical Ind|Process for making block copolymers|
    DE1595758A1|1966-08-02|1970-02-12|Glanzstoff Ag|Process for the production of polyamides with Aether bonds|
    US3393252A|1967-04-19|1968-07-16|Du Pont|Melt blend of polyamides|
    US3729449A|1969-08-27|1973-04-24|Kanegafuchi Spinning Co Ltd|Polyamide fibers composed of the polyamide and methods for producing thereof|
    US3863609A|1972-09-19|1975-02-04|Yoshio Ikarashi|Rotary engine|
    US3882090A|1973-06-04|1975-05-06|Eastman Kodak Co|Water-soluble polyamides from alkyleneoxy bis|
    IN142629B|1973-11-14|1977-08-06|Sun Ventures Inc|US4165346A|1976-11-26|1979-08-21|Sun Oil Company Of Pennsylvania|Copolymer of poly-polycaprolactam containing terephthalic acid|
    US4235714A|1978-12-18|1980-11-25|Suntech, Inc.|Hydrophilic polyamide film for semipermeable membranes|
    US4297454A|1979-11-14|1981-10-27|Suntech, Inc.|Manufacture of a block copolymer containing a polyetheramide and a polylactam|
    US4328331A|1981-04-20|1982-05-04|The Upjohn Company|Novel polyester-amides|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/745,320|US4045512A|1976-11-26|1976-11-26|Melt blending polyamide process|
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