• 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:
    1384100 Extrusion polymerizing RHONEPOULENC SA 22 Dec 1972 [27 Dec 1971] 59521/72 Heading B5A [Also in Division C3] A kneader 2 equipped with an extrusion screw, which does not have a dead zone during the forward movement of the material, i.e. once the material has entered the kneader there is no space available for it to remain static, is used in a continuous process for the preparation of a thermosetting resin from an N,N<SP>1</SP>-bis-maleimide andbis-(4-amino-phenyl)-methane. The kneader may contain two helical feed screws which engage intimately in one another and turn in the same direction. Alternatively the kneader may comprise a helical feed screw with an interrupted thread which simultaneously executes an axial rotational movement and an oscillating movement in the direction of the axis, provided in a jacket or housing containing teeth adapted to co-operate with the interrupted thread of the screw. In the apparatus used in the examples, the kneader comprises a helical feed screw formed by a suitably driven shaft carrying interrupted helicoidal threads, the interruptions forming separate flights. The screw is housed in a body comprising three adjacent, coaxial, cylindrical, double-walled heating jackets; the internal wall of the kneader carries projections in the form of teeth.
    公开号:SU843761A3
    申请号:SU721869483
    申请日:1972-12-27
    公开日:1981-06-30
    发明作者:Жерар Бернар
    申请人:Рон-Пуленк С.А. (Фирма)；
    IPC主号:
    专利说明:

    (54) METHOD FOR OBTAINING THERMALLY CONFIRMED PRE-POLYMERS
    Count; gostvo reagents are usually such that oi ;; jOiiJeHHe
    - the number of g-mole of bis-maleinimide
    „: C
    the number of g-mole diamine is enclosed in the range from .1 to 5..
    For convenience of execution, it is preferred to use bis-maleimide in Bnede particles with sizes of 0.1-5 mm. Its supply to the mixer is controlled by means of known devices for this purpose, such as metering screws or scales.
    Bis- {amino-4-phenyl) -methane is loaded in the liquid state into the mixing zone, it can be supplied with the help of a metering pump. The diamine is usually preheated to 100-130 ° C and served at one or several set points, preferably after the bis supply zone -imida
    Maintaining the desired temperature in the mixing zone is usually provided by controlled heating of the mixer body used. In addition to this, it is also possible to produce controlled heating of the screw or screw screws of the apparatus. Heating of the casing can be carried out evenly throughout its length, but it is also possible to have non-slip adjacent heating zones that impart a temperature to the mixing zone, for example, increasing in the direction of the substance. Before the first feed point of the diamine, it is preferable that the temperature be in the range of 20-130-C.
    The residence time of products in the mixing zone may vary somewhat. Depending on the bis-maleimide used, on the temperature adopted and on the weight ratio of the reagents used, and is usually 1-30 minutes. If the bis-maleinimide is N, N-4,4-diphenylmethane-bis-; α-maleimide and if the ratio (1) is close to 2.5, then a preprlimer with viscosities of 0; 5-3 Ro is obtained (measured in a 45% solution of N-methyl pyrrolidone), at a prepolymerization temperature and a residence time of 5- 20 minutes. Under the same conditions, the reaction time can be shortened by adding a strong catalyst. acid. It is also possible to carry out the reaction in the presence of trimellitic anhydride.
    The proposed method is also suitable for the preparation of prepolymers containing fillers, in particular sprayed particles. These particles can be introduced continuously, for example, together with maleimide or at any other point in the mixing zone.
    Example 1. A Buss laboratory mixer is used, known as KO-Ma I axeur type. 58 which has a screw screw formed by a shaft having a spiral intermittent thread, with the gaps forming individual blades; this screw is driven by an appropriate mechanism. The screw is located in a housing consisting of three cylindrical coaxial shells adjacent to a double wall; The internal wall of the mixer housing is provided with teeth shaped protrusions. The screw is set in rotational motion and at the same time in oscillatory motion in the direction of its axis, which ensures mixing of the substances in both directions.
    Water is circulated in the inner membrane at 20 s, in the other two streams, heated to 145 ° C. The rotation speed of the screw is 33. rpm.
    N, N-4,4-diphenylmethane-bis-maleinimide is introduced into the first part of the mixer (corresponding to the first shell) through a dosing scale at the rate of 1800 g / h, bis-maleicimide is introduced in a crushed state, the average size of the granules O , 25 mm.
    Bis- (amino-4-phenyl) -methane is introduced into the second part of the mixer, at 403 g / h. A prepolymer with a softening point is obtained at the exit of the apparatus. The average residence time of the substance in the mixer is 6 minutes. After finishing it up, a prepolymer sample is used for coating by pouring metal conductors.
    EXAMPLE 2 The process is carried out analogously to Example 1, but feeding in the form of a thin mixture of bis-imides and trimellitic anhydride at a rate of 2.5 wt.% Based on the weight of the bis-imide mixture is fed at a rate of 1800 g / h.
    At the exit of the apparatus, a prepolymer is obtained, with a softening point with a viscosity of 1.6 Ro (measured in 45% N-methylpyrrolidone),
    45% by weight of the prepolymer solution in M-methylpyrrolidone is used to coat the glass fabric of the atlas type at a rate of 308 g / m, after which treatment is performed with 1 g of aminopropyltriethoxysilane. Impregnated fabric contains 35 g of prepolymer per 65 g of fabric; the fabric is dried in a ventilated environment at 15 min. Then 12 squares are cut (15x15 cm which are laid one on another and placed between the press plates at 100 ° C. A pressure of 60 Qap is created between the plates, and the temperature between them is raised to 30 minutes. These conditions are maintained for another hour, and then during cooling under pressure, the layered material is released at.
    权利要求:
    Claims (2)
    [1]
    After additional heat treatment at 250 ° C for 24 hours, the laminate has a flexural strength of 54 kg / mm at 38 kg / m at. After thermal stress at 1000 h, this strength is respectively 38 and 27 kg / mm. Example 3. A Buss industrial mixer, known under the name KO-Malaxeur type PR 140, is used. |, With a slight difference, this apparatus has the same elements as Example 1. All three shells are supplied with flows whose temperature is respectively 20, 130 and 160 ° С. Screw speed 40 rpm. The bis-imide is supplied at the rate of 24.9 kg / h in the form of a fine mixture with angiridam of trimethyl jitic acid (625 kg / h). Bis- (amino-4-phenyl) methane is preheated to 125 seconds and served at the rate of 5.6 kg / h. The residence time of reagents in the mixer is 7-8 minutes. At the exit, a prepolymer is obtained with a softening point of 76 ° C. The method of obtaining thermosetting prepolymers by the reaction of N, M-bis-maleimide and aromatic diamines with heating, characterized in that, in order to intensify the process, the reaction is carried out in a screw mixer, and the bis-maleimide is introduced in a fine state, and the aromatic diamine is in the molten state. Sources of information taken into account in the examination 1.Patent of France 1555564, cl. C 08 g 20/00, 1965 (prototype).
    [2]
    2.Fisher E.Zh. Extrusion plastics. Interscience RM, 1964, p. 104-108.
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    同族专利:
    公开号 | 公开日
    DE2263526C3|1980-07-03|
    NL7217291A|1973-06-29|
    USB317080I5|1975-01-28|
    NL146858B|1975-08-15|
    CA990890A|1976-06-08|
    AT322214B|1975-05-12|
    BR7208976D0|1973-09-25|
    CH547323A|1974-03-29|
    BE793362A|1973-06-27|
    LU66747A1|1973-07-18|
    SE435631B|1984-10-08|
    JPS4885689A|1973-11-13|
    DE2263526B2|1979-10-18|
    FR2165722A1|1973-08-10|
    DE2263526A1|1973-07-12|
    IT972951B|1974-05-31|
    US3925324A|1975-12-09|
    GB1384100A|1975-02-19|
    FR2165722B1|1974-08-30|
    JPS525959B2|1977-02-17|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    FR956605A|1943-07-24|1950-02-02|
    FR1555564A|1967-07-13|1969-01-31|
    DE1954878B2|1968-11-05|1972-03-02|Toray Industries, Ine , Tokio|PROCESS FOR THE PRODUCTION OF SHAPED BODIES BASED ON POLYCONDENSATES CONTAINING IMIDE GROUPS|JPS5520195Y2|1976-03-19|1980-05-14|
    JPS6131653Y2|1979-06-11|1986-09-13|
    US5521014A|1981-11-13|1996-05-28|The Boeing Company|Extended multidimensional ether or ester oligomers|
    US5969079A|1985-09-05|1999-10-19|The Boeing Company|Oligomers with multiple chemically functional end caps|
    US5610317A|1985-09-05|1997-03-11|The Boeing Company|Multiple chemically functional end cap monomers|
    US5210213A|1983-06-17|1993-05-11|The Boeing Company|Dimensional, crosslinkable oligomers|
    US5159055A|1983-06-17|1992-10-27|The Boeing Company|Coreactive oligomer blends|
    US5516876A|1983-09-27|1996-05-14|The Boeing Company|Polyimide oligomers and blends|
    US5705598A|1985-04-23|1998-01-06|The Boeing Company|Polyester sulfone oligomers and blends|
    US5618907A|1985-04-23|1997-04-08|The Boeing Company|Thallium catalyzed multidimensional ester oligomers|
    FR2609467B1|1987-01-09|1989-06-09|Rhone Poulenc Chimie|THERMOSETTING COMPOSITIONS BASED ON IMIDE AND EPOXY GROUPS|
    US5512676A|1987-09-03|1996-04-30|The Boeing Company|Extended amideimide hub for multidimensional oligomers|
    US5817744A|1988-03-14|1998-10-06|The Boeing Company|Phenylethynyl capped imides|
    US5693741A|1988-03-15|1997-12-02|The Boeing Company|Liquid molding compounds|
    US5115087A|1988-03-29|1992-05-19|The Boeing Company|Coreactive imido oligomer blends|
    JPH03295773A|1990-04-12|1991-12-26|Daisuke Fujii|Running ship carrier for seashore|
    JPH03295772A|1990-04-12|1991-12-26|Daisuke Fujii|Running ship carrier for seashore|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7146753A|FR2165722B1|1971-12-27|1971-12-27|
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