• 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:
    An elastomeric fluoropolymer having improved low temperature properties is provided. The composition contains polymerized units of 57-61 weight % vinylidene fluoride, 27-31 weight % hexafluoropropene, and 10-14 weight % tetrafluoroethylene.
    公开号:SU865129A3
    申请号:SU782620282
    申请日:1978-05-30
    公开日:1981-09-15
    发明作者:Август Стьюарт Клэр (Младший)
    申请人:Е.И.Дюпон Де Немур Энд Компани (Фирма)；
    IPC主号:
    专利说明:

    one
    The invention relates to polymer chemistry, namely to a process for the preparation of a copolymer of vinylidene fluoride, hexafluoropropylene and tetrafluoroethylene. The known method is the obtained fluorine-containing copolymer by copolymerizing tetrafluoroethylene, vinylidene fluoride and hexafluoropropylene containing these compounds in the following molar ratios: 5:85; 7: 9/3 and 30:54:16
    D.1.
    The closest to the invention is a method for producing a fluorine-containing copolymer by copolymerizing vinylidene fluoride, hexafluoropropylene and tetrafluoroethylene in the presence of water in the presence of ammonium persulfate at 40-140 ° C and 1.4-14.0 atm, containing 10-30% by weight of tetrafluoroethylene (TFE) and 90 -70% by weight of vinylidene fluoride (HF1) and hexafluoropropylene (HFP), which in turn are contained in a weight ratio of (1.6: 1.0) to (4.0: 1.0)
    The aim of the invention is to improve the physicochemical properties of the final product.
    The goal is achieved by carrying out the copolymerization, wt.%: Vinyl-30
    denfluoride 58-59 hexafluoropropylene 28-30 and tetrafluoroethylene 12-14.
    Example 1. In an autoclave with a capacity of 2 liters, equipped with a mechanical stirrer, maintain a temperature of 105 s and a pressure of 6.3 atm. Bi autoclave was charged with the following ingredients: 4 L / h of water containing 2.17 g / L of ammonium persulfate and 0.43 g / L of sodium hydroxide; 4 l / h of water containing 0.7 g / l of diethyl malonate; 2210 g / h of a mixture of compressed gases containing 12% TPV, 59% VF2 and 29% HFP. After several cycles of changing the contents of the autoclave, the liquid effluent from the reactor is collected and treated with a solution of potassium-containing aluminum sulfate. The resulting rubbery crumb is separated. The crumb is washed with water and dried in a heater through which air circulates. By measuring the amounts of raw materials and unreacted monomers (61 g / h) which are separated from the effluent stream, and the composition of the effluent stream, which is determined by gas chromatographic examination (1 cubic ml of TFE, 34 mol.% HF, 65 mol. % HFP) ,, set the composition of the polymer, weight ...%:
    TFE 12; WF1 B.O. and HFP 28. The resulting polymer has a Mooney score of 93.
    EXAMPLES. 2-17. Polymers, the results of which are given in table. one,. carried out in accordance with the method described in example 1. The exception is examples 5-7, where the temperature is under {and the nominal time varies between 9-30 minutes (the total amount of water varies from 13.3 up to 4.0 l / h). It is necessary to carry out compensating changes in the amount of the catalyst in order to obtain comparable molecular weights.
    C) table. Table 2 shows the glass transition temperatures of the crude polymers obtained in Examples 1-17, which are measured using differential scanning calorimetry, and the temperature of the cured sample has a torsional modulus of 69 atm measured using the Cless Verge method. In accordance with this method, 100 weight, h. the copolymer sample is mixed using a rubber plant with the composition, parts by weight: thermal carbon black 30j active magnesium oxide 3; calcium oxide hydrate 6 benzyltriphenylphosphonium chloride 0.6 and 2,2-bis (para-hydroxyphenyl) -hexafluoropropane 1.35. These compounds are placed in a mold for 10 minutes, where the temperature is maintained at ± 77 ° C, and then subjected to heat treatment in a furnace through which air circulates, for 24 hours at. glass transition temperatures and Klash-Berg temperatures are measured by measuring the limiting temperature at which the polymer still retains its degree of elasticity during the cooling process. Besides, in
    tab. Table 2 shows the residual compressive strain data, which are measured on similarly vulcanized samples (70 hours at, the final thickness is measured at 0 ° C). The samples are then allowed to warm to room temperature and each sample is classified as good if the residual strain is less than 20%, and measurements are taken within 1 hour as the sample temperature reaches room temperature or the residual strain is less than 10% after , as the sample is at room temperature for 8-12 hours (measurement takes at least 16 hours) and bad if the residual deformation exceeds the above values.
    The polymers of comparative examples 9-10 have intensive crystallization in accordance with the differential scanners of an calorimetric test, and the sample from comparative example 14 has a less intensive crystallization. Thus, the aforementioned samples are not suitable for use with low teratras.
    As can be seen from the table. 2, the copolymers obtained by this method have higher non-glass transition temperatures. compared with the copolymers of comparative examples 8 and 14-17. The copolymers prepared in Examples 9-14 are not suitable for use at low temperatures because of their crystallinity at room temperature, or the crystallinity associated with residual deformation.
    The content of copolymers, wt.%
    2
    3
    four .
    five
    6
    7
    Table 1
    28 30 29 29 29 29
    58 58 59 59 59 59
    14 12 12 12 12 12
    Continued table. one
    -25
    -26
    -26
    -23
    -22
    -23
    -23
    The final thickness is measured at.
    权利要求:
    Claims (1)
    [1]
    1. US patent No. 3801552, cl. 260-80.77, publ. 1972.
    2. Issuance of Japan No. 48-18957, published. 1973 (prototype
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    同族专利:
    公开号 | 公开日
    GB1600940A|1981-10-21|
    IT7824003D0|1978-05-30|
    IE781074L|1978-11-30|
    DK237478A|1978-12-01|
    NL171712C|1983-05-02|
    DK147497B|1984-09-03|
    US4123603A|1978-10-31|
    IT1096613B|1985-08-26|
    FR2393012B1|1980-10-31|
    DE2823179C2|1986-01-16|
    JPS621965B2|1987-01-17|
    SE439489B|1985-06-17|
    NL7805923A|1978-12-04|
    DE2823179A1|1978-12-07|
    BE867619A|1978-11-30|
    DK147497C|1985-03-18|
    SE7804128L|1978-12-01|
    AU523479B2|1982-07-29|
    CA1103398A|1981-06-16|
    NL171712B|1982-12-01|
    LU79728A1|1979-02-02|
    FR2393012A1|1978-12-29|
    IE46834B1|1983-10-05|
    JPS53149291A|1978-12-26|
    AU3663078A|1979-12-06|
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    US4141874A|1975-11-15|1979-02-27|Daikin Kogyo Co., Ltd.|Fluorine-containing elastomeric copolymers, process for preparing the same and composition containing the same|US4346710A|1978-06-16|1982-08-31|Pennwalt Corporation|Article for storage and transport of biogenic fluids|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/801,567|US4123603A|1977-05-31|1977-05-31|Fluoroelastomer composition|
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