Peroxide cross-linked fluorine-containing elastomer composition
A peroxide and elastomer technology, which is applied in the field of peroxide crosslinked fluoroelastomer compositions, can solve the problems of deterioration of compression set resistance, increase of CSM dosage, deterioration of elongation, etc., and achieve the goal of reducing viscosity Effect
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[0267] Next, examples are given to illustrate the present invention, but the present invention is not limited to the examples.
[0268]
[0269] Device: HLC-8020 (manufactured by Tosoh Corporation)
[0270] Column: GPC KF-806M 2pcs
[0271] GPC KF-801 1 piece
[0272] GPC KF-802 1 piece
[0273] Detector: Differential Refractometer
[0274] Developing solvent: tetrahydrofuran
[0275] Temperature: 35°C
[0276] Sample concentration: 0.1% by weight
[0277] Standard samples: various monodisperse polystyrenes ((Mw / Mn)=1.14(Max)), TSKstandard POLYSTYRENE (manufactured by Tosoh Corporation)
[0278]
[0279] The Mooney viscosity is measured in accordance with ASTM-D1646 and JIS K6300-1.
[0280] Measuring machine: Automatic Mooney viscometer manufactured by Uejima Seisakusho Co., Ltd.
[0281] Rotor speed: 2rpm
[0282] Measurement temperature: 100°C (60°C for some)
[0283]
[0284] Device: GPCmax-TDA302 system (Viscotech)
[0285] Detectors: RI (Differential Ref...
reference example 1
[0322] Reference example 1 (production of branched fluoroelastomer (A-1))
[0323] In a polymerization tank having an electromagnetic induction stirring device as a stirring device with an internal volume of 3 liters, add pure water 1730g, C 5 f 11 CHOONH 4 1.73g, 2,3,3,3-tetrafluoro-2-[1,1,2,3,3,3-hexafluoro-2-(1,1,2-trifluoroallyloxy)propoxy Base] Propionic acid ammonium salt 0.173g, after fully replacing the inside of the system with nitrogen gas, the pressure was reduced. This operation was repeated 5 times, 35 g of VdF, 42 g of TFE, and 1090 g of HFP were added under reduced pressure, and the temperature was raised to 80° C. while stirring. Next, inject 0.24 g of APS dissolved in 10 g of pure water with nitrogen pressure to initiate polymerization, and continue polymerization under the conditions of (a), (b), (c), (d), and (e) for 4 hours Finally, the stirring was stopped, the monomer was released, and the polymerization was stopped.
[0324] (a) Using Aspen Plus Ver...
reference example 2
[0331] Reference Example 2 (Manufacture of branched fluoroelastomer (A-2))
[0332] Within the conditions of (d) among the conditions described in Reference Example 1, 1.45 g of octafluoro-1,4-diiodobutane (0.26 parts by mass relative to 100 parts by mass of the fluoroelastomer), IM single Body (CF 2 = CFOCF 2 CF 2 CH 2 1) 5.1 g (0.85 parts by mass relative to 100 parts by mass of the fluoroelastomer as the target product), except that, in the same manner as in Reference Example 1, a branched-chain fluoroelastomer (A- 2).
[0333] The weight of the obtained emulsion was 2182 g, and the polymer concentration was 27.6% by mass. In addition, the amount of the fluoroelastomer was 602 g, the weight average molecular weight Mw measured by GPC was 179,000, the number average molecular weight Mn was 101,000, and Mw / Mn was 1.76. Also, take advantage of 19 The composition of the polymer measured by F-NMR was VdF / TFE / HFP=51 / 20 / 29 (mol%). The Mooney viscosity at 100°C is 105.
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