Method for measuring crosslinking density of molded article of crosslinked thermoplastic polymer foam and molded article of crosslinked foam
A thermoplastic polymer, cross-linking density technology, applied in shoemaking machinery, using stable tension/pressure to test material strength, measuring devices, etc., can solve problems such as effective network chain structure identification
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Embodiment 1
[0170] (1) Preparation of co-catalyst carrier
[0171] In a reactor with a stirrer after nitrogen replacement, put silicon dioxide (Sylopol948 manufactured by Davison Company; 50% volume average particle diameter=59 μm; pore volume=1.68ml / g; specific surface area = 313m 2 / g) 0.36 kg and 3.5 liters of toluene were stirred. Then, after cooling to 5°C, 0.15 liters of 1,1,1,3,3,3-hexamethyldisilazane and 0.2 liters of toluene were added dropwise over 30 minutes while keeping the temperature in the reactor at 5°C. mixed solution. After completion of the dropwise addition, the mixture was stirred at 5° C. for 1 hour, then heated up to 95° C., stirred at 95° C. for 3 hours, and filtered. The obtained solid content was washed 6 times with 2 liters of toluene. Then, 2 liters of toluene was added to make a slurry, which was allowed to stand overnight.
[0172] Into the slurry obtained above, 0.27 liter of a hexane solution of diethylzinc (diethylzinc concentration: 2 mol / liter) w...
Embodiment 2
[0181] (1) Pressurized cross-linked foam molding
[0182] Except for changing the chemical foaming amount to 2.2 parts by weight, kneading was carried out under exactly the same conditions as in Example 1, and pressure crosslinking and foaming were performed to obtain a crosslinked foamed molded article (2). Table 3 shows the evaluation results of the physical properties of the obtained cross-linked foamed molded article, as well as the evaluation results of the cross-linking density and the gel fraction.
Embodiment 3
[0184] (1) Manufacture of ethylene-α-olefin copolymer
[0185] Using the prepolymerized catalyst component (1) obtained in Example 1, ethylene and 1-hexene were copolymerized in a continuous fluidized bed gas phase polymerization apparatus to obtain a polymer powder. In terms of polymerization conditions, the polymerization temperature is 84° C., the polymerization pressure is 2 MPa, the molar ratio of hydrogen to ethylene is 0.38%, and the molar ratio of 1-hexene to the sum of ethylene and 1-hexene is 2.0%. In order to keep the gas composition constant during the polymerization, ethylene, 1-hexene and hydrogen were continuously supplied. In addition, the above-mentioned prepolymerized catalyst component and triisobutylaluminum were continuously supplied to keep the total powder weight of 80 kg in the fluidized bed constant. The average polymerization time was 4 hr. The obtained polymer powder was extruded using an extruder (LCM50 manufactured by Kobe Steel Co., Ltd.) under ...
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