反応式
C=C.[CH2:3]=[CH:4][CH2:5][CH2:6][CH2:7][CH3:8]>>[CH2:3]=[CH2:4].[CH2:3]=[CH:4][CH2:5][CH2:6][CH2:7][CH3:8].[CH2:3]=[CH:4][CH2:5][CH2:6][CH2:7][CH3:8]参加物
4
実験手順
Using a stirring-type autoclave-type continuous reactor with an inner volume of 1.5 L, a mixture of ethylene and 1-hexene, as a raw material gas, was continuously supplied in a rate of 40 kg/hr, so that the composition of 1-hexene was 75% by weight, under maintaining pressure inside the reactor at 130 MPa. In addition, the above catalyst solution was supplied continuously by adjusting supply amount thereof so as to maintain polymerization temperature at 150° C. Production amount of the polymer was about 4.3 kg per hour. After completion of the reaction, the ethylene•1-hexene copolymer (PE-1), with a content of 1-hexene of 24% by weight, an MFR of 35 g/10 min, a density of 0.880 g/cm3, and a Mz/Mn of 3.7, was obtained.
後処理
- temperatureunder maintaining pressure inside the reactor at 130 MPa
- temperatureso as to maintain
- custompolymerization temperature at 150° C
- customAfter completion of the reaction
出典と根拠
- ORDレコード
- ord-f3611dc3a1c24601b8ca9b5782248957
- 出典データセット
- uspto-grants-2014_04
- 特許番号
- US08697984B2
関連ノート
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