Beteiligte Stoffe
| Rolle | Name | HCID | Einwaage |
|---|
| Edukt | Ethylene | HCID 6325 | — |
| Edukt | Propylene | HCID 8252 | — |
| Edukt | Ethylidenenorbornene | HCID 27756 | — |
| Katalysator | HCID 178420597 | HCID 178420597 | — |
| Lösungsmittel | Toluene | HCID 1140 | — |
| Produkt | Ethene propene ethylidenenorbornene | HCID 168253 | — |
Reaktionsschritte
A 1-liter continuous polymerization reactor was continuously charged hourly with 500 ml of purified toluene, 5×10-3 milligram-atom, as the zirconium atom, of the catalyst component (A) in Example 7 and 2.5 milligram-atom, as the aluminum atom, of the catalyst component (B) synthesized in Example 7. Furthermore, 150 liters/hr of ethylene, 100 liters/hr of propylene and 1.2 g/hr of 5-ethylidene-2-norbornene (ENB) were simultaneously fed into the reactor continuously, and polymerized at a temperature of 20° C. under atmospheric pressure with a residence time of 1 hour while the concentration of the polymer was maintained at 17 g/liter. The resulting polymer solution was worked up in the same way as in Example 7 to give an ethylene/propylene/ENB copolymer having an ethylene content of 83 mole %, an MFR of 3.59 g/10 min., an Mw/Mn of 2.10 and an iodine value of 13. The activity was 1,700 g of polymer/milligram-atom of zirconium.
Herkunft & Nachweise
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|
| Patentnummer | US05700750 |
|---|
| Quelldatensatz | uspto-grants-1997_12 |
|---|
| ORD ID | ord-41a0342401244dcaac71b12bcf4822e8 |
|---|
| Quellennotiz | uspto-grants-1997_12 |
|---|