HuagongsheHuagongshe Chemistry Print Report · For research reference only
Ethylene → ethylene/propylene VNB
Participants
| Role | Name | HCID | Charge |
|---|---|---|---|
| Reactant | Ethylene | HCID 6325 | — |
| Reactant | Diethylaluminum chloride | HCID 7277 | — |
| Reactant | Propylene | HCID 8252 | — |
| Reactant | 5-Vinyl-2-norbornene | HCID 18273 | — |
| Reactant | HCID 178418361 | HCID 178418361 | — |
| Solvent | Hexane | HCID 8058 | — |
| Product | ethylene/propylene VNB | HCID 86599654 | — |
Reaction Steps
In a 100-liter stainless steel polymerization reactor equipped with a stirring blade (number of stirring revolutions: 250 rpm), terpolymerization of ethylene, propylene and 5-vinyl-2-norbornene was continuously carried out. To the liquid phase in the reactor were fed hexane at a rate of 60 l/hr, ethylene at a rate of 3.7 kg/hr, propylene at a rate of 8.0 kg/hr and 5-vinyl-2-norbornene at a rate of 480 g/hr, and were further continuously fed hydrogen at a rate of 50 l/hr and as catalysts VOCl3 at a rate of 48 mmol/hr, Al(Et)2Cl at a rate of 240 mmol/hr and Al(Et)1.5Cl1.5 at a rate of 48 mmol/hr, through the side inlet of the reactor.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|---|
| Patent number | US06864315B1 |
| Source dataset | uspto-grants-2005_03 |
| ORD ID | ord-5021612d7b2d4cffbe353a4588ed1fb5 |
| Source note | uspto-grants-2005_03 |