The reaction kinetics of ethylene oligomerization was investigated over the temperature range 278-323 K and near-atmospheric pressure in a laboratory slurry reactor. The nickel/sulfated alumina catalyst was prepared by use of a non-porous fumed alumina (ALON TM) support and by ion-exchange thereon o
Oligomerization of Ethene In a Slurry Reactor Using a Nickel(II)-Exchanged Silica–Alumina Catalyst
✍ Scribed by Michael D Heydenrych; Christakis P Nicolaides; Michael S Scurrell
- Book ID
- 112256255
- Publisher
- Elsevier Science
- Year
- 2001
- Tongue
- English
- Weight
- 126 KB
- Volume
- 197
- Category
- Article
- ISSN
- 0021-9517
No coin nor oath required. For personal study only.
📜 SIMILAR VOLUMES
A novel slurry reactor was used to investigate the copolymerization behavior of ethylene and 1-butene in the presence of 1 wt % Cr on Davison silica (Phillips-type) catalyst over the temperature range of O-5O0C, space velocity of about 0.0051 [m3 (STP)]/(g of catalyst) h, and a fixed ethylene to 1-b
Kinetics of hydration of propylene oxide using an ion-exchange msin catalyst in a slurry reactor was studied. The kinetics of homogeneous, uncatalyzed reaction was studied separately and used to obtain heterogeneous reaction kinetics. The homogeneous reaction was found to be 0.43 order with respect