Oligomerisation of olefins with zeolite catalyst
US8742192B2 · kind B2 · utility
Assignee
Inventors
Key dates
| Filing date | Jun 16, 2006 |
| Grant date | Jun 3, 2014 |
| Priority date | — |
| Expiry date | Jul 22, 2030 |
Classification
- Technology area (CPC B)Performing Operations; Transporting
- CPC primaryB01J2219/00245
- WIPO fieldOrganic fine chemistry
- WIPO sectorChemistry
Abstract
The conversion and run length for oligomerization of olefins over a molecular sieve catalyst in a tubular reactor is improved by controlling the peak temperature to not exceed 50 degrees C. above the temperature of the temperature control fluid exiting the shell side outlet of the reactor. A tubular reactor containing molecular sieve catalyst is provided with a multipoint thermocouple in at least one tube, and optionally with a bottom design adapted for fast unloading of the molecular sieve catalyst from the tubular reactor.
Source: USPTO / EPO open patent data. Objective bibliographic and citation counts.