January 2018
Process Control and Instrumentation
Migrating from Fortran to ISA S-88
A major refiner operates two catalytic reforming units for gasoline octane improvement and aromatics production in Texas. In each of these units, five reactors filled with catalyst are operated continuously in series to reform paraffinic hydrocarbons in the presence of hydrogen (H2). During this process, some byproduct coke is unavoidably produced and deposits on the catalyst, which leads to gradual catalyst deactivation.
This is a preview of our premium content. Thank you for your interest—please log in or subscribe to read the full article.
The Authors
Related Articles
- Best practices to achieve highest integrity isolation for black powder-generated gas processes
- Innovative grassroots CDU-VDU configuration: Pioneering energy efficiency and net-zero pathways in modern refineries
- Improving isolation valve reliability in delayed coker units: Field experience-driven design enhancements


Comments