Engineering & Design
Integrating fire and gas safety with process control systems: Why, what and how
If a fire, smoke or gas leak is detected in a hydrocarbon processing facility, prescriptive actions must be taken by the fire and gas (F&G) safety system, as well as by the process control system (PCS), to mitigate and control the hazard.
Built-up backpressure at the outlet flange of a pressure relief valve
Even for pressure relief valves (PRVs) discharging directly to the atmosphere through short tailpipes, API 520 Part 11 warns that choked flow may develop at the outlet flange, resulting in high backpressure.
Reliability: How application engineers add value
Making the vendor-manufacturer your technology provider has been our consistent advice to the user industries; we have recommended this highly effective approach for many decades.
Process safety as a profit center?
In today’s economic environment, new capital spending is harder to find than loose change buried under the couch cushions.
Hydrocarbon Processing Awards
<i>Hydrocarbon Processing,</i> the downstream processing sector’s leading technical publication, has announced the winners for its second annual awards.
Getting onboard with modernization
While electrical equipment typically has a lengthy lifespan, it is not meant to last, or be relevant, forever.
A game-changing approach to furnace safeguarding
This work is a follow-up article to “Automate furnace controls to improve safety and energy efficiency,” which was published in the June 2014 edition of <i>Hydrocarbon Processing.</i>
Technical considerations for the Heydar Aliyev refinery revamp
The following case study describes the early development phases of SOCAR’s ongoing major revamp project at the Heydar Aliyev Refinery (HAR) in Baku, Azerbaijan, and its interface with the associated Azerikimya (AZK) steam cracking complex near Sumgait. References are made to the related SOCAR polymer project in Sumgayit, as well.
Additive solutions to SOx emissions in FCCUs
Sulfur oxide additives are typically based on hydrotalcite or magnesium aluminate spinel-type structures. Magnesium alumina is the pickup agent present in the most effective SO<sub>x</sub> additives on the market; therefore, to optimize SO<sub>x</sub> reduction, it is critical to maximize the amount of the critical magnesium component in the fluid catalytic cracking unit (FCCU) in an efficient and cost-effective way.
- bp's Whiting refinery union workers reject contract extension 2/2
- China's CNPC set to restart Dalian refinery to process Russian oil 2/2
- Dow announces 2029 startup of Phase 1 of its $7.5-B Path2Zero ethylene project 2/2
- ExxonMobil, Chevron see glimmer of Venezuela's potential, especially in refining its crude 2/2
- Valero Energy Q4 profit beats estimates; shares surge 1/30
- Dow launches "Transform to Outperform" to raise the competitive industry benchmark for productivity and growth to enable improved returns 1/30
