HCBBS Forum (English)
Submit Chemical Projects / Find Solutions
Amplify Your Requirements on a Broader Chemical Platform *Engineering · Technology · Equipment · Solutions*
Submit Request

Corrosion of catalytic devices

2011-10-12View Original

Thread Content

Corrosion of the catalytic device, types of corrosion that occur, and locations. Let’s discuss whether there is naphthenic acid corrosion
Reply #22011-10-13
Settler: High-temperature sulfur corrosion; Sliding valve, regenerator internals, regenerator outlet pipeline: cracking due to polysulfuric acid ; Waste heat boiler: erosion, condensate corrosion, stress cracking ; Bottom of distillation tower: high-temperature sulfur corrosion ; Top of distillation tower: Ammonium chloride corrosion, low-temperature hydrogen sulfide corrosion ; Stirring tower: high-temperature sulfur corrosion, ammonium chloride corrosion ; Compressor inlet pipeline: wet hydrogen sulfide corrosion, ammonium chloride corrosion ; Stability: Wet hydrogen sulfide injury ; Naphthenic acid is affected by temperature as follows: at 400°C, petroleum acid decomposes and corrosion decreases. Therefore, it is believed that naphthenic acid decomposes, and there is no corrosion caused by naphthenic acid under catalytic conditions.

Submit a Project

**Looking for Chemical Technology, Equipment & Solutions?** No Registration Required Broader Platform Exposure | Global Chemical Service Provider Connections

Submit Request — Free Consultation

Disclaimer

This is an automated machine translation of the original thread. Some technical terms may have inaccuracies; the original text shall prevail. Click "View Original" at the top right to access the source page, which supports IP-based automatic real-time language translation. Please watch out for contact details and sales inducements to prevent fraud. All content and translations are for reference only, representing solely the poster's personal views. For enquiries, email service@hcbbs.com.