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

Desulfurization issue

2017-04-16View Original

Thread Content

The coke oven gas purification process consists of cold drumming, desulfurization, ammonium sulfide production, and benzene extraction. The desulfurization process employs a wet desulfurization method, which falls under pre-desulfurization. The hydrogen sulfide concentration at the outlet of the desulfurization section (at the exit of the desulfurization tower) is no more than 10 milligrams per cubic meter; at the inlet of the ammonium sulfate production section, it is 20 milligrams per cubic meter, while it is 100 milligrams per cubic meter after the ammonium sulfate production section and after the benzene washing section. Why is there a difference of 10 times between the hydrogen sulfide levels analyzed after the desulfurization section and those analyzed after the benzene washing section? What is the reason for this? How to solve this problem? I would appreciate it if experts could provide some insights

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.