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

Issues with sep separation

2009-11-09View Original

Thread Content

This post was last edited by wyaiyzh on 2009-11-10 at 20:17. Thank you very much to everyone; I couldn’t figure it out. I’m using sep to simulate the desulfurization process simply, with the outlet being clean gas and acid gas. The acid gas is supposed to contain 95% H2S, 95% COS, and 0.15% CO2. I’ve set these split fractions for the acid gas, but I’m encountering an issue: “For each stream but one, split fraction or flow must be specified for at least one component in each substream.” What should I do?
Reply #22009-11-09
As the original poster said, have you defined both the clean gas and acid gas streams at the outlet? It’s sufficient to define the composition of the components in one of these streams; the composition of the other stream will be clear automatically, so there’s no need to define it I tried it, and there were no problems!
Reply #32009-11-09
The answer above is correct; for the sep model, it is sufficient to set one of the logistics components at x%, with the other component being 1-x%
Reply #42009-11-09
0049 2# wuwawa Thank you~ I just defined one. There’s no problem when calculating separately, but issues arise once they are connected. I don’t know why; I’ll try adjusting it again.
Reply #52009-11-10
It’s fixed; it turns out that for some components I thought didn’t exist, no definition was provided. All components in a logistics must be fully defined. It’s actually quite simple; I just held back for such a long time. Thank you all for your help!

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.