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

Newbie simulation

2017-05-10View Original

Thread Content

*** SEVERE ERROR: THE MATERIAL AND ENERGY BALANCES COULD NOT BE CONVERGED; CHECK THE COLUMN SPECIFICATIONS OR PROVIDE BETTER ESTIMATIONS FOR TEMPERATURE AND COMPOSITION. *** SEVERE ERROR: THE FOLLOWING STAGES EXPERIENCED DRYING OUT: 1 A LIMIT OF 0.10000E-04 * SUM OF FEEDS WAS IMPOSED ON THE FLOW RATES. ** ERROR: BLOCK T101 IS NOT IN MASS BALANCE; MASS INLET FLOW = 0.15539748E+03, MASS OUTLET FLOW = 0.20448186E+03, RELATIVE DIFFERENCE = 0.31586339E+00 * WARNING: STREAM 102 IS NOT IN CHARGE BALANCE; ANION FLOW = -.17212081E+00, CATION FLOW = 0.10085429E+00, ABSOLUTE DIFFERENCE = -.71266524E-01, RELATIVE DIFFERENCE = -.70662861E+00
Reply #22017-05-12
Thank you, I’ve found a solution.
Reply #32019-12-16
Hero, how was the problem solved? I hope you can give some advice

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.