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

Problems with cascade control

2017-10-01View Original

Thread Content

We have some issues with our cascade control systems and need everyone’s help. First, there are two cascade controls; after the outer-loop cascade is activated, the MV value does not change in response to changes in the PV value, remaining at a constant level. The outer ring represents temperature, while the inner ring represents flow rate. After introducing the cascade control, whether the temperature rises or falls. The outer loop MV value remains constant, which causes the inner loop SV value to remain unchanged as well. It cannot be adjusted. Second, there is a cascade control system: the outer loop functions normally, but the MV value of the inner loop does not reach 0 when the SV value does. Is this related to the fact that there is still some flow when the valve is open by about 10 percent? I appreciate your help. Thank you
Reply #22017-10-02
Configure and take a photo – any issues during debugging?

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.