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

Distillation Unit Quiz Questions, November 3, 2017

2017-11-03View Original

Thread Content

What happens if the normal bottom injection steam volume is too high or too low?
Reply #22017-11-03
When an excessive amount of steam is introduced at the bottom, it increases the volume of steam rising inside the tower, which can cause the gas flow velocity within the tower to exceed the specified value and lead to tower flooding. This also increases the load on the top of the tower as well as on the condenser at the tower top. If the superheated steam volume is too low, the extraction yield at atmospheric pressure will be low; when the temperatures in the various side streams remain constant, the composition of the product will be leaner.
Reply #32017-11-03
When an excessive amount of steam is introduced at the bottom, it increases the volume of steam rising inside the tower, which can cause the gas flow velocity within the tower to exceed the specified value and lead to tower flooding. This also increases the load on the top of the tower as well as on the condenser at the tower top. If the superheated steam volume is too low, the yield at atmospheric pressure will be low; when the temperatures in various side streams remain constant, the composition of the product will be leaner
Reply #42017-11-03
When an excessive amount of steam is introduced at the bottom, it increases the volume of steam rising inside the tower, which can cause the gas flow velocity within the tower to exceed the specified value and lead to tower flooding. This also increases the load on the top of the tower as well as on the condenser at the tower top. If the superheated steam volume is too low, the extraction yield at atmospheric pressure will be low; when the temperatures in the various side streams remain constant, the composition of the product will be leaner.
Reply #52017-11-03
When an excessive amount of steam is introduced at the bottom, it increases the volume of steam rising inside the tower, which can cause the gas flow velocity within the tower to exceed the specified value and lead to tower flooding. This also increases the load on the top of the tower as well as on the condenser at the tower top. If the superheated steam volume is too low, the extraction yield at atmospheric pressure will be low; when the temperatures in the various side streams remain constant, the composition of the product will be leaner.
Reply #62017-11-03
When an excessive amount of steam is introduced at the bottom, it increases the volume of steam rising inside the tower, which can cause the gas flow velocity within the tower to exceed the specified value and lead to tower flooding. This also increases the load on the top of the tower as well as on the condenser at the tower top. If the superheated steam volume is too low, the extraction yield at atmospheric pressure will be low; when the temperatures in the various side streams remain constant, the composition of the product will be leaner.
Reply #72017-11-03
When an excessive amount of steam is introduced at the bottom, it increases the volume of steam rising inside the tower, which can cause the gas flow velocity within the tower to exceed the specified value and lead to tower flooding. This also increases the load on the top of the tower as well as on the condenser at the tower top. If the superheated steam volume is too low, the extraction yield at atmospheric pressure will be low; when the temperatures in the various side streams remain constant, the composition of the product will be leaner.
Reply #82017-11-03
When an excessive amount of steam is introduced at the bottom, it increases the volume of steam rising inside the tower, which can cause the gas flow velocity within the tower to exceed the specified value and lead to tower flooding. This also increases the load on the top of the tower as well as on the condenser at the tower top. If the superheated steam volume is too low, the extraction yield at atmospheric pressure will be low; when the temperatures in the various side streams remain constant, the composition of the product will be leaner.
Reply #92017-11-03
When an excessive amount of steam is introduced at the bottom, it increases the volume of steam rising inside the tower, which can cause the gas flow velocity within the tower to exceed the specified value and lead to tower flooding. This also increases the load on the top of the tower as well as on the condenser at the tower top. If the superheated steam volume is too low, the extraction yield at atmospheric pressure will be low; when the temperatures in the various side streams remain constant, the composition of the product will be leaner.
Reply #102017-11-03
When an excessive amount of steam is introduced at the bottom, it increases the volume of steam rising inside the tower, which can cause the gas flow velocity within the tower to exceed the specified value and lead to tower flooding. This also increases the load on the top of the tower as well as on the condenser at the tower top. If the superheated steam volume is too low, the extraction yield at atmospheric pressure will be low; when the temperatures in the various side streams remain constant, the composition of the product will be leaner.
Reply #112017-11-03
When an excessive amount of steam is introduced at the bottom, it increases the volume of steam rising inside the tower, which can cause the gas flow velocity within the tower to exceed the specified value and lead to tower flooding. This also increases the load on the top of the tower as well as on the condenser at the tower top. If the superheated steam volume is too low, the extraction yield at atmospheric pressure will be low; when the temperatures in the various side streams remain constant, the composition of the product will be leaner.

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.