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

Temperature of hot hydrogen with oil in reformation pre-hydrogenation zone

2017-01-10View Original

Thread Content

When we go out for training*, the temperature of the hot hydrogen with oil in the pre-hydrogenation zone is set at 260 degrees. Right? I think it needs to be over 300 degrees. And what determines the temperature of hot hydrogen with oil?
Reply #22017-01-11
On my end, I keep it around 275. Under certain pressure conditions, the impurity content in the refined oil serves as a basis for determining the pre-hydrogenation temperature; the impurities include olefins, halogens, and metals
Reply #32017-01-11
Do you mean the temperature of hot hydrogen with oil, from the furnace outlet to the reactor?
Reply #42017-01-11
260 degrees is sufficient; we use 250 degrees, as long as the oil can fully vaporize at that pressure
Reply #52017-01-11
When the temperature is high and there is oil present, the catalyst in its sulfided state can be reduced over time; therefore, it is advisable to keep the temperature of hot hydrogen with oil at 200°C and not to allow more than 24 hours to pass. Catalysts from different manufacturers also have different requirements
Reply #62017-01-12
A oil temperature of 260 degrees is sufficient
Reply #72017-01-12
Is hot hydrogen used for oil removal, meaning that feeding is stopped during pre-hydrogenation and hydrogen is used to remove the oil?
Reply #82017-02-06
In our plant, the temperature for pre-hydrogenation with hot hydrogen and oil present is 180 degrees, and the process takes 4 hours. Excessively high temperatures pose a risk of catalyst reduction.
Reply #92017-02-17
In our plant’s reforming unit, the temperature of the hot hydrogen containing oil during pre-hydrogenation is generally controlled by setting the outlet temperature of the heater at 280°C. If this temperature is too high, it can have an adverse effect on the pre-hydrogenation catalyst. It is also necessary to pay attention to the amount of hydrogen supplied, as well as to control the pressure in the high-pressure tank – this helps to ensure an adequate amount of hydrogen circulating in the system and prevents coking of the catalyst. The oil-containing principle states that the liquid level in the high-pressure tank should no longer rise; generally, this is achieved after about 4 hours.

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.