A continuous liquid-phase diesel hydrotreating method
A liquid-phase hydrogenation and hydrogenation treatment technology, applied in refining to remove heteroatoms, etc., can solve problems such as poor catalyst stability, achieve good stability, high hydrogen utilization rate, good hydrogenation performance and stability
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0044] A Middle Eastern high-sulfur straight-run diesel fraction is used as feedstock 1, feedstock 1 is mixed with reactor effluent and hydrogen at a pressure of 8.2MPa, and the mixed material is introduced into the reactor equipped with hydrorefining catalyst D1, The deep hydrodesulfurization reaction is carried out here, and the reaction conditions are: reaction temperature 360°C, reactor pressure 8.0MPa, raw oil liquid hourly volume space velocity 1.5h -1 . The reactor is evenly divided into three beds, and at the outlet of the two beds, the hydrogen concentration in the flow in the reactor is measured to be 2×10 -4 g H 2 / g, the flow in the reactor and the hydrogen introduced from the outside enter the second mixer between the 2nd bed and the 3rd bed for mixing, and then enter the 3rd bed to continue the reaction, and the reaction is measured at the outlet of the 1st bed The concentration of hydrogen in the stream in the device is greater than 5×10 -4 g H 2 / g, so ther...
Embodiment 2
[0060] A secondary processing catalytic cracking diesel fraction is feed oil 2, feed oil 2 is mixed with reactor effluent and hydrogen at a pressure of 10.2MPa, and the mixed material is introduced into the reactor equipped with supported hydrofining catalyst D1 The deep hydrodesulfurization reaction is carried out in the middle, the reaction conditions are: reaction temperature 370 ℃, reactor pressure 10.0MPa, raw material oil liquid hourly volume space velocity 1.2h -1 . The reactor is evenly divided into five beds, and the hydrogen concentration in the stream in the reactor is measured at the outlet of the first bed to be 5×10 -4 g H 2 / g, the stream in the reactor and the hydrogen are mixed in the first mixer, and then enter the 2-bed layer for reaction; the hydrogen concentration in the stream in the reactor is measured at the outlet of the 2-bed layer as 8×10 -4 g H 2 / g, the concentration of hydrogen in the stream in the reactor was measured at the outlet of the 3-be...
PUM
Property | Measurement | Unit |
---|---|---|
concentration | aaaaa | aaaaa |
water absorption | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com