Hydrogenation process and system for producing catalytically reformed raw material
A technology of catalytic reforming and raw materials, which is applied in the field of hydrocarbon oil cracking, can solve the problems of low yield of catalytic reforming raw materials and low latent content of aromatics, and achieve the effects of improving economic benefits of enterprises, reducing production costs and increasing selectivity
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0050] The mixed raw material of raw oil F and H enters the first hydrogenation reaction zone together with hydrogen, and reacts with the hydrofining catalyst A, and the reaction effluent enters the first high-pressure separator for gas-liquid separation, and the obtained first liquid phase stream enters The reaction is carried out in the second hydrogenation reaction zone equipped with the hydrocracking catalyst C, and the reaction product in the second hydrogenation reaction zone is recycled to the first high-pressure separator. The obtained first gas-phase stream enters the third hydrogenation reaction zone equipped with hydrocracking catalyst E for reaction, and the reaction effluent enters the second high-pressure separator, and the obtained second liquid-phase stream enters the fractionation tower to obtain light naphtha fraction , heavy naphtha fraction and diesel fraction, and the diesel fraction is returned to the third hydrogenation reaction zone for circulation conve...
Embodiment 2
[0054] The mixed raw material of raw oil G and H enters the first hydrogenation reaction zone together with hydrogen, and reacts with the hydrogenation catalyst B. The reaction effluent enters the first high-pressure separator for gas-liquid separation, and the obtained first liquid phase stream enters the The reaction is carried out in the second hydrogenation reaction zone equipped with the hydrocracking catalyst D, and the reaction product in the second hydrogenation reaction zone is recycled to the first high-pressure separator. The obtained first gas-phase stream enters the third hydrogenation reaction zone equipped with hydrocracking catalyst E for reaction, and the reaction effluent enters the second high-pressure separator, and the obtained second liquid-phase stream enters the fractionation tower to obtain light naphtha fraction , heavy naphtha fraction and diesel fraction, and the diesel fraction is returned to the third hydrogenation reaction zone for circulation con...
PUM
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