Method for producing clean low freezing point diesel oil by treating high nitrogen diesel oil
A diesel and clean technology, applied in the treatment of hydrocarbon oil, hydrotreating process, petroleum industry, etc., can solve the limitation of diesel fraction yield and pour point depressurization effect, reduce the service life of hydropour pour point depressant catalyst, and reduce the reaction temperature at the bed outlet. Advanced problems, to achieve good selective cracking performance, good isomerization performance, and the effect of lowering freezing point
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0043] use figure 1 The process flow shown is to produce low-condensation-point diesel oil by using gradation series and mixed packing process. In Example 1, two hydrogenation reaction zones connected in series are included, and in the composite bed of the depreciation catalyst in each reaction zone, the mixing volume ratio of the hydrogenation modified isomerization depreciation catalyst to the hydrogenation modified isomerization depreciation catalyst is 1:2 . The hydrorefining catalyst agent used in Example 1 is FF-36 catalyst, the hydrogenation modified isomerization depreciation catalyst is FC-14 catalyst, and the hydrodepreciation catalyst is FDW-3 catalyst, all of which are Fushun Petroleum A commercial catalyst developed and produced by the Chemical Research Institute.
[0044] The operating conditions and test results are listed in Table 3.
Embodiment 2
[0046] use figure 1The process flow shown is to produce low-condensation-point diesel oil by using gradation series and mixed packing process. In embodiment 1, two hydrogenation reaction zones connected in series are included, and in the composite depreciation catalyst bed of each reaction zone, the mixing volume ratio of the hydrogenation modified isomerization depreciation catalyst and the hydrogenation modified isomerization depreciation catalyst is 1:2 , The total amount of catalyst used is the same as that of Comparative Example 1 and Comparative Example 2. The hydromodified isomerization depreciation catalyst used in Example 2 was FC-14G catalyst, and the hydrodegradation catalyst was FDW-3 catalyst, both of which were commercial catalysts developed and produced by Fushun Petrochemical Research Institute.
[0047] The operating conditions and test results are listed in Table 3.
[0048] Table 2 Raw oil properties table.
[0049] project Raw oil source...
PUM
Property | Measurement | Unit |
---|---|---|
dew point | aaaaa | aaaaa |
dry point | aaaaa | aaaaa |
specific surface area | 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