Hydrogenation modification method of distillate oil
A technology of hydrogenation upgrading and distillate oil, which is applied in the fields of hydrotreating process, petroleum industry, and hydrocarbon oil treatment, etc. It can solve the problems of high cost, high operating cost, and low space velocity, and achieve low investment and operating costs , Improve conversion depth, increase the effect of cetane number
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0036] After the raw material oil A is mixed with hydrogen, it contacts and reacts with the hydrogenation upgrading catalyst C in the first hydrogenation reaction zone, and the reaction product directly enters the second hydrogenation reaction zone without separation, and reacts under the action of the hydrofinishing catalyst I , the reaction effluent in the second hydrogenation reaction zone is cooled, separated and fractionated to obtain a diesel fraction and a naphtha fraction, and the loading volume ratio of the hydrogenation upgrading catalyst and the hydrofinishing catalyst I is 3:1, and the specific reaction conditions As shown in Table 2, the main product properties are shown in Table 3.
[0037] It can be seen from Table 3 that the density of the diesel fraction is 0.8569g / cm 3 , the sulfur content is less than 50 μg / g, the polycyclic aromatic hydrocarbon content is 3.4% by weight, and the cetane number is 38.7. Compared with the raw material, the cetane number is inc...
Embodiment 2
[0039] After the raw material oil A is mixed with hydrogen, it contacts and reacts with the hydrogenation upgrading catalyst C in the first hydrogenation reaction zone, and the reaction product directly enters the second hydrogenation reaction zone without separation, and reacts under the action of the hydrogenation refining catalyst II , the reaction effluent in the second hydrogenation reaction zone is cooled, separated and fractionated to obtain a diesel fraction and a naphtha fraction, and the loading volume ratio of the hydrogenation upgrading catalyst and the hydrofinishing catalyst I is 2:1, and the specific reaction conditions As shown in Table 2, the main product properties are shown in Table 3.
[0040] It can be seen from Table 3 that the density of the diesel fraction is 0.8506g / cm 3 , the sulfur content is less than 50 μg / g, the polycyclic aromatic hydrocarbon content is 2.4% by weight, and the cetane number is 42.3. Compared with the raw material, the cetane numb...
Embodiment 3
[0042] After the raw material oil B is mixed with hydrogen, it contacts and reacts with the hydrogenation upgrading catalyst C in the first hydrogenation reaction zone, and the reaction product directly enters the second hydrogenation reaction zone without separation, and reacts under the action of the hydrofinishing catalyst I , the reaction effluent in the second hydrogenation reaction zone is cooled, separated and fractionated to obtain a diesel fraction and a naphtha fraction, and the loading volume ratio of the hydroreforming catalyst and the hydrofinishing catalyst I is 4:1, and the specific reaction conditions As shown in Table 2, the main product properties are shown in Table 3.
[0043] It can be seen from Table 3 that the density of the diesel fraction is 0.8806g / cm 3 , the sulfur content is less than 50 μg / g, the polycyclic aromatic hydrocarbon content is 7.9% by weight, and the cetane number is 33.2. Compared with the raw material, the cetane number is increased by...
PUM
| Property | Measurement | Unit |
|---|---|---|
| boiling point | aaaaa | aaaaa |
| density | aaaaa | aaaaa |
| density | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More - R&D
- Intellectual Property
- Life Sciences
- Materials
- Tech Scout
- Unparalleled Data Quality
- Higher Quality Content
- 60% Fewer Hallucinations
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2025 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com
